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	<title>Fluids, Vol. 11, Pages 161: Experimental and Numerical Investigation of an Integrated Fan-Driven Co-Flow Jet System for a High-Performance Automotive Rear Wing</title>
	<link>https://www.mdpi.com/2311-5521/11/6/161</link>
	<description>This study investigates the application of the Co-Flow Jet (CFJ) active flow-control methodology to an automotive rear wing through a combined CFD and experimental campaign conducted on a modified McLaren 765LT. The work evaluates the aerodynamic response, energy performance, and practical integration of embedded Co-Flow systems under representative on-track conditions. An extensive CFD design campaign assessed multiple Co-Flow architectures, from which three representative configurations incorporating embedded ducted axial fans were selected for experimental testing. The results indicate that aerodynamic performance is strongly influenced by the interaction between momentum injection, vehicle conditions, and duct architecture. The most effective configuration achieved drag reductions of up to 9% together with downforce increases of approximately 15% under highly loaded conditions, significantly exceeding the repeatability levels of the measurements. The efficiency analysis further showed that, under selected operating conditions, the aerodynamic benefits obtained from the Co-Flow system can exceed the electrical power required by the actuation system. However, increased mass-flow capability alone was not found to guarantee improved aerodynamic performance or efficiency. The results demonstrate the successful integration and operation of a fan-driven Co-Flow system on a production-based vehicle and highlight the importance of momentum injection level and duct design. The findings should be interpreted within the scope of the investigated vehicle and operating envelope. Due to confidentiality constraints, part of the absolute aerodynamic data could not be disclosed, and the results are therefore presented primarily as relative variations.</description>
	<pubDate>2026-06-22</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 161: Experimental and Numerical Investigation of an Integrated Fan-Driven Co-Flow Jet System for a High-Performance Automotive Rear Wing</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/161">doi: 10.3390/fluids11060161</a></p>
	<p>Authors:
		Marco Robert Herberg
		Guglielmo Luca Bambino
		Stefano De Pinto
		Giuseppe Pascazio
		Marco Donato de Tullio
		</p>
	<p>This study investigates the application of the Co-Flow Jet (CFJ) active flow-control methodology to an automotive rear wing through a combined CFD and experimental campaign conducted on a modified McLaren 765LT. The work evaluates the aerodynamic response, energy performance, and practical integration of embedded Co-Flow systems under representative on-track conditions. An extensive CFD design campaign assessed multiple Co-Flow architectures, from which three representative configurations incorporating embedded ducted axial fans were selected for experimental testing. The results indicate that aerodynamic performance is strongly influenced by the interaction between momentum injection, vehicle conditions, and duct architecture. The most effective configuration achieved drag reductions of up to 9% together with downforce increases of approximately 15% under highly loaded conditions, significantly exceeding the repeatability levels of the measurements. The efficiency analysis further showed that, under selected operating conditions, the aerodynamic benefits obtained from the Co-Flow system can exceed the electrical power required by the actuation system. However, increased mass-flow capability alone was not found to guarantee improved aerodynamic performance or efficiency. The results demonstrate the successful integration and operation of a fan-driven Co-Flow system on a production-based vehicle and highlight the importance of momentum injection level and duct design. The findings should be interpreted within the scope of the investigated vehicle and operating envelope. Due to confidentiality constraints, part of the absolute aerodynamic data could not be disclosed, and the results are therefore presented primarily as relative variations.</p>
	]]></content:encoded>

	<dc:title>Experimental and Numerical Investigation of an Integrated Fan-Driven Co-Flow Jet System for a High-Performance Automotive Rear Wing</dc:title>
			<dc:creator>Marco Robert Herberg</dc:creator>
			<dc:creator>Guglielmo Luca Bambino</dc:creator>
			<dc:creator>Stefano De Pinto</dc:creator>
			<dc:creator>Giuseppe Pascazio</dc:creator>
			<dc:creator>Marco Donato de Tullio</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060161</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-22</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-22</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>161</prism:startingPage>
		<prism:doi>10.3390/fluids11060161</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/161</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
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        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/160">

	<title>Fluids, Vol. 11, Pages 160: Irreversibility Analysis in the Tapered Wavy Wall of a Tubular Non-Newtonian Nanofluid with Gyrotactic Microorganisms</title>
	<link>https://www.mdpi.com/2311-5521/11/6/160</link>
	<description>This research analyzes the wavy, axisymmetric flow of a Ree&amp;amp;ndash;Eyring non-Newtonian nanofluid, infused with motile microorganisms, within a porous, tapered cylindrical channel under a transverse magnetic field. This investigation presents a theoretical framework that may inform the improvement of energy efficiency and thermal management in biomedical engineering applications, such as drug delivery systems and microfluidic biosensors. The work provides an extended insight by a contribution to the evaluation of entropy generation, explicitly considering the influence of motile microorganisms, thereby bridging a gap in the existing literature. The comprehensive physical model further incorporates the combined effects of Joule heating, viscous dissipation, nonlinear thermal radiation, and chemical reactions. Methodologically, the governing nonlinear equations of the system were rendered tractable under long-wavelength and low-Reynolds-number assumptions and subsequently solved using the numerical Runge&amp;amp;ndash;Kutta&amp;amp;ndash;Fehlberg technique. The key conclusion is that, based on the present numerical model, careful selection of magnetic field strength and microorganism motility parameters may reduce irreversible energy losses, potentially improving the net usable work in advanced nanofluid transport systems for biomedical applications, subject to experimental validation. The most significant finding reveals that the magnetic field serves as a dual-purpose control parameter: increasing its strength boosts total entropy generation by 20&amp;amp;ndash;30% while simultaneously raising the Bejan number, confirming heat transfer as the dominant irreversibility mechanism in the system. Additionally, nanoparticle concentration diminishes substantially with elevated chemical reaction rates and Schmidt numbers, while microorganism density is highly sensitive to the P&amp;amp;eacute;clet number, which causes flow disruptions.</description>
	<pubDate>2026-06-21</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 160: Irreversibility Analysis in the Tapered Wavy Wall of a Tubular Non-Newtonian Nanofluid with Gyrotactic Microorganisms</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/160">doi: 10.3390/fluids11060160</a></p>
	<p>Authors:
		Khaled Elagamy
		</p>
	<p>This research analyzes the wavy, axisymmetric flow of a Ree&amp;amp;ndash;Eyring non-Newtonian nanofluid, infused with motile microorganisms, within a porous, tapered cylindrical channel under a transverse magnetic field. This investigation presents a theoretical framework that may inform the improvement of energy efficiency and thermal management in biomedical engineering applications, such as drug delivery systems and microfluidic biosensors. The work provides an extended insight by a contribution to the evaluation of entropy generation, explicitly considering the influence of motile microorganisms, thereby bridging a gap in the existing literature. The comprehensive physical model further incorporates the combined effects of Joule heating, viscous dissipation, nonlinear thermal radiation, and chemical reactions. Methodologically, the governing nonlinear equations of the system were rendered tractable under long-wavelength and low-Reynolds-number assumptions and subsequently solved using the numerical Runge&amp;amp;ndash;Kutta&amp;amp;ndash;Fehlberg technique. The key conclusion is that, based on the present numerical model, careful selection of magnetic field strength and microorganism motility parameters may reduce irreversible energy losses, potentially improving the net usable work in advanced nanofluid transport systems for biomedical applications, subject to experimental validation. The most significant finding reveals that the magnetic field serves as a dual-purpose control parameter: increasing its strength boosts total entropy generation by 20&amp;amp;ndash;30% while simultaneously raising the Bejan number, confirming heat transfer as the dominant irreversibility mechanism in the system. Additionally, nanoparticle concentration diminishes substantially with elevated chemical reaction rates and Schmidt numbers, while microorganism density is highly sensitive to the P&amp;amp;eacute;clet number, which causes flow disruptions.</p>
	]]></content:encoded>

	<dc:title>Irreversibility Analysis in the Tapered Wavy Wall of a Tubular Non-Newtonian Nanofluid with Gyrotactic Microorganisms</dc:title>
			<dc:creator>Khaled Elagamy</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060160</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-21</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-21</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>160</prism:startingPage>
		<prism:doi>10.3390/fluids11060160</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/160</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
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        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/159">

	<title>Fluids, Vol. 11, Pages 159: A Comprehensive Review of Numerical Simulations on Vortex-Induced Vibration Response Characteristics of Deep-Sea Risers</title>
	<link>https://www.mdpi.com/2311-5521/11/6/159</link>
	<description>As core structural components for deep-sea oil and gas exploitation, deep-sea risers are continuously subjected to wind, wave, and current loads, which readily induce vortex-induced vibration (VIV) and further trigger structural fatigue damage. Furthermore, the progressive exploitation of deepwater and ultra-deepwater oil and gas resources has exacerbated the complexity and risk of riser VIV, rendering it a critical engineering problem that urgently requires effective solutions. This paper presents a comprehensive review of numerical studies on deep-sea riser VIV, systematically elaborating the fundamental principles, research advances, and application scenarios of three mainstream numerical approaches: semi-empirical models, computational fluid dynamics (CFD) models, and computational structural dynamics (CSD) models. The respective accuracy advantages and inherent limitations of each numerical method are thoroughly analyzed. Additionally, this review focuses on key research hotspots and challenging issues, including VIV responses of flexible risers, dynamic fluid&amp;amp;ndash;structure boundary coupling, internal&amp;amp;ndash;external flow coupling effects, wake interference of multi-riser systems, efficient VIV prediction, and vibration suppression optimization. The current technical bottlenecks in existing research are clarified. This study aims to provide a systematic theoretical framework and methodological reference for subsequent numerical investigations and engineering applications of riser VIV, and offer technical support for the optimal structural design and safety risk prevention of deep-sea riser systems.</description>
	<pubDate>2026-06-21</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 159: A Comprehensive Review of Numerical Simulations on Vortex-Induced Vibration Response Characteristics of Deep-Sea Risers</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/159">doi: 10.3390/fluids11060159</a></p>
	<p>Authors:
		Xiangquan Li
		Renwei Ji
		Ho-Seong Yang
		Yuquan Zhang
		Ratthakrit Reabroy
		Peng Dou
		Linfeng Chen
		Lixin Xu
		</p>
	<p>As core structural components for deep-sea oil and gas exploitation, deep-sea risers are continuously subjected to wind, wave, and current loads, which readily induce vortex-induced vibration (VIV) and further trigger structural fatigue damage. Furthermore, the progressive exploitation of deepwater and ultra-deepwater oil and gas resources has exacerbated the complexity and risk of riser VIV, rendering it a critical engineering problem that urgently requires effective solutions. This paper presents a comprehensive review of numerical studies on deep-sea riser VIV, systematically elaborating the fundamental principles, research advances, and application scenarios of three mainstream numerical approaches: semi-empirical models, computational fluid dynamics (CFD) models, and computational structural dynamics (CSD) models. The respective accuracy advantages and inherent limitations of each numerical method are thoroughly analyzed. Additionally, this review focuses on key research hotspots and challenging issues, including VIV responses of flexible risers, dynamic fluid&amp;amp;ndash;structure boundary coupling, internal&amp;amp;ndash;external flow coupling effects, wake interference of multi-riser systems, efficient VIV prediction, and vibration suppression optimization. The current technical bottlenecks in existing research are clarified. This study aims to provide a systematic theoretical framework and methodological reference for subsequent numerical investigations and engineering applications of riser VIV, and offer technical support for the optimal structural design and safety risk prevention of deep-sea riser systems.</p>
	]]></content:encoded>

	<dc:title>A Comprehensive Review of Numerical Simulations on Vortex-Induced Vibration Response Characteristics of Deep-Sea Risers</dc:title>
			<dc:creator>Xiangquan Li</dc:creator>
			<dc:creator>Renwei Ji</dc:creator>
			<dc:creator>Ho-Seong Yang</dc:creator>
			<dc:creator>Yuquan Zhang</dc:creator>
			<dc:creator>Ratthakrit Reabroy</dc:creator>
			<dc:creator>Peng Dou</dc:creator>
			<dc:creator>Linfeng Chen</dc:creator>
			<dc:creator>Lixin Xu</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060159</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-21</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-21</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Review</prism:section>
	<prism:startingPage>159</prism:startingPage>
		<prism:doi>10.3390/fluids11060159</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/159</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/158">

	<title>Fluids, Vol. 11, Pages 158: Modeling of Soluble and Biodegradable Contaminant Transport in Channels and Rivers</title>
	<link>https://www.mdpi.com/2311-5521/11/6/158</link>
	<description>Accurate prediction of contaminant transport and self-purification processes in rivers remains challenging because pollutant dispersion, biochemical reactions, and hydrodynamic conditions interact across multiple spatial scales. This study aims to develop and compare mathematical models for soluble contaminant transport and biodegradable organic matter removal in channels and rivers. Unsteady advection&amp;amp;ndash;diffusion&amp;amp;ndash;reaction equations were formulated for one-dimensional (1D), two-dimensional (2D), and three-dimensional (3D) transport scenarios and solved through numerical techniques based on the transformation of partial differential equations into systems of ordinary differential or algebraic equations. In parallel, the classical Streeter&amp;amp;ndash;Phelps model and an extended formulation incorporating turbulent diffusion were implemented to evaluate organic load degradation and oxygen deficit dynamics. Simulations were performed using a Matlab R2019a-based computational framework under representative hydraulic and reaction conditions obtained from literature data and empirical correlations. The results showed that, under specific conditions, the 3D model reproduced trends comparable to those predicted by the 2D model, while the latter approached the behavior of the 1D formulation. The Streeter&amp;amp;ndash;Phelps model predicted an organic load removal efficiency of 97.74%, a purification index of 1.9564, a critical time of 18.43 h, and a critical distance of 6.93 km. These findings provide a useful framework for river water-quality assessment and support future applications involving complex hydrodynamic and pollutant-loading scenarios.</description>
	<pubDate>2026-06-20</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 158: Modeling of Soluble and Biodegradable Contaminant Transport in Channels and Rivers</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/158">doi: 10.3390/fluids11060158</a></p>
	<p>Authors:
		Luis Américo Carrasco-Venegas
		Juan Taumaturgo Medina-Collana
		Luz Genara Castañeda-Pérez
		Aurelio Carrasco-Venegas
		Daril Giovanni Martínez-Hilario
		José Vulfrano González-Fernández
		César Gutiérrez-Cuba
		Héctor Ricardo Cuba-Torre
		Lia Elis Concepción-Gamarra
		Rodolfo Paz-Salazar
		Salvador Apolinar Trujillo-Pérez
		</p>
	<p>Accurate prediction of contaminant transport and self-purification processes in rivers remains challenging because pollutant dispersion, biochemical reactions, and hydrodynamic conditions interact across multiple spatial scales. This study aims to develop and compare mathematical models for soluble contaminant transport and biodegradable organic matter removal in channels and rivers. Unsteady advection&amp;amp;ndash;diffusion&amp;amp;ndash;reaction equations were formulated for one-dimensional (1D), two-dimensional (2D), and three-dimensional (3D) transport scenarios and solved through numerical techniques based on the transformation of partial differential equations into systems of ordinary differential or algebraic equations. In parallel, the classical Streeter&amp;amp;ndash;Phelps model and an extended formulation incorporating turbulent diffusion were implemented to evaluate organic load degradation and oxygen deficit dynamics. Simulations were performed using a Matlab R2019a-based computational framework under representative hydraulic and reaction conditions obtained from literature data and empirical correlations. The results showed that, under specific conditions, the 3D model reproduced trends comparable to those predicted by the 2D model, while the latter approached the behavior of the 1D formulation. The Streeter&amp;amp;ndash;Phelps model predicted an organic load removal efficiency of 97.74%, a purification index of 1.9564, a critical time of 18.43 h, and a critical distance of 6.93 km. These findings provide a useful framework for river water-quality assessment and support future applications involving complex hydrodynamic and pollutant-loading scenarios.</p>
	]]></content:encoded>

	<dc:title>Modeling of Soluble and Biodegradable Contaminant Transport in Channels and Rivers</dc:title>
			<dc:creator>Luis Américo Carrasco-Venegas</dc:creator>
			<dc:creator>Juan Taumaturgo Medina-Collana</dc:creator>
			<dc:creator>Luz Genara Castañeda-Pérez</dc:creator>
			<dc:creator>Aurelio Carrasco-Venegas</dc:creator>
			<dc:creator>Daril Giovanni Martínez-Hilario</dc:creator>
			<dc:creator>José Vulfrano González-Fernández</dc:creator>
			<dc:creator>César Gutiérrez-Cuba</dc:creator>
			<dc:creator>Héctor Ricardo Cuba-Torre</dc:creator>
			<dc:creator>Lia Elis Concepción-Gamarra</dc:creator>
			<dc:creator>Rodolfo Paz-Salazar</dc:creator>
			<dc:creator>Salvador Apolinar Trujillo-Pérez</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060158</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-20</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-20</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>158</prism:startingPage>
		<prism:doi>10.3390/fluids11060158</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/158</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/157">

	<title>Fluids, Vol. 11, Pages 157: Flow Control Techniques: Advances in Flow System Analysis, Modeling and Applications</title>
	<link>https://www.mdpi.com/2311-5521/11/6/157</link>
	<description>Flow control has assumed a key role in many applied aspects of fluid dynamics andpropulsion in efforts toward CO2-neutral growth in air, ground and maritime transportation [...]</description>
	<pubDate>2026-06-20</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 157: Flow Control Techniques: Advances in Flow System Analysis, Modeling and Applications</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/157">doi: 10.3390/fluids11060157</a></p>
	<p>Authors:
		Michele Ferlauto
		</p>
	<p>Flow control has assumed a key role in many applied aspects of fluid dynamics andpropulsion in efforts toward CO2-neutral growth in air, ground and maritime transportation [...]</p>
	]]></content:encoded>

	<dc:title>Flow Control Techniques: Advances in Flow System Analysis, Modeling and Applications</dc:title>
			<dc:creator>Michele Ferlauto</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060157</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-20</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-20</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Editorial</prism:section>
	<prism:startingPage>157</prism:startingPage>
		<prism:doi>10.3390/fluids11060157</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/157</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/156">

	<title>Fluids, Vol. 11, Pages 156: Research on the Influence of Channel Bending on Control Rod Drop</title>
	<link>https://www.mdpi.com/2311-5521/11/6/156</link>
	<description>Research on the effect of channel bending on control rod drop is crucial; this paper employs FLUENT dynamic mesh technology to study the drop behavior of a control rod in a simplified control rod channel after bending deformation. It compares the differences in rod drop under different fluid media and various bent channel geometries (straight channel, C-shaped bent channel, S-shaped bent channel), and analyzes the variation patterns of rod drop time, velocity, static pressure, dynamic pressure, and flow field. The results show that under C-shaped and S-shaped bends, the changes in the flow field when the control rod descends without contacting the channel have no effect on the rod drop time.</description>
	<pubDate>2026-06-19</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 156: Research on the Influence of Channel Bending on Control Rod Drop</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/156">doi: 10.3390/fluids11060156</a></p>
	<p>Authors:
		Siyu Zou
		Chang’e Wu
		Yangyang Tang
		Qifeng Lv
		Yue Ma
		Jinghua Tang
		</p>
	<p>Research on the effect of channel bending on control rod drop is crucial; this paper employs FLUENT dynamic mesh technology to study the drop behavior of a control rod in a simplified control rod channel after bending deformation. It compares the differences in rod drop under different fluid media and various bent channel geometries (straight channel, C-shaped bent channel, S-shaped bent channel), and analyzes the variation patterns of rod drop time, velocity, static pressure, dynamic pressure, and flow field. The results show that under C-shaped and S-shaped bends, the changes in the flow field when the control rod descends without contacting the channel have no effect on the rod drop time.</p>
	]]></content:encoded>

	<dc:title>Research on the Influence of Channel Bending on Control Rod Drop</dc:title>
			<dc:creator>Siyu Zou</dc:creator>
			<dc:creator>Chang’e Wu</dc:creator>
			<dc:creator>Yangyang Tang</dc:creator>
			<dc:creator>Qifeng Lv</dc:creator>
			<dc:creator>Yue Ma</dc:creator>
			<dc:creator>Jinghua Tang</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060156</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-19</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-19</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>156</prism:startingPage>
		<prism:doi>10.3390/fluids11060156</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/156</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/155">

	<title>Fluids, Vol. 11, Pages 155: A Correction Term for the Asymptotic Scaling of Drag in Flat-Plate Turbulent Boundary Layers</title>
	<link>https://www.mdpi.com/2311-5521/11/6/155</link>
	<description>Dixit et al. proposed an asymptotic drag scaling method for zero-pressure-gradient flat-plate turbulent boundary layers based on the approximation M&amp;amp;sim;U&amp;amp;tau;2&amp;amp;delta;, where M is the kinematic momentum rate through the boundary layer, U&amp;amp;tau; is the friction velocity, and &amp;amp;delta; is the boundary-layer thickness. In the present paper, an explicit Reynolds-number-dependent correction to this approximation is derived from the logarithmic mean-velocity profile. Integration of the log law across the layer yields M&amp;amp;sim;U&amp;amp;tau;2&amp;amp;delta;f(Re&amp;amp;tau;), where Re&amp;amp;tau;=&amp;amp;delta;U&amp;amp;tau;/&amp;amp;nu; is the friction Reynolds number and f(Re&amp;amp;tau;) is given analytically. Application of the correction to the dataset compiled by Dixit et al. shows that the corrected scaling gives an exponent consistent with the asymptotic value &amp;amp;minus;1/2 within bootstrap confidence intervals, whereas the uncorrected formulation does not. The correction should be viewed as a leading-order amendment, since the derivation uses the logarithmic law outside its strict range of validity.</description>
	<pubDate>2026-06-18</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 155: A Correction Term for the Asymptotic Scaling of Drag in Flat-Plate Turbulent Boundary Layers</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/155">doi: 10.3390/fluids11060155</a></p>
	<p>Authors:
		Nils Tångefjord Basse
		</p>
	<p>Dixit et al. proposed an asymptotic drag scaling method for zero-pressure-gradient flat-plate turbulent boundary layers based on the approximation M&amp;amp;sim;U&amp;amp;tau;2&amp;amp;delta;, where M is the kinematic momentum rate through the boundary layer, U&amp;amp;tau; is the friction velocity, and &amp;amp;delta; is the boundary-layer thickness. In the present paper, an explicit Reynolds-number-dependent correction to this approximation is derived from the logarithmic mean-velocity profile. Integration of the log law across the layer yields M&amp;amp;sim;U&amp;amp;tau;2&amp;amp;delta;f(Re&amp;amp;tau;), where Re&amp;amp;tau;=&amp;amp;delta;U&amp;amp;tau;/&amp;amp;nu; is the friction Reynolds number and f(Re&amp;amp;tau;) is given analytically. Application of the correction to the dataset compiled by Dixit et al. shows that the corrected scaling gives an exponent consistent with the asymptotic value &amp;amp;minus;1/2 within bootstrap confidence intervals, whereas the uncorrected formulation does not. The correction should be viewed as a leading-order amendment, since the derivation uses the logarithmic law outside its strict range of validity.</p>
	]]></content:encoded>

	<dc:title>A Correction Term for the Asymptotic Scaling of Drag in Flat-Plate Turbulent Boundary Layers</dc:title>
			<dc:creator>Nils Tångefjord Basse</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060155</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-18</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-18</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>155</prism:startingPage>
		<prism:doi>10.3390/fluids11060155</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/155</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/154">

	<title>Fluids, Vol. 11, Pages 154: A Low-Cost Time Calibration Validation Method for Synchronized PIV Systems Using Readily Available Components</title>
	<link>https://www.mdpi.com/2311-5521/11/6/154</link>
	<description>Particle Image Velocimetry (PIV) has recently evolved from a costly, specialized technique into an accessible method thanks to affordable hardware and open-source software. This work introduces a time calibration validation method tailored for low-cost or Do-It-Yourself (DIY) PIV systems. By utilizing inexpensive components such as light-dependent resistors (LDRs), basic resistors, and data acquisition devices or microcontrollers, the study enables accurate timing analysis of light pulses from synchronized lasers or LEDs. Experimental data obtained in real time using a National Instruments USB-6003 DAQ device confirm the system&amp;amp;rsquo;s ability to detect light pulses with high temporal resolution. Through voltage signal interpretation, the synchronization accuracy of light sources is validated across different sampling rates. Moreover, the study demonstrates how the internal frequency settings of PIVlab, an open-source PIV software package, can be customized to enhance acquisition flexibility. Timing deviations of up to 20% were identified across selected default frequency settings. The proposed method ensures that low-cost systems maintain sufficient accuracy for phase-sensitive flow measurements, such as oscillatory flow or wave action, contributing to the broader adoption of PIV in resource-limited environments. It presents a low-cost method for validating timing accuracy in PIV systems, employs widely available components and is adaptable to multiple platforms, and enables precise synchronization checks critical for flow visualization.</description>
	<pubDate>2026-06-18</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 154: A Low-Cost Time Calibration Validation Method for Synchronized PIV Systems Using Readily Available Components</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/154">doi: 10.3390/fluids11060154</a></p>
	<p>Authors:
		Sinan Erucar
		Taylan Bagci
		V. S. Ozgur Kirca
		</p>
	<p>Particle Image Velocimetry (PIV) has recently evolved from a costly, specialized technique into an accessible method thanks to affordable hardware and open-source software. This work introduces a time calibration validation method tailored for low-cost or Do-It-Yourself (DIY) PIV systems. By utilizing inexpensive components such as light-dependent resistors (LDRs), basic resistors, and data acquisition devices or microcontrollers, the study enables accurate timing analysis of light pulses from synchronized lasers or LEDs. Experimental data obtained in real time using a National Instruments USB-6003 DAQ device confirm the system&amp;amp;rsquo;s ability to detect light pulses with high temporal resolution. Through voltage signal interpretation, the synchronization accuracy of light sources is validated across different sampling rates. Moreover, the study demonstrates how the internal frequency settings of PIVlab, an open-source PIV software package, can be customized to enhance acquisition flexibility. Timing deviations of up to 20% were identified across selected default frequency settings. The proposed method ensures that low-cost systems maintain sufficient accuracy for phase-sensitive flow measurements, such as oscillatory flow or wave action, contributing to the broader adoption of PIV in resource-limited environments. It presents a low-cost method for validating timing accuracy in PIV systems, employs widely available components and is adaptable to multiple platforms, and enables precise synchronization checks critical for flow visualization.</p>
	]]></content:encoded>

	<dc:title>A Low-Cost Time Calibration Validation Method for Synchronized PIV Systems Using Readily Available Components</dc:title>
			<dc:creator>Sinan Erucar</dc:creator>
			<dc:creator>Taylan Bagci</dc:creator>
			<dc:creator>V. S. Ozgur Kirca</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060154</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-18</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-18</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>154</prism:startingPage>
		<prism:doi>10.3390/fluids11060154</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/154</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/153">

	<title>Fluids, Vol. 11, Pages 153: Capacity-Specific Anti-Cavitation Radial Control-Valve Trims via Density-Based Topology Optimization</title>
	<link>https://www.mdpi.com/2311-5521/11/6/153</link>
	<description>We present a material distribution topology optimization (TO) framework that directly generates capacity-specific radial trims for severe-service control valves. The method uses an out-of-plane resistance modified two-dimensional turbulence model and objective functions that maximize directional change to create tortuous pressure-staging geometries at predefined channel depths. Four trims targeting non-dimensional capacities (CV) of 0.672, 0.96 (two objectives), and 1.248 were optimized, MSLA-printed, and tested in a globe valve using IEC 60534 procedures. The measured capacities ranged from &amp;amp;minus;13.7% to +4.8% of the targets for a fully 2D optimization process, dropping to a maximum of 7.8% when coupled with a hybrid 3D tuning step. Acoustic detection indicated incipient cavitation at a pressure drop ratios greater than 0.87 for the most highly staged design and 0.73 for the highest capacity design, which is consistent with our simulations of the flow field before fabrication. These results demonstrate that TO can deliver fit-to-service, capacity-tuned trims with excellent cavitation suppression, reducing reliance on large parametric design libraries.</description>
	<pubDate>2026-06-17</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 153: Capacity-Specific Anti-Cavitation Radial Control-Valve Trims via Density-Based Topology Optimization</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/153">doi: 10.3390/fluids11060153</a></p>
	<p>Authors:
		Bruce Butler
		Joe Alexandersen
		Sameer Rao
		</p>
	<p>We present a material distribution topology optimization (TO) framework that directly generates capacity-specific radial trims for severe-service control valves. The method uses an out-of-plane resistance modified two-dimensional turbulence model and objective functions that maximize directional change to create tortuous pressure-staging geometries at predefined channel depths. Four trims targeting non-dimensional capacities (CV) of 0.672, 0.96 (two objectives), and 1.248 were optimized, MSLA-printed, and tested in a globe valve using IEC 60534 procedures. The measured capacities ranged from &amp;amp;minus;13.7% to +4.8% of the targets for a fully 2D optimization process, dropping to a maximum of 7.8% when coupled with a hybrid 3D tuning step. Acoustic detection indicated incipient cavitation at a pressure drop ratios greater than 0.87 for the most highly staged design and 0.73 for the highest capacity design, which is consistent with our simulations of the flow field before fabrication. These results demonstrate that TO can deliver fit-to-service, capacity-tuned trims with excellent cavitation suppression, reducing reliance on large parametric design libraries.</p>
	]]></content:encoded>

	<dc:title>Capacity-Specific Anti-Cavitation Radial Control-Valve Trims via Density-Based Topology Optimization</dc:title>
			<dc:creator>Bruce Butler</dc:creator>
			<dc:creator>Joe Alexandersen</dc:creator>
			<dc:creator>Sameer Rao</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060153</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-17</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-17</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>153</prism:startingPage>
		<prism:doi>10.3390/fluids11060153</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/153</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/152">

	<title>Fluids, Vol. 11, Pages 152: Numerical Simulation of Shock Wave Propagation Through Multiple Raindrops</title>
	<link>https://www.mdpi.com/2311-5521/11/6/152</link>
	<description>A numerical study of shock wave propagation through multiple raindrops is presented using a density-based compressible two-phase flow solver coupled with a sharp-interface volume-of-fluid (VoF) method. The piecewise linear interface calculation (PLIC) approach is employed to reconstruct gas&amp;amp;ndash;liquid interfaces and capture droplet deformation during shock interaction. The numerical framework is first validated using a one-dimensional gas&amp;amp;ndash;liquid shock tube problem and a shock&amp;amp;ndash;helium bubble interaction benchmark. The method is then applied to investigate shock interactions with single, double, and multiple raindrops under compressible flow conditions. Numerical results show that complex wave structures, including shock reflection, diffraction, and wave interference, develop during shock propagation through raindrop fields. Interactions between neighboring droplets lead to local pressure amplification and non-uniform flow structures.</description>
	<pubDate>2026-06-16</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 152: Numerical Simulation of Shock Wave Propagation Through Multiple Raindrops</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/152">doi: 10.3390/fluids11060152</a></p>
	<p>Authors:
		Lingquan Li
		Jianglan Li
		Zhouteng Ye
		Jia Yan
		Linchuan Tian
		Xiaoquan Yang
		</p>
	<p>A numerical study of shock wave propagation through multiple raindrops is presented using a density-based compressible two-phase flow solver coupled with a sharp-interface volume-of-fluid (VoF) method. The piecewise linear interface calculation (PLIC) approach is employed to reconstruct gas&amp;amp;ndash;liquid interfaces and capture droplet deformation during shock interaction. The numerical framework is first validated using a one-dimensional gas&amp;amp;ndash;liquid shock tube problem and a shock&amp;amp;ndash;helium bubble interaction benchmark. The method is then applied to investigate shock interactions with single, double, and multiple raindrops under compressible flow conditions. Numerical results show that complex wave structures, including shock reflection, diffraction, and wave interference, develop during shock propagation through raindrop fields. Interactions between neighboring droplets lead to local pressure amplification and non-uniform flow structures.</p>
	]]></content:encoded>

	<dc:title>Numerical Simulation of Shock Wave Propagation Through Multiple Raindrops</dc:title>
			<dc:creator>Lingquan Li</dc:creator>
			<dc:creator>Jianglan Li</dc:creator>
			<dc:creator>Zhouteng Ye</dc:creator>
			<dc:creator>Jia Yan</dc:creator>
			<dc:creator>Linchuan Tian</dc:creator>
			<dc:creator>Xiaoquan Yang</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060152</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-16</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-16</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>152</prism:startingPage>
		<prism:doi>10.3390/fluids11060152</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/152</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/151">

	<title>Fluids, Vol. 11, Pages 151: Experimental and Numerical Investigation of Drag Reduction and Heat-Transfer Characteristics of Xanthan Gum Solutions at Different Concentrations in Turbulent Pipe Flow Under Varying Temperature Conditions</title>
	<link>https://www.mdpi.com/2311-5521/11/6/151</link>
	<description>This study presents a combined experimental and numerical investigation of xanthan gum solutions at 100 and 300 ppm in turbulent smooth pipe flow under temperatures of 30&amp;amp;ndash;50 &amp;amp;deg;C and Reynolds numbers of 8000&amp;amp;ndash;12,000. Water was used as the Newtonian reference fluid, while xanthan gum was modelled using temperature- and concentration-dependent shear-thinning properties. Experimental pressure-drop data were used to evaluate drag-reduction behaviour, whereas numerical simulations were employed to analyse the associated flow and heat-transfer responses. The results show that XG 100 ppm produced a relatively stable drag-reduction response of approximately 31&amp;amp;ndash;39%, while XG 300 ppm showed a wider and more condition-dependent range of about 25&amp;amp;ndash;45%. Water exhibited higher Nusselt numbers of approximately 68&amp;amp;ndash;106. In contrast, XG 100 ppm produced Nusselt numbers of approximately 45&amp;amp;ndash;69, while XG 300 ppm showed lower values of about 35&amp;amp;ndash;61. The corresponding heat-transfer reduction ranged from approximately 26&amp;amp;ndash;48% for XG 100 ppm and 23&amp;amp;ndash;46% for XG 300 ppm. These findings confirm a clear hydraulic&amp;amp;ndash;thermal trade-off, indicating that the xanthan gum concentration should be optimised according to both pressure-loss reduction and heat-transfer requirements.</description>
	<pubDate>2026-06-16</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 151: Experimental and Numerical Investigation of Drag Reduction and Heat-Transfer Characteristics of Xanthan Gum Solutions at Different Concentrations in Turbulent Pipe Flow Under Varying Temperature Conditions</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/151">doi: 10.3390/fluids11060151</a></p>
	<p>Authors:
		Andi Cahya Ichi
		Sri Poernomo Sari
		 Gunawan
		 Yanuar
		</p>
	<p>This study presents a combined experimental and numerical investigation of xanthan gum solutions at 100 and 300 ppm in turbulent smooth pipe flow under temperatures of 30&amp;amp;ndash;50 &amp;amp;deg;C and Reynolds numbers of 8000&amp;amp;ndash;12,000. Water was used as the Newtonian reference fluid, while xanthan gum was modelled using temperature- and concentration-dependent shear-thinning properties. Experimental pressure-drop data were used to evaluate drag-reduction behaviour, whereas numerical simulations were employed to analyse the associated flow and heat-transfer responses. The results show that XG 100 ppm produced a relatively stable drag-reduction response of approximately 31&amp;amp;ndash;39%, while XG 300 ppm showed a wider and more condition-dependent range of about 25&amp;amp;ndash;45%. Water exhibited higher Nusselt numbers of approximately 68&amp;amp;ndash;106. In contrast, XG 100 ppm produced Nusselt numbers of approximately 45&amp;amp;ndash;69, while XG 300 ppm showed lower values of about 35&amp;amp;ndash;61. The corresponding heat-transfer reduction ranged from approximately 26&amp;amp;ndash;48% for XG 100 ppm and 23&amp;amp;ndash;46% for XG 300 ppm. These findings confirm a clear hydraulic&amp;amp;ndash;thermal trade-off, indicating that the xanthan gum concentration should be optimised according to both pressure-loss reduction and heat-transfer requirements.</p>
	]]></content:encoded>

	<dc:title>Experimental and Numerical Investigation of Drag Reduction and Heat-Transfer Characteristics of Xanthan Gum Solutions at Different Concentrations in Turbulent Pipe Flow Under Varying Temperature Conditions</dc:title>
			<dc:creator>Andi Cahya Ichi</dc:creator>
			<dc:creator>Sri Poernomo Sari</dc:creator>
			<dc:creator> Gunawan</dc:creator>
			<dc:creator> Yanuar</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060151</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-16</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-16</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>151</prism:startingPage>
		<prism:doi>10.3390/fluids11060151</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/151</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/150">

	<title>Fluids, Vol. 11, Pages 150: Assessment of Injection Modeling Techniques for a Water Spray Using an Euler/Lagrange Approach</title>
	<link>https://www.mdpi.com/2311-5521/11/6/150</link>
	<description>In the context of aircraft engine technologies, sprays are used to inject water into the engine cycle to enhance efficiency and reduce emissions. Accurate specification of droplet injection boundary conditions is therefore essential for reliable numerical predictions. This study presents a numerical validation of a water spray configuration previously characterized using phase Doppler anemometry. An Euler/Lagrange approach is applied to simulate the spray using two distinct injection strategies: an array of injector points (Case 1) and a solid-cone injector (Case 2). Numerical results are compared with experimental data to assess droplet size and velocity distributions. Both approaches capture the main spray characteristics, while Case 1 provides improved agreement due to a more accurate representation of the injection conditions. In addition, the influence of droplet&amp;amp;ndash;droplet collisions is investigated using different collision-regime maps. While the collision models lead to significantly different collision outcomes, only minor differences are observed in spray characteristics, with noticeable deviations occurring in the downstream region. Overall, the results demonstrate the importance of accurate injection modeling for reliable spray predictions, while simpler injection approaches remain viable with reduced accuracy. The influence of collision modeling is limited under the present conditions and for the investigated spray metrics, providing insight into its role and limitations in polydisperse sprays.</description>
	<pubDate>2026-06-13</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 150: Assessment of Injection Modeling Techniques for a Water Spray Using an Euler/Lagrange Approach</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/150">doi: 10.3390/fluids11060150</a></p>
	<p>Authors:
		Marwan Khaled
		Martin Sommerfeld
		Laurin Mächtig
		Kai Alexander Schulz
		Alexander Woitalka
		Bernhard Weigand
		</p>
	<p>In the context of aircraft engine technologies, sprays are used to inject water into the engine cycle to enhance efficiency and reduce emissions. Accurate specification of droplet injection boundary conditions is therefore essential for reliable numerical predictions. This study presents a numerical validation of a water spray configuration previously characterized using phase Doppler anemometry. An Euler/Lagrange approach is applied to simulate the spray using two distinct injection strategies: an array of injector points (Case 1) and a solid-cone injector (Case 2). Numerical results are compared with experimental data to assess droplet size and velocity distributions. Both approaches capture the main spray characteristics, while Case 1 provides improved agreement due to a more accurate representation of the injection conditions. In addition, the influence of droplet&amp;amp;ndash;droplet collisions is investigated using different collision-regime maps. While the collision models lead to significantly different collision outcomes, only minor differences are observed in spray characteristics, with noticeable deviations occurring in the downstream region. Overall, the results demonstrate the importance of accurate injection modeling for reliable spray predictions, while simpler injection approaches remain viable with reduced accuracy. The influence of collision modeling is limited under the present conditions and for the investigated spray metrics, providing insight into its role and limitations in polydisperse sprays.</p>
	]]></content:encoded>

	<dc:title>Assessment of Injection Modeling Techniques for a Water Spray Using an Euler/Lagrange Approach</dc:title>
			<dc:creator>Marwan Khaled</dc:creator>
			<dc:creator>Martin Sommerfeld</dc:creator>
			<dc:creator>Laurin Mächtig</dc:creator>
			<dc:creator>Kai Alexander Schulz</dc:creator>
			<dc:creator>Alexander Woitalka</dc:creator>
			<dc:creator>Bernhard Weigand</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060150</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-13</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-13</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>150</prism:startingPage>
		<prism:doi>10.3390/fluids11060150</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/150</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/149">

	<title>Fluids, Vol. 11, Pages 149: Numerical Investigation of Stall Flutter of a Pitching Airfoil at Low Reynolds Number</title>
	<link>https://www.mdpi.com/2311-5521/11/6/149</link>
	<description>The present work investigates fluid&amp;amp;ndash;structure instabilities and flow-induced oscillations of a pitching NACA0012 airfoil through numerical simulations. The flow is modeled using the compressible Navier&amp;amp;ndash;Stokes equations in a non-inertial rotating reference frame, while the structural dynamics are represented by a torsional spring&amp;amp;ndash;mass&amp;amp;ndash;damper system. The analysis focuses on the effects of reduced velocity, equilibrium angle of attack, and elastic axis position on the aeroelastic behavior at low Reynolds number (Re=1000). Particular attention is devoted to characterizing the transition from vortex-shedding-dominated oscillations to fully developed limit-cycle oscillations and to assessing its sensitivity to aerodynamic and structural parameters. The results show a transition from steady flow to vortex shedding and, at higher reduced velocities, to limit-cycle oscillations. Increasing the equilibrium angle of attack promotes an earlier onset of instability and stronger aerodynamic forcing, while moving the elastic axis downstream has a similar destabilizing effect due to the larger aerodynamic moment arm (up to approximately 20% reduction of the critical reduced velocity). The nature of the transition is found to depend strongly on the equilibrium angle of attack, with distinct behaviors observed at low and high incidence. Frequency analysis highlights the progressive coupling between fluid and structural dynamics: vortex shedding dominates in the weakly coupled regime, whereas the structural frequency governs the response in the limit-cycle regime. The study provides a consistent description of the mechanisms driving flow-induced oscillations and of the parameters controlling aeroelastic stability.</description>
	<pubDate>2026-06-11</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 149: Numerical Investigation of Stall Flutter of a Pitching Airfoil at Low Reynolds Number</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/149">doi: 10.3390/fluids11060149</a></p>
	<p>Authors:
		Maria Adele Cecchini
		Giulio Soldati
		Peter Jordan
		Sergio Pirozzoli
		</p>
	<p>The present work investigates fluid&amp;amp;ndash;structure instabilities and flow-induced oscillations of a pitching NACA0012 airfoil through numerical simulations. The flow is modeled using the compressible Navier&amp;amp;ndash;Stokes equations in a non-inertial rotating reference frame, while the structural dynamics are represented by a torsional spring&amp;amp;ndash;mass&amp;amp;ndash;damper system. The analysis focuses on the effects of reduced velocity, equilibrium angle of attack, and elastic axis position on the aeroelastic behavior at low Reynolds number (Re=1000). Particular attention is devoted to characterizing the transition from vortex-shedding-dominated oscillations to fully developed limit-cycle oscillations and to assessing its sensitivity to aerodynamic and structural parameters. The results show a transition from steady flow to vortex shedding and, at higher reduced velocities, to limit-cycle oscillations. Increasing the equilibrium angle of attack promotes an earlier onset of instability and stronger aerodynamic forcing, while moving the elastic axis downstream has a similar destabilizing effect due to the larger aerodynamic moment arm (up to approximately 20% reduction of the critical reduced velocity). The nature of the transition is found to depend strongly on the equilibrium angle of attack, with distinct behaviors observed at low and high incidence. Frequency analysis highlights the progressive coupling between fluid and structural dynamics: vortex shedding dominates in the weakly coupled regime, whereas the structural frequency governs the response in the limit-cycle regime. The study provides a consistent description of the mechanisms driving flow-induced oscillations and of the parameters controlling aeroelastic stability.</p>
	]]></content:encoded>

	<dc:title>Numerical Investigation of Stall Flutter of a Pitching Airfoil at Low Reynolds Number</dc:title>
			<dc:creator>Maria Adele Cecchini</dc:creator>
			<dc:creator>Giulio Soldati</dc:creator>
			<dc:creator>Peter Jordan</dc:creator>
			<dc:creator>Sergio Pirozzoli</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060149</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-11</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-11</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>149</prism:startingPage>
		<prism:doi>10.3390/fluids11060149</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/149</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/148">

	<title>Fluids, Vol. 11, Pages 148: Linear Solvers in OpenFOAM: A Technical Review and SIMPLE Convergence Study</title>
	<link>https://www.mdpi.com/2311-5521/11/6/148</link>
	<description>This article reviews the linear solvers available in OpenFOAM and assesses their impact on the convergence behaviour of the SIMPLE algorithm. The discretisation of transport equations in CFD results in large and sparse linear systems, for which the choice of linear solver strongly influences the computational time. Although the solver does not change the final discrete solution, the difference in speed and robustness between the solvers can be more than one order of magnitude. A brief overview is given concerning how the velocity and pressure fields are decoupled in OpenFOAM, followed by a detailed review of the main linear solver families, including direct methods, basic iterative methods, multigrid methods and Krylov subspace methods, with attention to their practical strengths and weaknesses. The performance of the most advanced solvers is evaluated on a full-scale non-reacting kiln case consisting of 2.3 million cells. The pressure-corrector equation is identified as the main bottleneck in the SIMPLE algorithm. The conjugate gradient (CG) solver with a multigrid (MG) preconditioner is found to be the fastest and most stable method, achieving speed-ups of up to a factor of 7 compared to the slower advanced methods. Using MG as a preconditioner also improves the robustness of the Bi-CGStab method.</description>
	<pubDate>2026-06-11</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 148: Linear Solvers in OpenFOAM: A Technical Review and SIMPLE Convergence Study</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/148">doi: 10.3390/fluids11060148</a></p>
	<p>Authors:
		Mohamed El Abbassi
		Cornelis Vuik
		</p>
	<p>This article reviews the linear solvers available in OpenFOAM and assesses their impact on the convergence behaviour of the SIMPLE algorithm. The discretisation of transport equations in CFD results in large and sparse linear systems, for which the choice of linear solver strongly influences the computational time. Although the solver does not change the final discrete solution, the difference in speed and robustness between the solvers can be more than one order of magnitude. A brief overview is given concerning how the velocity and pressure fields are decoupled in OpenFOAM, followed by a detailed review of the main linear solver families, including direct methods, basic iterative methods, multigrid methods and Krylov subspace methods, with attention to their practical strengths and weaknesses. The performance of the most advanced solvers is evaluated on a full-scale non-reacting kiln case consisting of 2.3 million cells. The pressure-corrector equation is identified as the main bottleneck in the SIMPLE algorithm. The conjugate gradient (CG) solver with a multigrid (MG) preconditioner is found to be the fastest and most stable method, achieving speed-ups of up to a factor of 7 compared to the slower advanced methods. Using MG as a preconditioner also improves the robustness of the Bi-CGStab method.</p>
	]]></content:encoded>

	<dc:title>Linear Solvers in OpenFOAM: A Technical Review and SIMPLE Convergence Study</dc:title>
			<dc:creator>Mohamed El Abbassi</dc:creator>
			<dc:creator>Cornelis Vuik</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060148</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-11</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-11</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Review</prism:section>
	<prism:startingPage>148</prism:startingPage>
		<prism:doi>10.3390/fluids11060148</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/148</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/147">

	<title>Fluids, Vol. 11, Pages 147: Consistently Enforced Wall Models by Reinforcement Learning for Wall-Modeled Large-Eddy Simulation</title>
	<link>https://www.mdpi.com/2311-5521/11/6/147</link>
	<description>A reinforcement-learning-based wall-modeled large-eddy simulation (RL-WMLES) framework is proposed to improve the physical consistency of near-wall turbulence predictions. In this approach, a reinforcement learning agent is coupled with the WMLES solver to dynamically adjust a compensating stress term, with the objective of enforcing agreement between the LES solution and the law of the wall. The agent is trained using the proximal policy optimization (PPO) algorithm, where the state is defined as the discrepancy between the near-wall LES velocity and the wall-model prediction, and the action corresponds to modifying a parameterized support viscosity distribution. The proposed method is implemented within a high-performance CFD solver and trained on turbulent channel flow. Numerical results demonstrate that the trained agent effectively reduces the log-layer mismatch and significantly improves the accuracy of near-wall velocity predictions. Furthermore, the RL-WMLES framework exhibits a degree of generalization capability: the trained agent performs robustly with varying levels of numerical dissipation and Reynolds numbers. By introducing a simple interpolation strategy, the same agent can be successfully applied to configurations with different matching locations. Overall, the RL-WMLES framework provides a flexible and data-driven approach for enforcing physical constraints in turbulence modeling. The method shows strong potential for extension to more complex flows.</description>
	<pubDate>2026-06-11</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 147: Consistently Enforced Wall Models by Reinforcement Learning for Wall-Modeled Large-Eddy Simulation</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/147">doi: 10.3390/fluids11060147</a></p>
	<p>Authors:
		Runze Gao
		Yurong Li
		Yu Lv
		</p>
	<p>A reinforcement-learning-based wall-modeled large-eddy simulation (RL-WMLES) framework is proposed to improve the physical consistency of near-wall turbulence predictions. In this approach, a reinforcement learning agent is coupled with the WMLES solver to dynamically adjust a compensating stress term, with the objective of enforcing agreement between the LES solution and the law of the wall. The agent is trained using the proximal policy optimization (PPO) algorithm, where the state is defined as the discrepancy between the near-wall LES velocity and the wall-model prediction, and the action corresponds to modifying a parameterized support viscosity distribution. The proposed method is implemented within a high-performance CFD solver and trained on turbulent channel flow. Numerical results demonstrate that the trained agent effectively reduces the log-layer mismatch and significantly improves the accuracy of near-wall velocity predictions. Furthermore, the RL-WMLES framework exhibits a degree of generalization capability: the trained agent performs robustly with varying levels of numerical dissipation and Reynolds numbers. By introducing a simple interpolation strategy, the same agent can be successfully applied to configurations with different matching locations. Overall, the RL-WMLES framework provides a flexible and data-driven approach for enforcing physical constraints in turbulence modeling. The method shows strong potential for extension to more complex flows.</p>
	]]></content:encoded>

	<dc:title>Consistently Enforced Wall Models by Reinforcement Learning for Wall-Modeled Large-Eddy Simulation</dc:title>
			<dc:creator>Runze Gao</dc:creator>
			<dc:creator>Yurong Li</dc:creator>
			<dc:creator>Yu Lv</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060147</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-11</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-11</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>147</prism:startingPage>
		<prism:doi>10.3390/fluids11060147</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/147</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/146">

	<title>Fluids, Vol. 11, Pages 146: Numerical Investigation of Dynamics and Particle Transport in Gas&amp;ndash;Liquid&amp;ndash;Solid Three-Phase Multi-Source Converging Flows</title>
	<link>https://www.mdpi.com/2311-5521/11/6/146</link>
	<description>This study utilizes a large-scale numerical simulation model to investigate the hydrodynamic behavior and particle transport characteristics of gas&amp;amp;ndash;liquid&amp;amp;ndash;solid three-phase flow in vertical wellbores featuring multi-source confluence and curved geometries. Simulation results indicate that increasing flow velocity shifts the dominant control mechanism from surface tension to inertial forces, transitioning the flow pattern from slug flow to churn flow. In curved pipe sections, centrifugal phase separation and geometric shielding effects cause significant flow asymmetry and maintain large bubble stability at the inner wall. Additionally, the multi-inlet structure induces shear rate gradients that result in the spatial coexistence of two distinct bubble scales. Furthermore, localized gas concentrations exceeding 70% at the upper inlet can trigger severe gas-locking phenomena and intense pressure pulsations.</description>
	<pubDate>2026-06-10</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 146: Numerical Investigation of Dynamics and Particle Transport in Gas&amp;ndash;Liquid&amp;ndash;Solid Three-Phase Multi-Source Converging Flows</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/146">doi: 10.3390/fluids11060146</a></p>
	<p>Authors:
		Lei Wang
		Zhiqiang Hu
		Lilin Li
		Zhenxiang Zhang
		Liang Tao
		</p>
	<p>This study utilizes a large-scale numerical simulation model to investigate the hydrodynamic behavior and particle transport characteristics of gas&amp;amp;ndash;liquid&amp;amp;ndash;solid three-phase flow in vertical wellbores featuring multi-source confluence and curved geometries. Simulation results indicate that increasing flow velocity shifts the dominant control mechanism from surface tension to inertial forces, transitioning the flow pattern from slug flow to churn flow. In curved pipe sections, centrifugal phase separation and geometric shielding effects cause significant flow asymmetry and maintain large bubble stability at the inner wall. Additionally, the multi-inlet structure induces shear rate gradients that result in the spatial coexistence of two distinct bubble scales. Furthermore, localized gas concentrations exceeding 70% at the upper inlet can trigger severe gas-locking phenomena and intense pressure pulsations.</p>
	]]></content:encoded>

	<dc:title>Numerical Investigation of Dynamics and Particle Transport in Gas&amp;amp;ndash;Liquid&amp;amp;ndash;Solid Three-Phase Multi-Source Converging Flows</dc:title>
			<dc:creator>Lei Wang</dc:creator>
			<dc:creator>Zhiqiang Hu</dc:creator>
			<dc:creator>Lilin Li</dc:creator>
			<dc:creator>Zhenxiang Zhang</dc:creator>
			<dc:creator>Liang Tao</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060146</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-10</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-10</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>146</prism:startingPage>
		<prism:doi>10.3390/fluids11060146</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/146</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/145">

	<title>Fluids, Vol. 11, Pages 145: Modified Luneburg Lens: How Well Does It Focus Surface Water Waves?</title>
	<link>https://www.mdpi.com/2311-5521/11/6/145</link>
	<description>An optical lens focuses light and a similar device can be developed to focus surface water waves. A detailed description of such hydrodynamic lenses is given, for which the focusing is induced by shaping the bathymetry of the bottom. Classically, the Luneburg lens uses a specific radial variation of the refractive index. The modified Luneburg lens (MLL) introduces an extra degree of freedom, permitting the focal point to be tuned. It is shown how to design the MLL for water waves, and then its performance is evaluated. Compared with a simple parabolic-shaped mount, the MLL is shown to be free of spherical aberration, resulting in a focus with larger intensity and smaller size of the focal point. Moreover, the focusing properties can be tuned and enhanced thanks to the possibility of changing the position of the focal point. The focusing quality of the MLL is described in all water-depth regimes (covering dispersive and non-dispersive waves) and the focusing of linear and nonlinear waves is revealed experimentally. The option of moving the focal point outside the lens, where the water depth is constant, may be useful when locating devices for harvesting wave energy.</description>
	<pubDate>2026-06-09</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 145: Modified Luneburg Lens: How Well Does It Focus Surface Water Waves?</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/145">doi: 10.3390/fluids11060145</a></p>
	<p>Authors:
		H. Pichard
		A. Maurel
		P. A. Martin
		P. Petitjeans
		V. Pagneux
		</p>
	<p>An optical lens focuses light and a similar device can be developed to focus surface water waves. A detailed description of such hydrodynamic lenses is given, for which the focusing is induced by shaping the bathymetry of the bottom. Classically, the Luneburg lens uses a specific radial variation of the refractive index. The modified Luneburg lens (MLL) introduces an extra degree of freedom, permitting the focal point to be tuned. It is shown how to design the MLL for water waves, and then its performance is evaluated. Compared with a simple parabolic-shaped mount, the MLL is shown to be free of spherical aberration, resulting in a focus with larger intensity and smaller size of the focal point. Moreover, the focusing properties can be tuned and enhanced thanks to the possibility of changing the position of the focal point. The focusing quality of the MLL is described in all water-depth regimes (covering dispersive and non-dispersive waves) and the focusing of linear and nonlinear waves is revealed experimentally. The option of moving the focal point outside the lens, where the water depth is constant, may be useful when locating devices for harvesting wave energy.</p>
	]]></content:encoded>

	<dc:title>Modified Luneburg Lens: How Well Does It Focus Surface Water Waves?</dc:title>
			<dc:creator>H. Pichard</dc:creator>
			<dc:creator>A. Maurel</dc:creator>
			<dc:creator>P. A. Martin</dc:creator>
			<dc:creator>P. Petitjeans</dc:creator>
			<dc:creator>V. Pagneux</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060145</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-09</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-09</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>145</prism:startingPage>
		<prism:doi>10.3390/fluids11060145</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/145</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/144">

	<title>Fluids, Vol. 11, Pages 144: Autoencoder-Based Optimal Sensor Placement and Aerodynamic Load Reconstruction for Airfoils</title>
	<link>https://www.mdpi.com/2311-5521/11/6/144</link>
	<description>Optimal sensor placement is a crucial issue in scientific and engineering research. This study proposes an autoencoder-based deep learning framework for automated optimal sensor layout and flow field reconstruction. A dataset is established based on transient Computational Fluid Dynamics (CFD) simulation results of a three-dimensional finite-span airfoil under various Reynolds numbers and angles of attack, enabling high-precision reconstruction of airfoil surface pressure distribution using sparse pressure coefficient data. The multilayer perceptron of both the encoder and decoder adopts an optimal five-layer structure with 200 nodes per layer, and the ReLU activation function delivers superior performance with a training loss reduction of over 45%. When using 50 sensors, the proposed architecture determined detailed placement and obtained a reconstruction error of 0.0604, which outperforms traditional manual sensor placement. The reconstruction accuracy of aerodynamic loads improves with increasing sensor count, but exhibits diminishing returns beyond the optimal threshold 50, necessitating a balanced selection that optimizes performance-to-cost ratio. The proposed method adaptively captures critical flow regions with high gradients, cutting sensor quantity by 60&amp;amp;ndash;80% versus grid-based placement. This method can flexibly use either CFD or experimental data in practical applications, offering an efficient solution for aerodynamic field reconstruction.</description>
	<pubDate>2026-06-08</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 144: Autoencoder-Based Optimal Sensor Placement and Aerodynamic Load Reconstruction for Airfoils</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/144">doi: 10.3390/fluids11060144</a></p>
	<p>Authors:
		Lixia Chen
		Chao Yuan
		Junlong Zhao
		</p>
	<p>Optimal sensor placement is a crucial issue in scientific and engineering research. This study proposes an autoencoder-based deep learning framework for automated optimal sensor layout and flow field reconstruction. A dataset is established based on transient Computational Fluid Dynamics (CFD) simulation results of a three-dimensional finite-span airfoil under various Reynolds numbers and angles of attack, enabling high-precision reconstruction of airfoil surface pressure distribution using sparse pressure coefficient data. The multilayer perceptron of both the encoder and decoder adopts an optimal five-layer structure with 200 nodes per layer, and the ReLU activation function delivers superior performance with a training loss reduction of over 45%. When using 50 sensors, the proposed architecture determined detailed placement and obtained a reconstruction error of 0.0604, which outperforms traditional manual sensor placement. The reconstruction accuracy of aerodynamic loads improves with increasing sensor count, but exhibits diminishing returns beyond the optimal threshold 50, necessitating a balanced selection that optimizes performance-to-cost ratio. The proposed method adaptively captures critical flow regions with high gradients, cutting sensor quantity by 60&amp;amp;ndash;80% versus grid-based placement. This method can flexibly use either CFD or experimental data in practical applications, offering an efficient solution for aerodynamic field reconstruction.</p>
	]]></content:encoded>

	<dc:title>Autoencoder-Based Optimal Sensor Placement and Aerodynamic Load Reconstruction for Airfoils</dc:title>
			<dc:creator>Lixia Chen</dc:creator>
			<dc:creator>Chao Yuan</dc:creator>
			<dc:creator>Junlong Zhao</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060144</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-08</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-08</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>144</prism:startingPage>
		<prism:doi>10.3390/fluids11060144</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/144</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/143">

	<title>Fluids, Vol. 11, Pages 143: Probability-Based Droplet Modeling for In-Flight Icing Problems</title>
	<link>https://www.mdpi.com/2311-5521/11/6/143</link>
	<description>A probability-based model (PBM) is developed to predict the evolution of a population of impinging droplets on a solid substrate and the eventual transition between dropwise and filmwise regimes. A dedicated heat transfer model is designed, in order to estimate the evaporating mass flux when the solid substrate is heated. Statistical information such as the droplet size distribution and the influence of surface wettability, required by the PBM, are derived using a previously developed high-fidelity individual-based model (IBM). The PBM is verified with the high-fidelity model for a small patch of solid substrate. Then, validation with experimental evidence from the literature is carried out in the case of in-flight ice on the NACA0012 airfoil. Results show that the present PBM is capable of investigating in-flight ice problems and can be integrated with a CFD analysis of the air flow past an airfoil flying through a cloud of supercooled droplets to predict the possible onset of ice accretion on the airfoil surface. Compared to Messinger-like models, the influence of surface morphology on runback water flow is incorporated in the PBM through the modeling of a discontinuous wetting layer, contributing to the design of passive and active anti-icing systems.</description>
	<pubDate>2026-06-07</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 143: Probability-Based Droplet Modeling for In-Flight Icing Problems</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/143">doi: 10.3390/fluids11060143</a></p>
	<p>Authors:
		Giulio Croce
		Nicola Suzzi
		</p>
	<p>A probability-based model (PBM) is developed to predict the evolution of a population of impinging droplets on a solid substrate and the eventual transition between dropwise and filmwise regimes. A dedicated heat transfer model is designed, in order to estimate the evaporating mass flux when the solid substrate is heated. Statistical information such as the droplet size distribution and the influence of surface wettability, required by the PBM, are derived using a previously developed high-fidelity individual-based model (IBM). The PBM is verified with the high-fidelity model for a small patch of solid substrate. Then, validation with experimental evidence from the literature is carried out in the case of in-flight ice on the NACA0012 airfoil. Results show that the present PBM is capable of investigating in-flight ice problems and can be integrated with a CFD analysis of the air flow past an airfoil flying through a cloud of supercooled droplets to predict the possible onset of ice accretion on the airfoil surface. Compared to Messinger-like models, the influence of surface morphology on runback water flow is incorporated in the PBM through the modeling of a discontinuous wetting layer, contributing to the design of passive and active anti-icing systems.</p>
	]]></content:encoded>

	<dc:title>Probability-Based Droplet Modeling for In-Flight Icing Problems</dc:title>
			<dc:creator>Giulio Croce</dc:creator>
			<dc:creator>Nicola Suzzi</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060143</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-07</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-07</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>143</prism:startingPage>
		<prism:doi>10.3390/fluids11060143</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/143</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/142">

	<title>Fluids, Vol. 11, Pages 142: Experimental Investigation of Friction Factor Performance in Additively Manufactured PCHE-Type Semicircular Channels with Corner Filleting</title>
	<link>https://www.mdpi.com/2311-5521/11/6/142</link>
	<description>Additive manufacturing (AM) introduces surface roughness that is much larger than that in chemically etched printed circuit heat exchanger (PCHE) channels, limiting the applicability of established design correlation. In this study, four selective laser melting (SLM) 3D-printed stainless steel test sections were tested, namely two semicircular and two rounded-edge semicircular channels, at hydraulic diameters of 2 mm and 4 mm. Water was used as the test fluid in the experiment, with a Reynolds number ranging from 500 to 7000 and wall heat flux ranging from 20 to 90 kW/m2. Scanning electron microscopy image characterization shows significant material accumulation concentrated at the rounded edges of the as-built channels. The experimental results show that for the entire flow regime, the printed rounded edge increases the friction factor by approximately 9% for 2 mm and 4 mm channels. The filleting design would increase the effective hydraulic roughness in small-diameter AM channels. The SLM 3D-printed rougher channel has a lower transition Reynolds number and higher turbulent friction factors compared to the etching channel. The data were compared with existing smooth PCHE channel data and rough AM mini-channel correlation, and two empirical correlations were developed for SLM 3D-printed mini-channels for transition and turbulent regimes.</description>
	<pubDate>2026-06-07</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 142: Experimental Investigation of Friction Factor Performance in Additively Manufactured PCHE-Type Semicircular Channels with Corner Filleting</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/142">doi: 10.3390/fluids11060142</a></p>
	<p>Authors:
		Lam Lam
		Yifan Yang
		Jiahang Chen
		Lap Mou Tam
		Afshin J. Ghajar
		</p>
	<p>Additive manufacturing (AM) introduces surface roughness that is much larger than that in chemically etched printed circuit heat exchanger (PCHE) channels, limiting the applicability of established design correlation. In this study, four selective laser melting (SLM) 3D-printed stainless steel test sections were tested, namely two semicircular and two rounded-edge semicircular channels, at hydraulic diameters of 2 mm and 4 mm. Water was used as the test fluid in the experiment, with a Reynolds number ranging from 500 to 7000 and wall heat flux ranging from 20 to 90 kW/m2. Scanning electron microscopy image characterization shows significant material accumulation concentrated at the rounded edges of the as-built channels. The experimental results show that for the entire flow regime, the printed rounded edge increases the friction factor by approximately 9% for 2 mm and 4 mm channels. The filleting design would increase the effective hydraulic roughness in small-diameter AM channels. The SLM 3D-printed rougher channel has a lower transition Reynolds number and higher turbulent friction factors compared to the etching channel. The data were compared with existing smooth PCHE channel data and rough AM mini-channel correlation, and two empirical correlations were developed for SLM 3D-printed mini-channels for transition and turbulent regimes.</p>
	]]></content:encoded>

	<dc:title>Experimental Investigation of Friction Factor Performance in Additively Manufactured PCHE-Type Semicircular Channels with Corner Filleting</dc:title>
			<dc:creator>Lam Lam</dc:creator>
			<dc:creator>Yifan Yang</dc:creator>
			<dc:creator>Jiahang Chen</dc:creator>
			<dc:creator>Lap Mou Tam</dc:creator>
			<dc:creator>Afshin J. Ghajar</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060142</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-07</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-07</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>142</prism:startingPage>
		<prism:doi>10.3390/fluids11060142</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/142</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/141">

	<title>Fluids, Vol. 11, Pages 141: Numerical Study on the Effect of Structural Parameters on Flow and Heat Transfer Characteristics of Helical Cruciform Fuel</title>
	<link>https://www.mdpi.com/2311-5521/11/6/141</link>
	<description>As a high-performance innovative fuel rod design, helical cruciform fuel (HCF) exhibits significant advantages over conventional circular fuel rods, such as a larger heat transfer area per unit volume, enhanced fluid flow and heat transfer characteristics due to its helical geometry, and a periodic self-supporting configuration. These attributes make it a highly promising option for future advanced reactor applications. Using the SST k-&amp;amp;omega; turbulence model, this study numerically investigates single-phase flow and heat transfer in a triangularly arranged 7-rod compact HCF fuel bundle, focusing on the effects of cross-sectional geometry and helical pitch on its three-dimensional flow and heat transfer behavior. Numerical results indicate that reducing the concave arc radius R increases the heat transfer surface area of the rod bundle, effectively enhancing heat transfer performance and reducing wall temperature; decreasing the helical pitch substantially strengthens fluid mixing. However, when the concave arc radius R becomes excessively small, the cross-flow intensity exhibits a local minimum in the concave region, resulting in a significant degradation of convective heat transfer capability in this area. These findings provide valuable insights for the structural optimization and design selection of HCF.</description>
	<pubDate>2026-06-05</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 141: Numerical Study on the Effect of Structural Parameters on Flow and Heat Transfer Characteristics of Helical Cruciform Fuel</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/141">doi: 10.3390/fluids11060141</a></p>
	<p>Authors:
		Yixiang Zou
		Yue Ma
		Jingwen Yan
		Chang’e Wu
		Qifeng Lv
		Jianqiang Shan
		</p>
	<p>As a high-performance innovative fuel rod design, helical cruciform fuel (HCF) exhibits significant advantages over conventional circular fuel rods, such as a larger heat transfer area per unit volume, enhanced fluid flow and heat transfer characteristics due to its helical geometry, and a periodic self-supporting configuration. These attributes make it a highly promising option for future advanced reactor applications. Using the SST k-&amp;amp;omega; turbulence model, this study numerically investigates single-phase flow and heat transfer in a triangularly arranged 7-rod compact HCF fuel bundle, focusing on the effects of cross-sectional geometry and helical pitch on its three-dimensional flow and heat transfer behavior. Numerical results indicate that reducing the concave arc radius R increases the heat transfer surface area of the rod bundle, effectively enhancing heat transfer performance and reducing wall temperature; decreasing the helical pitch substantially strengthens fluid mixing. However, when the concave arc radius R becomes excessively small, the cross-flow intensity exhibits a local minimum in the concave region, resulting in a significant degradation of convective heat transfer capability in this area. These findings provide valuable insights for the structural optimization and design selection of HCF.</p>
	]]></content:encoded>

	<dc:title>Numerical Study on the Effect of Structural Parameters on Flow and Heat Transfer Characteristics of Helical Cruciform Fuel</dc:title>
			<dc:creator>Yixiang Zou</dc:creator>
			<dc:creator>Yue Ma</dc:creator>
			<dc:creator>Jingwen Yan</dc:creator>
			<dc:creator>Chang’e Wu</dc:creator>
			<dc:creator>Qifeng Lv</dc:creator>
			<dc:creator>Jianqiang Shan</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060141</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-05</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-05</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>141</prism:startingPage>
		<prism:doi>10.3390/fluids11060141</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/141</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/140">

	<title>Fluids, Vol. 11, Pages 140: Mathematical Modeling of Fluid Flow and Heat Transfer in the Laminar Entrance Region of a Cylindrical Pipe</title>
	<link>https://www.mdpi.com/2311-5521/11/6/140</link>
	<description>This study conducted a numerical simulation of laminar flow within a cylindrical pipe using a semi-implicit method. The full Navier&amp;amp;ndash;Stokes equations in cylindrical coordinates were solved, with modifications to the SIMPLE algorithm to handle pressure-linked equations. We evaluated three key thermophysical parameters&amp;amp;mdash;dynamic viscosity, specific heat capacity, and thermal conductivity&amp;amp;mdash;under both constant and variable conditions in the entrance region. Due to the process&amp;amp;rsquo;s two-dimensional, time-dependent nature, third-kind boundary conditions were used to accurately model the effects of ambient temperature, external wind, and the pipe&amp;amp;rsquo;s geometric and physical features. From the numerical results, we analyzed the velocity field, pressure distribution, surface friction coefficient, and temperature distribution at various pipe cross-sections. These findings are of practical and scientific importance: they offer insights into the hydrodynamics and thermal behavior of the internal flow and enhance understanding of fluid flow and heat transfer, improving predictive models. This advancement supports better design and operational control in pipeline systems.</description>
	<pubDate>2026-06-04</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 140: Mathematical Modeling of Fluid Flow and Heat Transfer in the Laminar Entrance Region of a Cylindrical Pipe</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/140">doi: 10.3390/fluids11060140</a></p>
	<p>Authors:
		Ismatulla Khujaev
		Khusniddin Mamadaliev
		Muzaffar Hamdamov
		Shohjaxon Ravshanov
		Makhbuba Boborakhimova
		Oybek Begimov
		Shokhrukh Chulliyev
		</p>
	<p>This study conducted a numerical simulation of laminar flow within a cylindrical pipe using a semi-implicit method. The full Navier&amp;amp;ndash;Stokes equations in cylindrical coordinates were solved, with modifications to the SIMPLE algorithm to handle pressure-linked equations. We evaluated three key thermophysical parameters&amp;amp;mdash;dynamic viscosity, specific heat capacity, and thermal conductivity&amp;amp;mdash;under both constant and variable conditions in the entrance region. Due to the process&amp;amp;rsquo;s two-dimensional, time-dependent nature, third-kind boundary conditions were used to accurately model the effects of ambient temperature, external wind, and the pipe&amp;amp;rsquo;s geometric and physical features. From the numerical results, we analyzed the velocity field, pressure distribution, surface friction coefficient, and temperature distribution at various pipe cross-sections. These findings are of practical and scientific importance: they offer insights into the hydrodynamics and thermal behavior of the internal flow and enhance understanding of fluid flow and heat transfer, improving predictive models. This advancement supports better design and operational control in pipeline systems.</p>
	]]></content:encoded>

	<dc:title>Mathematical Modeling of Fluid Flow and Heat Transfer in the Laminar Entrance Region of a Cylindrical Pipe</dc:title>
			<dc:creator>Ismatulla Khujaev</dc:creator>
			<dc:creator>Khusniddin Mamadaliev</dc:creator>
			<dc:creator>Muzaffar Hamdamov</dc:creator>
			<dc:creator>Shohjaxon Ravshanov</dc:creator>
			<dc:creator>Makhbuba Boborakhimova</dc:creator>
			<dc:creator>Oybek Begimov</dc:creator>
			<dc:creator>Shokhrukh Chulliyev</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060140</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-04</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-04</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>140</prism:startingPage>
		<prism:doi>10.3390/fluids11060140</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/140</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/139">

	<title>Fluids, Vol. 11, Pages 139: Hydraulic Characterization of a Direct-Acting Pressure-Reducing Valve Using CFD and Experimental Validation</title>
	<link>https://www.mdpi.com/2311-5521/11/6/139</link>
	<description>This study presents the hydraulic characterization of a direct-acting pressure-reducing valve (PRV) using a combined experimental and numerical approach. An experimental test bench was implemented to measure inlet, control port, and outlet pressures over a flow rate range from 0 to 4.0 m3/h, under a constant inlet pressure of 8 bar and a set pressure of 3 bar. In parallel, a three-dimensional steady-state CFD model was developed using a sequential force balance analysis between hydraulic and spring restoring forces. The results show good agreement between numerical predictions and experimental data, with a maximum error below 10% in outlet pressure. The pressure drop exhibited a nonlinear increasing trend with flow rate, reaching values close to 1.8 bar at 4.0 m3/h. The flow coefficient Kv remained within a range of 2.2&amp;amp;ndash;3.0, while the pressure regulation coefficient S remained below 0.05, indicating stable regulation performance. Additional simulations at 25 bar provided improved agreement with manufacturer data, suggesting that catalog curves may be based on nominal pressure conditions. The proposed methodology demonstrates that steady-state CFD coupled with force balance analysis is an effective and computationally efficient approach for predicting the hydraulic behavior of direct-acting PRVs.</description>
	<pubDate>2026-06-02</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 139: Hydraulic Characterization of a Direct-Acting Pressure-Reducing Valve Using CFD and Experimental Validation</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/139">doi: 10.3390/fluids11060139</a></p>
	<p>Authors:
		Gonzalo López-Villacís
		Pablo Valle-Velasco
		Martha Sevilla-Abarca
		Diana Peralta-Zurita
		Segundo Espín-Lagos
		</p>
	<p>This study presents the hydraulic characterization of a direct-acting pressure-reducing valve (PRV) using a combined experimental and numerical approach. An experimental test bench was implemented to measure inlet, control port, and outlet pressures over a flow rate range from 0 to 4.0 m3/h, under a constant inlet pressure of 8 bar and a set pressure of 3 bar. In parallel, a three-dimensional steady-state CFD model was developed using a sequential force balance analysis between hydraulic and spring restoring forces. The results show good agreement between numerical predictions and experimental data, with a maximum error below 10% in outlet pressure. The pressure drop exhibited a nonlinear increasing trend with flow rate, reaching values close to 1.8 bar at 4.0 m3/h. The flow coefficient Kv remained within a range of 2.2&amp;amp;ndash;3.0, while the pressure regulation coefficient S remained below 0.05, indicating stable regulation performance. Additional simulations at 25 bar provided improved agreement with manufacturer data, suggesting that catalog curves may be based on nominal pressure conditions. The proposed methodology demonstrates that steady-state CFD coupled with force balance analysis is an effective and computationally efficient approach for predicting the hydraulic behavior of direct-acting PRVs.</p>
	]]></content:encoded>

	<dc:title>Hydraulic Characterization of a Direct-Acting Pressure-Reducing Valve Using CFD and Experimental Validation</dc:title>
			<dc:creator>Gonzalo López-Villacís</dc:creator>
			<dc:creator>Pablo Valle-Velasco</dc:creator>
			<dc:creator>Martha Sevilla-Abarca</dc:creator>
			<dc:creator>Diana Peralta-Zurita</dc:creator>
			<dc:creator>Segundo Espín-Lagos</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060139</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-06-02</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-06-02</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>139</prism:startingPage>
		<prism:doi>10.3390/fluids11060139</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/139</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/138">

	<title>Fluids, Vol. 11, Pages 138: Comparing Methods of Deforming and Overlapping Meshes to Simulate the Motion of Bodies on a Free Surface</title>
	<link>https://www.mdpi.com/2311-5521/11/6/138</link>
	<description>Two methods of accounting for the motion of the bodies&amp;amp;mdash;the deforming mesh method and the method of overlapping meshes (or overset mesh method)&amp;amp;mdash;are compared using problems with floating bodies, which are typical for the shipbuilding industry. Three problems are considered: oscillation of the cylinder on the water surface, movement of the box under the influence of waves, and heaving and pitching of the ship model in head waves. Numerical computations are carried out in the LOGOS software package, the simulation methodology used is based on the solution of a system of Reynolds-averaged Navier-Stokes equations, and the Volume of fluid (VOF) method to take into account the free surface. In all problems, the characteristics of the movement of bodies are evaluated; the resistance force of the ship model is also determined in the third problem; control values obtained using two methods of accounting for moving bodies are compared with the available experimental data. The results of numerical simulation have shown that both methods predict body movement parameters well; the accuracy in determining the resistance force in the task of streamlining the ship&amp;amp;rsquo;s hull is also comparable: the difference between the maximum deviations of the resistance coefficient in the computations with deformation and overlapping computation meshes is 0.5%. In the case of computations of the three-dimensional problem, the time spent when using the mesh-deformation method turned out to be 10% more; therefore, the method of overlapping meshes can be considered more optimal when solving such shipbuilding tasks as self-propelled tests and streamlining the ship&amp;amp;rsquo;s hull with and without wind and wave loads.</description>
	<pubDate>2026-05-31</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 138: Comparing Methods of Deforming and Overlapping Meshes to Simulate the Motion of Bodies on a Free Surface</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/138">doi: 10.3390/fluids11060138</a></p>
	<p>Authors:
		Andrey Kozelkov
		Andrey Kurkin
		Kseniya Plygunova
		Vadim Kurulin
		Vitaliy Gerasimov
		</p>
	<p>Two methods of accounting for the motion of the bodies&amp;amp;mdash;the deforming mesh method and the method of overlapping meshes (or overset mesh method)&amp;amp;mdash;are compared using problems with floating bodies, which are typical for the shipbuilding industry. Three problems are considered: oscillation of the cylinder on the water surface, movement of the box under the influence of waves, and heaving and pitching of the ship model in head waves. Numerical computations are carried out in the LOGOS software package, the simulation methodology used is based on the solution of a system of Reynolds-averaged Navier-Stokes equations, and the Volume of fluid (VOF) method to take into account the free surface. In all problems, the characteristics of the movement of bodies are evaluated; the resistance force of the ship model is also determined in the third problem; control values obtained using two methods of accounting for moving bodies are compared with the available experimental data. The results of numerical simulation have shown that both methods predict body movement parameters well; the accuracy in determining the resistance force in the task of streamlining the ship&amp;amp;rsquo;s hull is also comparable: the difference between the maximum deviations of the resistance coefficient in the computations with deformation and overlapping computation meshes is 0.5%. In the case of computations of the three-dimensional problem, the time spent when using the mesh-deformation method turned out to be 10% more; therefore, the method of overlapping meshes can be considered more optimal when solving such shipbuilding tasks as self-propelled tests and streamlining the ship&amp;amp;rsquo;s hull with and without wind and wave loads.</p>
	]]></content:encoded>

	<dc:title>Comparing Methods of Deforming and Overlapping Meshes to Simulate the Motion of Bodies on a Free Surface</dc:title>
			<dc:creator>Andrey Kozelkov</dc:creator>
			<dc:creator>Andrey Kurkin</dc:creator>
			<dc:creator>Kseniya Plygunova</dc:creator>
			<dc:creator>Vadim Kurulin</dc:creator>
			<dc:creator>Vitaliy Gerasimov</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060138</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-31</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-31</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>138</prism:startingPage>
		<prism:doi>10.3390/fluids11060138</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/138</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/137">

	<title>Fluids, Vol. 11, Pages 137: Rapid Prediction of Leakage Dispersion at Natural Gas Distribution Stations: A Prototype Development Using Computational Fluid Dynamics and Machine Learning</title>
	<link>https://www.mdpi.com/2311-5521/11/6/137</link>
	<description>Leakage incidents at natural gas distribution stations (NGDSs) present severe fire and explosion risks, demanding immediate, data-driven emergency responses. While crucial for minimizing hazard impacts, real-time prediction of gas dispersion ranges remains a significant operational challenge. To partially address this critical safety need, this study introduces a rapid-response prediction framework prototype integrating computational fluid dynamics (CFD) with machine learning (ML). Specifically, a comprehensive database of 500 experimentally validated CFD leakage scenarios at 60 s was developed first, specifically focusing on mapping gas concentration contours within the critical 5&amp;amp;ndash;15% flammability range. To identify the most effective real-time predictive tool, three ML algorithms, including a backpropagation neural network (BPNN), long short-term memory (LSTM), and gated recurrent unit (GRU), were evaluated. The BPNN initially outperformed the sequence models, with a coefficient of determination (R2) of 0.96, a mean squared error (MSE) of 1.35, a mean absolute error (MAE) of 0.77, a maximum absolute error (MaxAE) of 4.94 and an average training time of 4.23 s per epoch. To further meet the stringent speed and precision demands of emergency scenarios, the model was enhanced via particle swarm optimization (PSO-BPNN). This optimized framework achieved exceptional accuracy (R2 = 0.99, MSE = 0.34, and MAE = 0.38) while reducing the training time to just 1.42 s per epoch under the current computational configuration. The developed CFD-ML prototype provides a practical, highly efficient tool for NGDS operators and emergency responders, enabling them to instantly visualize hazard zones, optimize evacuation protocols, and safely mitigate leakage incidents before ignition occurs.</description>
	<pubDate>2026-05-31</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 137: Rapid Prediction of Leakage Dispersion at Natural Gas Distribution Stations: A Prototype Development Using Computational Fluid Dynamics and Machine Learning</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/137">doi: 10.3390/fluids11060137</a></p>
	<p>Authors:
		Hongfu Mi
		Runmei Zhou
		Sixu Chen
		Nanfang Li
		Aijie Huang
		Yu Feng
		Peng Shao
		Shuo Wang
		Yihui Niu
		Wenhe Wang
		Geng Tang
		Hang Yi
		</p>
	<p>Leakage incidents at natural gas distribution stations (NGDSs) present severe fire and explosion risks, demanding immediate, data-driven emergency responses. While crucial for minimizing hazard impacts, real-time prediction of gas dispersion ranges remains a significant operational challenge. To partially address this critical safety need, this study introduces a rapid-response prediction framework prototype integrating computational fluid dynamics (CFD) with machine learning (ML). Specifically, a comprehensive database of 500 experimentally validated CFD leakage scenarios at 60 s was developed first, specifically focusing on mapping gas concentration contours within the critical 5&amp;amp;ndash;15% flammability range. To identify the most effective real-time predictive tool, three ML algorithms, including a backpropagation neural network (BPNN), long short-term memory (LSTM), and gated recurrent unit (GRU), were evaluated. The BPNN initially outperformed the sequence models, with a coefficient of determination (R2) of 0.96, a mean squared error (MSE) of 1.35, a mean absolute error (MAE) of 0.77, a maximum absolute error (MaxAE) of 4.94 and an average training time of 4.23 s per epoch. To further meet the stringent speed and precision demands of emergency scenarios, the model was enhanced via particle swarm optimization (PSO-BPNN). This optimized framework achieved exceptional accuracy (R2 = 0.99, MSE = 0.34, and MAE = 0.38) while reducing the training time to just 1.42 s per epoch under the current computational configuration. The developed CFD-ML prototype provides a practical, highly efficient tool for NGDS operators and emergency responders, enabling them to instantly visualize hazard zones, optimize evacuation protocols, and safely mitigate leakage incidents before ignition occurs.</p>
	]]></content:encoded>

	<dc:title>Rapid Prediction of Leakage Dispersion at Natural Gas Distribution Stations: A Prototype Development Using Computational Fluid Dynamics and Machine Learning</dc:title>
			<dc:creator>Hongfu Mi</dc:creator>
			<dc:creator>Runmei Zhou</dc:creator>
			<dc:creator>Sixu Chen</dc:creator>
			<dc:creator>Nanfang Li</dc:creator>
			<dc:creator>Aijie Huang</dc:creator>
			<dc:creator>Yu Feng</dc:creator>
			<dc:creator>Peng Shao</dc:creator>
			<dc:creator>Shuo Wang</dc:creator>
			<dc:creator>Yihui Niu</dc:creator>
			<dc:creator>Wenhe Wang</dc:creator>
			<dc:creator>Geng Tang</dc:creator>
			<dc:creator>Hang Yi</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060137</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-31</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-31</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>137</prism:startingPage>
		<prism:doi>10.3390/fluids11060137</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/137</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/136">

	<title>Fluids, Vol. 11, Pages 136: Numerical Investigation of Spray Impingement Heat Transfer in the Film Boiling Regime</title>
	<link>https://www.mdpi.com/2311-5521/11/6/136</link>
	<description>Spray impingement cooling is a well-established heat removal technique employed across a wide range of industrial processes. A particularly significant cooling regime arises when the temperature of the cooled surface surpasses the Leidenfrost temperature of the spray. Developing an accurate numerical framework for this regime holds considerable potential for optimising industrial applications such as cryogenic machining and spray quenching. This paper presents a Eulerian&amp;amp;ndash;Lagrangian Conjugate Heat Transfer (CHT) model tailored for spray impingement under Leidenfrost conditions. Two heat transfer sub-models are incorporated to characterise droplet&amp;amp;ndash;solid thermal interaction: the first, developed by Breitenbach, is grounded in a theoretical analysis of the droplet impingement process, while the second, proposed by Deb, relies on a semi-empirical correlation. Both models were validated against an experimental correlation obtained from a literature study on orthogonal water spray impingement, yielding mean relative errors of 3.54% for the Deb model and 5.2% for the Breitenbach model across a broad range of operating conditions and surface temperatures.</description>
	<pubDate>2026-05-29</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 136: Numerical Investigation of Spray Impingement Heat Transfer in the Film Boiling Regime</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/136">doi: 10.3390/fluids11060136</a></p>
	<p>Authors:
		Mattia Pelosin
		Gianluca D’Errico
		Tommaso Lucchini
		Paolo Albertelli
		</p>
	<p>Spray impingement cooling is a well-established heat removal technique employed across a wide range of industrial processes. A particularly significant cooling regime arises when the temperature of the cooled surface surpasses the Leidenfrost temperature of the spray. Developing an accurate numerical framework for this regime holds considerable potential for optimising industrial applications such as cryogenic machining and spray quenching. This paper presents a Eulerian&amp;amp;ndash;Lagrangian Conjugate Heat Transfer (CHT) model tailored for spray impingement under Leidenfrost conditions. Two heat transfer sub-models are incorporated to characterise droplet&amp;amp;ndash;solid thermal interaction: the first, developed by Breitenbach, is grounded in a theoretical analysis of the droplet impingement process, while the second, proposed by Deb, relies on a semi-empirical correlation. Both models were validated against an experimental correlation obtained from a literature study on orthogonal water spray impingement, yielding mean relative errors of 3.54% for the Deb model and 5.2% for the Breitenbach model across a broad range of operating conditions and surface temperatures.</p>
	]]></content:encoded>

	<dc:title>Numerical Investigation of Spray Impingement Heat Transfer in the Film Boiling Regime</dc:title>
			<dc:creator>Mattia Pelosin</dc:creator>
			<dc:creator>Gianluca D’Errico</dc:creator>
			<dc:creator>Tommaso Lucchini</dc:creator>
			<dc:creator>Paolo Albertelli</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060136</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-29</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-29</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>136</prism:startingPage>
		<prism:doi>10.3390/fluids11060136</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/136</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/135">

	<title>Fluids, Vol. 11, Pages 135: Thrust Characteristics of a Ducted Fan of a Quadcopter in Various Flight Modes</title>
	<link>https://www.mdpi.com/2311-5521/11/6/135</link>
	<description>Ducted fans are widely used in vehicles with a high engine power per unit swept area, including hovercraft propulsors and vertical take-off aircraft. Computational fluid dynamics (CFD) is a powerful tool for selecting the aerodynamic configuration of new aircraft and engines and for determining their optimal operating conditions. The full Navier&amp;amp;ndash;Stokes equations, closed by the Shear Stress Transport (SST) and Spalart-Allmaras (SA) turbulence models, are used to simulate airflow induced by the rotating blades of quadcopter ducted-fan propulsors. Thrust characteristics of the ducted fan are analyzed based on numerical simulations in different flight modes, such as hovering and oblique inflow. Tip clearance and inner-wall effects on thrust and power are reported. For the studied four-blade ducted fan, varying the blade angle of attack from 16&amp;amp;#8728; to 32&amp;amp;#8728; raises the thrust coefficient from 0.27 to 0.84 and the power coefficient from 0.18 to 0.50. At a constant shaft power of 3750 W, the optimal relative tip clearance for moderately loaded blades is 1.5% (16&amp;amp;#8728; angle). For heavily loaded blades (32&amp;amp;#8728; angle), maximum thrust occurs at zero clearance. However, even at 0.8% clearance, losses are less than 0.1% compared to the closed-tip configuration. For technological reasons, a small clearance is generally preferred.</description>
	<pubDate>2026-05-29</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 135: Thrust Characteristics of a Ducted Fan of a Quadcopter in Various Flight Modes</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/135">doi: 10.3390/fluids11060135</a></p>
	<p>Authors:
		Pavel Bulat
		Pavel Chernyshov
		</p>
	<p>Ducted fans are widely used in vehicles with a high engine power per unit swept area, including hovercraft propulsors and vertical take-off aircraft. Computational fluid dynamics (CFD) is a powerful tool for selecting the aerodynamic configuration of new aircraft and engines and for determining their optimal operating conditions. The full Navier&amp;amp;ndash;Stokes equations, closed by the Shear Stress Transport (SST) and Spalart-Allmaras (SA) turbulence models, are used to simulate airflow induced by the rotating blades of quadcopter ducted-fan propulsors. Thrust characteristics of the ducted fan are analyzed based on numerical simulations in different flight modes, such as hovering and oblique inflow. Tip clearance and inner-wall effects on thrust and power are reported. For the studied four-blade ducted fan, varying the blade angle of attack from 16&amp;amp;#8728; to 32&amp;amp;#8728; raises the thrust coefficient from 0.27 to 0.84 and the power coefficient from 0.18 to 0.50. At a constant shaft power of 3750 W, the optimal relative tip clearance for moderately loaded blades is 1.5% (16&amp;amp;#8728; angle). For heavily loaded blades (32&amp;amp;#8728; angle), maximum thrust occurs at zero clearance. However, even at 0.8% clearance, losses are less than 0.1% compared to the closed-tip configuration. For technological reasons, a small clearance is generally preferred.</p>
	]]></content:encoded>

	<dc:title>Thrust Characteristics of a Ducted Fan of a Quadcopter in Various Flight Modes</dc:title>
			<dc:creator>Pavel Bulat</dc:creator>
			<dc:creator>Pavel Chernyshov</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060135</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-29</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-29</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>135</prism:startingPage>
		<prism:doi>10.3390/fluids11060135</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/135</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/134">

	<title>Fluids, Vol. 11, Pages 134: Multiphysics Modeling and Analysis of Droplet Impact on Tea Plant Leaves</title>
	<link>https://www.mdpi.com/2311-5521/11/6/134</link>
	<description>The impact of warmer droplets on cold leaves in sprinkler anti-frost is a case of agricultural engineering involving multiphysics. This study models the leaf as an elastic body of finite thickness, incorporates the temperature field, and establishes a fluid&amp;amp;ndash;solid&amp;amp;ndash;thermal multiphysics coupling model. The effects of droplet velocity, droplet diameter, and initial temperature are analyzed accordingly. The results show that the higher the Weber number (We) of the droplet, the higher the droplet spreading coefficient and the leaf stress. The maximum spreading coefficient and maximum leaf strain at We of 1583.1 are 1.58 and 4.75 times those at We of 1055.4, respectively. There is a gradual decrease in the leaf deformation, a very rapid process, a cycle of about 10% of the spreading time. The temperature at the impact point on the leaf surface increased with the droplet&amp;amp;rsquo;s initial temperature but could be influenced by an air bubble trapped at the droplet&amp;amp;rsquo;s bottom. The modeling and analysis of the dynamics of droplet impact on plant leaves enabled a better understanding of the mechanisms of sprinkler frost protection.</description>
	<pubDate>2026-05-29</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 134: Multiphysics Modeling and Analysis of Droplet Impact on Tea Plant Leaves</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/134">doi: 10.3390/fluids11060134</a></p>
	<p>Authors:
		Qingmin Pan
		Yongguang Hu
		</p>
	<p>The impact of warmer droplets on cold leaves in sprinkler anti-frost is a case of agricultural engineering involving multiphysics. This study models the leaf as an elastic body of finite thickness, incorporates the temperature field, and establishes a fluid&amp;amp;ndash;solid&amp;amp;ndash;thermal multiphysics coupling model. The effects of droplet velocity, droplet diameter, and initial temperature are analyzed accordingly. The results show that the higher the Weber number (We) of the droplet, the higher the droplet spreading coefficient and the leaf stress. The maximum spreading coefficient and maximum leaf strain at We of 1583.1 are 1.58 and 4.75 times those at We of 1055.4, respectively. There is a gradual decrease in the leaf deformation, a very rapid process, a cycle of about 10% of the spreading time. The temperature at the impact point on the leaf surface increased with the droplet&amp;amp;rsquo;s initial temperature but could be influenced by an air bubble trapped at the droplet&amp;amp;rsquo;s bottom. The modeling and analysis of the dynamics of droplet impact on plant leaves enabled a better understanding of the mechanisms of sprinkler frost protection.</p>
	]]></content:encoded>

	<dc:title>Multiphysics Modeling and Analysis of Droplet Impact on Tea Plant Leaves</dc:title>
			<dc:creator>Qingmin Pan</dc:creator>
			<dc:creator>Yongguang Hu</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060134</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-29</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-29</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>134</prism:startingPage>
		<prism:doi>10.3390/fluids11060134</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/134</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/133">

	<title>Fluids, Vol. 11, Pages 133: Hydrodynamic Synchronization of Two Oscillators in a Newtonian Fluid</title>
	<link>https://www.mdpi.com/2311-5521/11/6/133</link>
	<description>Particles moving in a fluid interact through the flow field they generate, which can lead to complex nonlinear dynamics. One important example is the synchronization of oscillatory motion in biological systems, such as the coordinated beating of cilia or flagella. In this work, we investigate the synchronization of two oscillators interacting through a Newtonian fluid using numerical simulations based on the lattice Boltzmann method. The oscillators are modeled as solid particles undergoing periodic motion, while hydrodynamic interactions are resolved explicitly through the surrounding flow. We analyze how synchronization depends on key physical parameters, including the fluid viscosity, the distance between the oscillators, the natural oscillation frequency, and the initial phase difference. The results are compared with predictions from the Kuramoto model in order to relate the hydrodynamic interaction to an effective phase coupling. We find that the coupling strength required for synchronization increases with both the oscillation frequency and the fluid viscosity, while it decreases with the distance between the oscillators. These results provide insight into the mechanisms underlying fluid-mediated synchronization and help bridge microscopic hydrodynamic models with reduced phase-oscillator descriptions.</description>
	<pubDate>2026-05-29</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 133: Hydrodynamic Synchronization of Two Oscillators in a Newtonian Fluid</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/133">doi: 10.3390/fluids11060133</a></p>
	<p>Authors:
		Tomé A. F. da Silva
		Brendon O. Pontes
		Elias S. Lima
		Rodrigo C. V. Coelho
		</p>
	<p>Particles moving in a fluid interact through the flow field they generate, which can lead to complex nonlinear dynamics. One important example is the synchronization of oscillatory motion in biological systems, such as the coordinated beating of cilia or flagella. In this work, we investigate the synchronization of two oscillators interacting through a Newtonian fluid using numerical simulations based on the lattice Boltzmann method. The oscillators are modeled as solid particles undergoing periodic motion, while hydrodynamic interactions are resolved explicitly through the surrounding flow. We analyze how synchronization depends on key physical parameters, including the fluid viscosity, the distance between the oscillators, the natural oscillation frequency, and the initial phase difference. The results are compared with predictions from the Kuramoto model in order to relate the hydrodynamic interaction to an effective phase coupling. We find that the coupling strength required for synchronization increases with both the oscillation frequency and the fluid viscosity, while it decreases with the distance between the oscillators. These results provide insight into the mechanisms underlying fluid-mediated synchronization and help bridge microscopic hydrodynamic models with reduced phase-oscillator descriptions.</p>
	]]></content:encoded>

	<dc:title>Hydrodynamic Synchronization of Two Oscillators in a Newtonian Fluid</dc:title>
			<dc:creator>Tomé A. F. da Silva</dc:creator>
			<dc:creator>Brendon O. Pontes</dc:creator>
			<dc:creator>Elias S. Lima</dc:creator>
			<dc:creator>Rodrigo C. V. Coelho</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060133</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-29</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-29</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>133</prism:startingPage>
		<prism:doi>10.3390/fluids11060133</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/133</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/132">

	<title>Fluids, Vol. 11, Pages 132: RIM-PIV Measurements of Turbulent Flow over a Rough Porous Bed</title>
	<link>https://www.mdpi.com/2311-5521/11/6/132</link>
	<description>Flow over permeable beds is important in sediment transport and mixing processes, yet detailed velocity and stress measurements remain difficult to obtain, particularly close to the sediment&amp;amp;ndash;water interface (SWI). In this work, we use refractive-index-matched PIV to study turbulent open-channel flow over and within a permeable bed composed of monodisperse borosilicate glass beads. Measurements are reported for three low-ReK cases, ReK=0.224, ReK=0.335, and ReK=0.360, to resolve the mean velocity structure and the associated viscous, turbulent, Reynolds, and dispersive stress distributions. The results show that both the mean velocity and the turbulence intensity decrease rapidly below the SWI, indicating strong damping within the porous bed. Above the bed, the flow retains a boundary-layer structure, and increasing ReK enhances the turbulence intensity without changing the overall regime. The results indicate a shift from turbulent transport above the bed to viscous control within the porous layer, while dispersive stresses peak near the interface. Overall, the SWI controls momentum exchange within a thin region and the porous bed suppresses turbulence penetration into the subsurface.</description>
	<pubDate>2026-05-27</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 132: RIM-PIV Measurements of Turbulent Flow over a Rough Porous Bed</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/132">doi: 10.3390/fluids11060132</a></p>
	<p>Authors:
		Zeeshan Qadir Memon
		James Liburdy
		</p>
	<p>Flow over permeable beds is important in sediment transport and mixing processes, yet detailed velocity and stress measurements remain difficult to obtain, particularly close to the sediment&amp;amp;ndash;water interface (SWI). In this work, we use refractive-index-matched PIV to study turbulent open-channel flow over and within a permeable bed composed of monodisperse borosilicate glass beads. Measurements are reported for three low-ReK cases, ReK=0.224, ReK=0.335, and ReK=0.360, to resolve the mean velocity structure and the associated viscous, turbulent, Reynolds, and dispersive stress distributions. The results show that both the mean velocity and the turbulence intensity decrease rapidly below the SWI, indicating strong damping within the porous bed. Above the bed, the flow retains a boundary-layer structure, and increasing ReK enhances the turbulence intensity without changing the overall regime. The results indicate a shift from turbulent transport above the bed to viscous control within the porous layer, while dispersive stresses peak near the interface. Overall, the SWI controls momentum exchange within a thin region and the porous bed suppresses turbulence penetration into the subsurface.</p>
	]]></content:encoded>

	<dc:title>RIM-PIV Measurements of Turbulent Flow over a Rough Porous Bed</dc:title>
			<dc:creator>Zeeshan Qadir Memon</dc:creator>
			<dc:creator>James Liburdy</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060132</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-27</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-27</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>132</prism:startingPage>
		<prism:doi>10.3390/fluids11060132</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/132</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/131">

	<title>Fluids, Vol. 11, Pages 131: From Black-Box Optimization to Importance-Guided Control: A Perspective on Explainable Deep Reinforcement Learning for Drag Reduction</title>
	<link>https://www.mdpi.com/2311-5521/11/6/131</link>
	<description>Fluid-dynamic drag accounts for a substantial fraction of energy consumption across air, ground, and maritime transport systems, making its reduction a critical lever for decarbonizing mobility. While active flow control (AFC) strategies have demonstrated significant drag reduction potential, their design remains constrained by heuristic physical assumptions about dominant flow structures. Recent developments in deep reinforcement learning (DRL) have emerged as a transformative paradigm, capable of autonomously discovering control strategies in high-dimensional turbulent environments. This perspective traces the evolution of drag reduction approaches from classical passive and active control approaches toward data-driven methods based on DRL. A particularly promising direction is the integration of explainable artificial intelligence (XAI) with DRL, which provides physically interpretable information about flow regions associated with drag generation and guides the learning process toward physically meaningful actuation schemes. As a result, XAI-guided DRL controllers have been shown in canonical configurations to achieve comparable or improved drag reduction with substantially lower actuation power than controllers trained directly for drag minimization. This transition from opaque optimization toward flow control informed by dynamical causal relationships represents a key step for the development of energy-efficient and sustainable flow-control solutions for transport systems.</description>
	<pubDate>2026-05-26</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 131: From Black-Box Optimization to Importance-Guided Control: A Perspective on Explainable Deep Reinforcement Learning for Drag Reduction</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/131">doi: 10.3390/fluids11060131</a></p>
	<p>Authors:
		Belén Reverte-Badillo
		Clara Trillo-Yagüe
		Andrés Cremades
		Ricardo Vinuesa
		Sergio Hoyas
		</p>
	<p>Fluid-dynamic drag accounts for a substantial fraction of energy consumption across air, ground, and maritime transport systems, making its reduction a critical lever for decarbonizing mobility. While active flow control (AFC) strategies have demonstrated significant drag reduction potential, their design remains constrained by heuristic physical assumptions about dominant flow structures. Recent developments in deep reinforcement learning (DRL) have emerged as a transformative paradigm, capable of autonomously discovering control strategies in high-dimensional turbulent environments. This perspective traces the evolution of drag reduction approaches from classical passive and active control approaches toward data-driven methods based on DRL. A particularly promising direction is the integration of explainable artificial intelligence (XAI) with DRL, which provides physically interpretable information about flow regions associated with drag generation and guides the learning process toward physically meaningful actuation schemes. As a result, XAI-guided DRL controllers have been shown in canonical configurations to achieve comparable or improved drag reduction with substantially lower actuation power than controllers trained directly for drag minimization. This transition from opaque optimization toward flow control informed by dynamical causal relationships represents a key step for the development of energy-efficient and sustainable flow-control solutions for transport systems.</p>
	]]></content:encoded>

	<dc:title>From Black-Box Optimization to Importance-Guided Control: A Perspective on Explainable Deep Reinforcement Learning for Drag Reduction</dc:title>
			<dc:creator>Belén Reverte-Badillo</dc:creator>
			<dc:creator>Clara Trillo-Yagüe</dc:creator>
			<dc:creator>Andrés Cremades</dc:creator>
			<dc:creator>Ricardo Vinuesa</dc:creator>
			<dc:creator>Sergio Hoyas</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060131</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-26</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-26</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Perspective</prism:section>
	<prism:startingPage>131</prism:startingPage>
		<prism:doi>10.3390/fluids11060131</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/131</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/130">

	<title>Fluids, Vol. 11, Pages 130: Editorial: Future Trends and Challenges in High-Performance Computing for Turbulence</title>
	<link>https://www.mdpi.com/2311-5521/11/6/130</link>
	<description>Turbulence remains one of the most persistent challenges in fluid dynamics and engineering [...]</description>
	<pubDate>2026-05-25</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 130: Editorial: Future Trends and Challenges in High-Performance Computing for Turbulence</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/130">doi: 10.3390/fluids11060130</a></p>
	<p>Authors:
		Yonghua Yan
		Yong Yang
		</p>
	<p>Turbulence remains one of the most persistent challenges in fluid dynamics and engineering [...]</p>
	]]></content:encoded>

	<dc:title>Editorial: Future Trends and Challenges in High-Performance Computing for Turbulence</dc:title>
			<dc:creator>Yonghua Yan</dc:creator>
			<dc:creator>Yong Yang</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060130</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-25</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-25</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Editorial</prism:section>
	<prism:startingPage>130</prism:startingPage>
		<prism:doi>10.3390/fluids11060130</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/130</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/6/129">

	<title>Fluids, Vol. 11, Pages 129: Hydrodynamic Analysis of Flow Inside a Novel Design for a Submerged Entry Nozzle for Steel Continuous Casting</title>
	<link>https://www.mdpi.com/2311-5521/11/6/129</link>
	<description>In slab continuous casting, the internal hydrodynamics of the submerged entry nozzle (SEN) play a determining role in mold flow stability and product quality, particularly when external electromagnetic flow-control technologies are not employed. This study analyzes a novel bifurcated SEN design intended to promote stable, highly symmetric outlet jets under asymmetric inlet flow conditions produced by typical flow-control devices. The proposed configuration combines three geometric modifications: a square-section bore, a flow-divider bottom wall derived from a rotated mountain-type geometry, and two bell-shaped protrusions that act as flow modulators positioned immediately above the outlet ports. The hydrodynamic behavior inside the nozzle was investigated using complementary experimental and numerical approaches. Physical modeling was conducted in a scaled water model using particle image velocimetry (PIV) to characterize time-averaged velocity fields and flow fluctuations. In parallel, three-dimensional large-eddy simulations (LESs) were performed to resolve transient flow structures and quantify jet characteristics at the nozzle exits. Both approaches show consistent results. The combined action of the flow modulators and the flow-divider bottom wall robustly induces the formation of two nearly identical counter-rotating vortices in the lower region of the SEN. This flow structure suppresses stagnation and recirculation zones near the outlet ports, mitigates inlet-induced asymmetries, and enhances flow evacuation efficiency. Quantitative analysis of the outlet jets indicates a significant reduction in angular dispersion and a flow-rate imbalance below 0.2%, markedly lower than that observed in conventional SEN configurations. The results demonstrate that appropriate internal geometric design can effectively stabilize SEN hydrodynamics without active control systems, offering a feasible and scalable strategy for improving mold flow stability in industrial continuous casting operations.</description>
	<pubDate>2026-05-23</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 129: Hydrodynamic Analysis of Flow Inside a Novel Design for a Submerged Entry Nozzle for Steel Continuous Casting</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/6/129">doi: 10.3390/fluids11060129</a></p>
	<p>Authors:
		Jesus Gonzalez-Trejo
		Cesar A. Real-Ramirez
		Ruslan Gabbasov
		Fernando Aragon-Rivera
		Carlos E. Alvarado-Rodriguez
		</p>
	<p>In slab continuous casting, the internal hydrodynamics of the submerged entry nozzle (SEN) play a determining role in mold flow stability and product quality, particularly when external electromagnetic flow-control technologies are not employed. This study analyzes a novel bifurcated SEN design intended to promote stable, highly symmetric outlet jets under asymmetric inlet flow conditions produced by typical flow-control devices. The proposed configuration combines three geometric modifications: a square-section bore, a flow-divider bottom wall derived from a rotated mountain-type geometry, and two bell-shaped protrusions that act as flow modulators positioned immediately above the outlet ports. The hydrodynamic behavior inside the nozzle was investigated using complementary experimental and numerical approaches. Physical modeling was conducted in a scaled water model using particle image velocimetry (PIV) to characterize time-averaged velocity fields and flow fluctuations. In parallel, three-dimensional large-eddy simulations (LESs) were performed to resolve transient flow structures and quantify jet characteristics at the nozzle exits. Both approaches show consistent results. The combined action of the flow modulators and the flow-divider bottom wall robustly induces the formation of two nearly identical counter-rotating vortices in the lower region of the SEN. This flow structure suppresses stagnation and recirculation zones near the outlet ports, mitigates inlet-induced asymmetries, and enhances flow evacuation efficiency. Quantitative analysis of the outlet jets indicates a significant reduction in angular dispersion and a flow-rate imbalance below 0.2%, markedly lower than that observed in conventional SEN configurations. The results demonstrate that appropriate internal geometric design can effectively stabilize SEN hydrodynamics without active control systems, offering a feasible and scalable strategy for improving mold flow stability in industrial continuous casting operations.</p>
	]]></content:encoded>

	<dc:title>Hydrodynamic Analysis of Flow Inside a Novel Design for a Submerged Entry Nozzle for Steel Continuous Casting</dc:title>
			<dc:creator>Jesus Gonzalez-Trejo</dc:creator>
			<dc:creator>Cesar A. Real-Ramirez</dc:creator>
			<dc:creator>Ruslan Gabbasov</dc:creator>
			<dc:creator>Fernando Aragon-Rivera</dc:creator>
			<dc:creator>Carlos E. Alvarado-Rodriguez</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11060129</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-23</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-23</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>6</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>129</prism:startingPage>
		<prism:doi>10.3390/fluids11060129</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/6/129</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/127">

	<title>Fluids, Vol. 11, Pages 127: Effects of Permeability and Gravity on Capillary Imbibition in Filter Paper</title>
	<link>https://www.mdpi.com/2311-5521/11/5/127</link>
	<description>Capillary imbibition is the process by which liquids are absorbed into porous materials as a result of capillary pressure differences at the pore scale. Accurate characterization of imbibition dynamics, particularly in the presence of gravitational potential, is essential for understanding fluid transport in diverse systems such as soil, fractured rocks, filtration media, and plant roots. This study presents systematic imbibition experiments using filter papers with pore sizes of 2.5 &amp;amp;micro;m, 11 &amp;amp;micro;m, and 20 &amp;amp;micro;m, each inclined at 80&amp;amp;deg; to quantify the influence of gravitational potential on imbibition behavior. For horizontally positioned samples, the imbibition front propagated radially and symmetrically, exhibiting a power law dependence on time. The measured temporal exponents ranged from 0.386 to 0.403, consistently lower than the theoretical value of 1/2 predicted by the Lucas&amp;amp;ndash;Washburn law. With increasing permeability, the temporal exponent approached the Washburn limit, indicating a marked dependence of imbibition dynamics on pore structure. For the inclined configuration at an 80&amp;amp;deg; angle, the imbibition fronts remained nearly circular but exhibited a pronounced displacement of the front center toward gravity. This displacement increased with permeability, from approximately 0.497 cm for the 11 &amp;amp;micro;m filter paper to 3545 cm for the 20 &amp;amp;micro;m filter paper, highlighting the combined effects of permeability and gravitational potential on fluid movement. Furthermore, the advance of the imbibition front was significantly slower in the smallest pores (2.5 &amp;amp;micro;m) compared to the larger ones. Experimental results were evaluated against a theoretical model proposed by Medina, demonstrating moderate quantitative agreement at early times, when gravitational potential effects are less significant. These findings confirm that both the temporal scaling exponent and the spatial evolution of the imbibition front are governed by the porous medium&amp;amp;rsquo;s permeability and inclination angle, providing experimental evidence of deviations from ideal Washburn behavior in real porous systems.</description>
	<pubDate>2026-05-21</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 127: Effects of Permeability and Gravity on Capillary Imbibition in Filter Paper</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/127">doi: 10.3390/fluids11050127</a></p>
	<p>Authors:
		Josefina Janeth Miranda-Blancas
		José Martínez-Trinidad
		Abraham Medina-Ovando
		Luis Alfonso Moreno-Pacheco
		Fernando Alonso-Cruz
		Osvaldo Quintana-Hernández
		Ricardo Andrés García-León
		</p>
	<p>Capillary imbibition is the process by which liquids are absorbed into porous materials as a result of capillary pressure differences at the pore scale. Accurate characterization of imbibition dynamics, particularly in the presence of gravitational potential, is essential for understanding fluid transport in diverse systems such as soil, fractured rocks, filtration media, and plant roots. This study presents systematic imbibition experiments using filter papers with pore sizes of 2.5 &amp;amp;micro;m, 11 &amp;amp;micro;m, and 20 &amp;amp;micro;m, each inclined at 80&amp;amp;deg; to quantify the influence of gravitational potential on imbibition behavior. For horizontally positioned samples, the imbibition front propagated radially and symmetrically, exhibiting a power law dependence on time. The measured temporal exponents ranged from 0.386 to 0.403, consistently lower than the theoretical value of 1/2 predicted by the Lucas&amp;amp;ndash;Washburn law. With increasing permeability, the temporal exponent approached the Washburn limit, indicating a marked dependence of imbibition dynamics on pore structure. For the inclined configuration at an 80&amp;amp;deg; angle, the imbibition fronts remained nearly circular but exhibited a pronounced displacement of the front center toward gravity. This displacement increased with permeability, from approximately 0.497 cm for the 11 &amp;amp;micro;m filter paper to 3545 cm for the 20 &amp;amp;micro;m filter paper, highlighting the combined effects of permeability and gravitational potential on fluid movement. Furthermore, the advance of the imbibition front was significantly slower in the smallest pores (2.5 &amp;amp;micro;m) compared to the larger ones. Experimental results were evaluated against a theoretical model proposed by Medina, demonstrating moderate quantitative agreement at early times, when gravitational potential effects are less significant. These findings confirm that both the temporal scaling exponent and the spatial evolution of the imbibition front are governed by the porous medium&amp;amp;rsquo;s permeability and inclination angle, providing experimental evidence of deviations from ideal Washburn behavior in real porous systems.</p>
	]]></content:encoded>

	<dc:title>Effects of Permeability and Gravity on Capillary Imbibition in Filter Paper</dc:title>
			<dc:creator>Josefina Janeth Miranda-Blancas</dc:creator>
			<dc:creator>José Martínez-Trinidad</dc:creator>
			<dc:creator>Abraham Medina-Ovando</dc:creator>
			<dc:creator>Luis Alfonso Moreno-Pacheco</dc:creator>
			<dc:creator>Fernando Alonso-Cruz</dc:creator>
			<dc:creator>Osvaldo Quintana-Hernández</dc:creator>
			<dc:creator>Ricardo Andrés García-León</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050127</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-21</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-21</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>127</prism:startingPage>
		<prism:doi>10.3390/fluids11050127</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/127</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/128">

	<title>Fluids, Vol. 11, Pages 128: Orientation-Dependent Drag Crisis and Flight Response of the FIFA World Cup Match Ball Trionda</title>
	<link>https://www.mdpi.com/2311-5521/11/5/128</link>
	<description>Surface orientation can influence the aerodynamic response of modern soccer balls, particularly in the drag crisis regime. This study quantified the orientation-dependent aerodynamic characteristics of the FIFA World Cup match ball Trionda using a single specimen and examined how these differences affect simulated flight at sea level and 1500 m altitude. Two reproducible reference orientations were defined: a red-panel-centered orientation (Series A) and a seam-junction-centered orientation (Series B). Each reference orientation was rotated by 0&amp;amp;deg;, 90&amp;amp;deg;, and 180&amp;amp;deg;, resulting in six fixed-orientation conditions. Wind tunnel measurements were repeated three times per condition to obtain drag, lift, and side-force coefficients, and two-dimensional non-spinning flight simulations were performed for representative long-kick and free-kick conditions. All six orientations exhibited drag crisis behavior, but the transition response magnitude, subcritical drag level, and supercritical drag state differed among conditions. The representative transition region occurred at approximately Re = 2.0 &amp;amp;times; 105 to 2.5 &amp;amp;times; 105. Among the tested conditions, B-90 showed the lowest full-range mean drag coefficient (0.231), whereas A-90 showed the highest (0.266). In the simulations, lower drag orientations consistently produced longer flight ranges, and the B-90 &amp;amp;gt; A-90 ordering was preserved across representative launch conditions and the expanded parametric comparison. These findings indicate that the aerodynamic response of Trionda cannot be represented adequately by a single mean drag coefficient and that surface orientation should be considered in aerodynamic characterization and flight prediction.</description>
	<pubDate>2026-05-21</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 128: Orientation-Dependent Drag Crisis and Flight Response of the FIFA World Cup Match Ball Trionda</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/128">doi: 10.3390/fluids11050128</a></p>
	<p>Authors:
		Sungchan Hong
		Takeshi Asai
		</p>
	<p>Surface orientation can influence the aerodynamic response of modern soccer balls, particularly in the drag crisis regime. This study quantified the orientation-dependent aerodynamic characteristics of the FIFA World Cup match ball Trionda using a single specimen and examined how these differences affect simulated flight at sea level and 1500 m altitude. Two reproducible reference orientations were defined: a red-panel-centered orientation (Series A) and a seam-junction-centered orientation (Series B). Each reference orientation was rotated by 0&amp;amp;deg;, 90&amp;amp;deg;, and 180&amp;amp;deg;, resulting in six fixed-orientation conditions. Wind tunnel measurements were repeated three times per condition to obtain drag, lift, and side-force coefficients, and two-dimensional non-spinning flight simulations were performed for representative long-kick and free-kick conditions. All six orientations exhibited drag crisis behavior, but the transition response magnitude, subcritical drag level, and supercritical drag state differed among conditions. The representative transition region occurred at approximately Re = 2.0 &amp;amp;times; 105 to 2.5 &amp;amp;times; 105. Among the tested conditions, B-90 showed the lowest full-range mean drag coefficient (0.231), whereas A-90 showed the highest (0.266). In the simulations, lower drag orientations consistently produced longer flight ranges, and the B-90 &amp;amp;gt; A-90 ordering was preserved across representative launch conditions and the expanded parametric comparison. These findings indicate that the aerodynamic response of Trionda cannot be represented adequately by a single mean drag coefficient and that surface orientation should be considered in aerodynamic characterization and flight prediction.</p>
	]]></content:encoded>

	<dc:title>Orientation-Dependent Drag Crisis and Flight Response of the FIFA World Cup Match Ball Trionda</dc:title>
			<dc:creator>Sungchan Hong</dc:creator>
			<dc:creator>Takeshi Asai</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050128</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-21</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-21</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>128</prism:startingPage>
		<prism:doi>10.3390/fluids11050128</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/128</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/126">

	<title>Fluids, Vol. 11, Pages 126: Numerical Simulation of Separation Characteristics of Particles Enhanced by Synergistic Extraction&amp;ndash;Shearing</title>
	<link>https://www.mdpi.com/2311-5521/11/5/126</link>
	<description>This study utilizes computational fluid dynamics (CFD), numerical simulation of particle separation characteristics enhanced by synergistic extraction&amp;amp;ndash;shearing is performed, and the two-phase flow in a liquid&amp;amp;ndash;solid stirred tank is simulated using the Eulerian&amp;amp;ndash;Eulerian two-fluid model and the standard k&amp;amp;minus;&amp;amp;epsilon; model. The effects of impeller speed, the hole arrangement pattern of the annular shroud, and the hole area on the multiphase fluid dynamics behavior and stirring power inside the tank are systematically studied. The results show that stirring speed is a key operating parameter affecting turbulence intensity and particle mixing uniformity. When the stirring speed increases from 2000 r/min to 4000 r/min, the overall tank turbulence increases significantly, but the stirring power increases from 4.69 kW to 36.57 kW. The annular cover at the bottom is arranged with vertical openings, which enables full energy transfer within the tank and effectively enhances the turbulence intensity in the middle and lower sections of the flow field; the horizontal opening form is more conducive to the radial diffusion of particles in the middle layer. Reducing the hole area by half increases the fluid jet velocity and local shear stress, effectively improving particle distribution uniformity, while the stirring power decreases by 43.75%, thereby achieving the collaborative optimization of mixing efficiency and energy consumption.</description>
	<pubDate>2026-05-20</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 126: Numerical Simulation of Separation Characteristics of Particles Enhanced by Synergistic Extraction&amp;ndash;Shearing</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/126">doi: 10.3390/fluids11050126</a></p>
	<p>Authors:
		Kai Wu
		Lixia Hu
		Zhanghao Wan
		Fupeng Liu
		Tao Jiang
		Qiang Zhou
		Li Luo
		</p>
	<p>This study utilizes computational fluid dynamics (CFD), numerical simulation of particle separation characteristics enhanced by synergistic extraction&amp;amp;ndash;shearing is performed, and the two-phase flow in a liquid&amp;amp;ndash;solid stirred tank is simulated using the Eulerian&amp;amp;ndash;Eulerian two-fluid model and the standard k&amp;amp;minus;&amp;amp;epsilon; model. The effects of impeller speed, the hole arrangement pattern of the annular shroud, and the hole area on the multiphase fluid dynamics behavior and stirring power inside the tank are systematically studied. The results show that stirring speed is a key operating parameter affecting turbulence intensity and particle mixing uniformity. When the stirring speed increases from 2000 r/min to 4000 r/min, the overall tank turbulence increases significantly, but the stirring power increases from 4.69 kW to 36.57 kW. The annular cover at the bottom is arranged with vertical openings, which enables full energy transfer within the tank and effectively enhances the turbulence intensity in the middle and lower sections of the flow field; the horizontal opening form is more conducive to the radial diffusion of particles in the middle layer. Reducing the hole area by half increases the fluid jet velocity and local shear stress, effectively improving particle distribution uniformity, while the stirring power decreases by 43.75%, thereby achieving the collaborative optimization of mixing efficiency and energy consumption.</p>
	]]></content:encoded>

	<dc:title>Numerical Simulation of Separation Characteristics of Particles Enhanced by Synergistic Extraction&amp;amp;ndash;Shearing</dc:title>
			<dc:creator>Kai Wu</dc:creator>
			<dc:creator>Lixia Hu</dc:creator>
			<dc:creator>Zhanghao Wan</dc:creator>
			<dc:creator>Fupeng Liu</dc:creator>
			<dc:creator>Tao Jiang</dc:creator>
			<dc:creator>Qiang Zhou</dc:creator>
			<dc:creator>Li Luo</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050126</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-20</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-20</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>126</prism:startingPage>
		<prism:doi>10.3390/fluids11050126</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/126</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/125">

	<title>Fluids, Vol. 11, Pages 125: An Investigation into Dry Gas Seals with Different Groove Structures</title>
	<link>https://www.mdpi.com/2311-5521/11/5/125</link>
	<description>Dry gas seals (DGSs) are currently the preferred sealing method for high-speed rotating machinery, widely used in the fields of petrochemicals and energy and power. This study analyzes the effect of groove structure and operating parameters (rotary ring speed and inlet pressure) on the performance of the sealing system. The results show that a swallowtail-like groove demonstrates a dual effect of improving film stability and reducing leakage under specific working conditions. Specifically, under the inlet pressure of 4.5852 MPa and rotational speed of 10,380 rpm, the swallowtail-like groove achieves a 1.84% reduction in leakage and a 0.32% increase in opening force compared with a conventional spiral groove. Rotational speed has the greatest impact on the gas film stability of the cluster spiral groove. Increasing inlet pressure enhances the dynamic stabilization of gas film. Dynamic analysis indicates that the opening force demonstrates a linear proportionality with inlet pressure, whereas leakage follows an exponential growth. This work can provide guidance for optimizing the groove structure in dry gas sealing systems.</description>
	<pubDate>2026-05-20</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 125: An Investigation into Dry Gas Seals with Different Groove Structures</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/125">doi: 10.3390/fluids11050125</a></p>
	<p>Authors:
		Yu-Wei Wang
		Bin-Bin Wu
		Wen-Qing Li
		Shuai Xu
		Zhe-Hui Ma
		Tian-Xiao Zhang
		Chuang Liu
		Jin-Yuan Qian
		</p>
	<p>Dry gas seals (DGSs) are currently the preferred sealing method for high-speed rotating machinery, widely used in the fields of petrochemicals and energy and power. This study analyzes the effect of groove structure and operating parameters (rotary ring speed and inlet pressure) on the performance of the sealing system. The results show that a swallowtail-like groove demonstrates a dual effect of improving film stability and reducing leakage under specific working conditions. Specifically, under the inlet pressure of 4.5852 MPa and rotational speed of 10,380 rpm, the swallowtail-like groove achieves a 1.84% reduction in leakage and a 0.32% increase in opening force compared with a conventional spiral groove. Rotational speed has the greatest impact on the gas film stability of the cluster spiral groove. Increasing inlet pressure enhances the dynamic stabilization of gas film. Dynamic analysis indicates that the opening force demonstrates a linear proportionality with inlet pressure, whereas leakage follows an exponential growth. This work can provide guidance for optimizing the groove structure in dry gas sealing systems.</p>
	]]></content:encoded>

	<dc:title>An Investigation into Dry Gas Seals with Different Groove Structures</dc:title>
			<dc:creator>Yu-Wei Wang</dc:creator>
			<dc:creator>Bin-Bin Wu</dc:creator>
			<dc:creator>Wen-Qing Li</dc:creator>
			<dc:creator>Shuai Xu</dc:creator>
			<dc:creator>Zhe-Hui Ma</dc:creator>
			<dc:creator>Tian-Xiao Zhang</dc:creator>
			<dc:creator>Chuang Liu</dc:creator>
			<dc:creator>Jin-Yuan Qian</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050125</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-20</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-20</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>125</prism:startingPage>
		<prism:doi>10.3390/fluids11050125</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/125</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/124">

	<title>Fluids, Vol. 11, Pages 124: Ester and Amide Functionalization of Maleated Polyolefins as Pour Point Depressants for Kumkol Waxy Crude Oil</title>
	<link>https://www.mdpi.com/2311-5521/11/5/124</link>
	<description>Pour point depressants (PPDs) based on functionalized polyolefins were obtained and evaluated for their efficiency in pour point reducing of Kumkol waxy crude oil (Kazakhstan), which contains 15.2 wt.% paraffin and has a pour point of +17 &amp;amp;deg;C. An ethylene&amp;amp;ndash;propylene copolymer (EPR-505A) was treated through grafting of maleic anhydride (MA-g-PO) and then converted into three different derivatives that had an identical polymer backbone: an ester-functionalized, an amide-functionalized, and a combined ester&amp;amp;ndash;amide additive. The obtained products were tested at 500 g/t through kinematic viscosity measurements, equilibrium and kinetic interfacial tension analysis, pour point determination, cooling curve analysis, and optical microscopy. The ester derivative reduced the pour point by 7 &amp;amp;deg;C, the amide derivative did so by 5 &amp;amp;deg;C, and the combined additive achieved a 10 &amp;amp;deg;C pour point reduction and a more than twofold decrease in kinematic viscosity at 0 &amp;amp;deg;C. Interfacial tension measurements and adsorption kinetics allowed us to assume that ester groups govern macromolecular solubility and diffusion mobility, while amide groups enhance adsorption affinity at paraffin crystal surfaces. Their combined action shifts crystallization from a collective to a dispersed regime. These findings establish structure&amp;amp;ndash;activity relationships between polar group architecture and PPD efficiency.</description>
	<pubDate>2026-05-20</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 124: Ester and Amide Functionalization of Maleated Polyolefins as Pour Point Depressants for Kumkol Waxy Crude Oil</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/124">doi: 10.3390/fluids11050124</a></p>
	<p>Authors:
		Assel Begimova
		Zhanna Nadirova
		Kazim Nadirov
		Gulmira Bimbetova
		Berik Sakybayev
		</p>
	<p>Pour point depressants (PPDs) based on functionalized polyolefins were obtained and evaluated for their efficiency in pour point reducing of Kumkol waxy crude oil (Kazakhstan), which contains 15.2 wt.% paraffin and has a pour point of +17 &amp;amp;deg;C. An ethylene&amp;amp;ndash;propylene copolymer (EPR-505A) was treated through grafting of maleic anhydride (MA-g-PO) and then converted into three different derivatives that had an identical polymer backbone: an ester-functionalized, an amide-functionalized, and a combined ester&amp;amp;ndash;amide additive. The obtained products were tested at 500 g/t through kinematic viscosity measurements, equilibrium and kinetic interfacial tension analysis, pour point determination, cooling curve analysis, and optical microscopy. The ester derivative reduced the pour point by 7 &amp;amp;deg;C, the amide derivative did so by 5 &amp;amp;deg;C, and the combined additive achieved a 10 &amp;amp;deg;C pour point reduction and a more than twofold decrease in kinematic viscosity at 0 &amp;amp;deg;C. Interfacial tension measurements and adsorption kinetics allowed us to assume that ester groups govern macromolecular solubility and diffusion mobility, while amide groups enhance adsorption affinity at paraffin crystal surfaces. Their combined action shifts crystallization from a collective to a dispersed regime. These findings establish structure&amp;amp;ndash;activity relationships between polar group architecture and PPD efficiency.</p>
	]]></content:encoded>

	<dc:title>Ester and Amide Functionalization of Maleated Polyolefins as Pour Point Depressants for Kumkol Waxy Crude Oil</dc:title>
			<dc:creator>Assel Begimova</dc:creator>
			<dc:creator>Zhanna Nadirova</dc:creator>
			<dc:creator>Kazim Nadirov</dc:creator>
			<dc:creator>Gulmira Bimbetova</dc:creator>
			<dc:creator>Berik Sakybayev</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050124</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-20</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-20</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>124</prism:startingPage>
		<prism:doi>10.3390/fluids11050124</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/124</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/123">

	<title>Fluids, Vol. 11, Pages 123: Evaluation of Surface Roughness, Cutting Forces, and Tool Wear Under MQL Using Different Nano Cutting Oils in Milling Hastelloy C276 Superalloy</title>
	<link>https://www.mdpi.com/2311-5521/11/5/123</link>
	<description>This paper presents a study on evaluating the effectiveness of nanofluid Minimum Quantity Lubrication (NF MQL) in machining Hastelloy C276 alloy&amp;amp;mdash;a difficult-to-cut material. The study compares NF MQL using different types of nanoparticles (Al2O3, MoS2, SiC, and GrP) with dry and pure MQL conditions in terms of surface roughness, cutting force components, and especially the variation of cutting forces over time. Experimental results indicate that the graphene-containing nanofluid MQL showed the most superior performance in terms of surface roughness Ra with 54.3% and 34% reduction, followed by MoS2 and Al2O3 nanofluid MQL conditions. Regarding the active cutting force Fa, Al2O3 nanofluid MQL achieves the largest reduction of about 18.4% and 22.1% when compared to dry and pure MQL, followed by GrP nanofluid MQL, MoS2 nanofluid MQL, and then SiC nanofluid MQL. Meanwhile, GrP nanofluid MQL shows the highest percentage of Fz reduction at about 13.4% and 26% when compared to the dry and pure MQL conditions, followed by MoS2 nanofluid MQL. Furthermore, the application of NF MQL also significantly improves tool life and extends about 36.4 &amp;amp;divide; 61.1% and 18.2 &amp;amp;divide; 50% compared to dry and pure MQL, respectively. Notably, through in-depth analysis of the variation of cutting forces, the study has elucidated the superior lubrication and cooling mechanism of the NF MQL method, confirming its potential application in machining advanced materials.</description>
	<pubDate>2026-05-19</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 123: Evaluation of Surface Roughness, Cutting Forces, and Tool Wear Under MQL Using Different Nano Cutting Oils in Milling Hastelloy C276 Superalloy</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/123">doi: 10.3390/fluids11050123</a></p>
	<p>Authors:
		Nguyen The Doan
		Ngo Minh Tuan
		Vu Lai Hoang
		Tran The Long
		</p>
	<p>This paper presents a study on evaluating the effectiveness of nanofluid Minimum Quantity Lubrication (NF MQL) in machining Hastelloy C276 alloy&amp;amp;mdash;a difficult-to-cut material. The study compares NF MQL using different types of nanoparticles (Al2O3, MoS2, SiC, and GrP) with dry and pure MQL conditions in terms of surface roughness, cutting force components, and especially the variation of cutting forces over time. Experimental results indicate that the graphene-containing nanofluid MQL showed the most superior performance in terms of surface roughness Ra with 54.3% and 34% reduction, followed by MoS2 and Al2O3 nanofluid MQL conditions. Regarding the active cutting force Fa, Al2O3 nanofluid MQL achieves the largest reduction of about 18.4% and 22.1% when compared to dry and pure MQL, followed by GrP nanofluid MQL, MoS2 nanofluid MQL, and then SiC nanofluid MQL. Meanwhile, GrP nanofluid MQL shows the highest percentage of Fz reduction at about 13.4% and 26% when compared to the dry and pure MQL conditions, followed by MoS2 nanofluid MQL. Furthermore, the application of NF MQL also significantly improves tool life and extends about 36.4 &amp;amp;divide; 61.1% and 18.2 &amp;amp;divide; 50% compared to dry and pure MQL, respectively. Notably, through in-depth analysis of the variation of cutting forces, the study has elucidated the superior lubrication and cooling mechanism of the NF MQL method, confirming its potential application in machining advanced materials.</p>
	]]></content:encoded>

	<dc:title>Evaluation of Surface Roughness, Cutting Forces, and Tool Wear Under MQL Using Different Nano Cutting Oils in Milling Hastelloy C276 Superalloy</dc:title>
			<dc:creator>Nguyen The Doan</dc:creator>
			<dc:creator>Ngo Minh Tuan</dc:creator>
			<dc:creator>Vu Lai Hoang</dc:creator>
			<dc:creator>Tran The Long</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050123</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-19</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-19</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>123</prism:startingPage>
		<prism:doi>10.3390/fluids11050123</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/123</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/122">

	<title>Fluids, Vol. 11, Pages 122: Multi-Scenario Resistance Optimisation of an Indonesian Pioneer Vessel Through Response Surface Method</title>
	<link>https://www.mdpi.com/2311-5521/11/5/122</link>
	<description>Improving ship hydrodynamic efficiency is an important strategy for reducing fuel consumption and operational costs. This study investigates the optimisation of ship resistance through a combined approach involving hull form modification and operational trim adjustment. The research focuses on a pioneer vessel model, where hydrodynamic performance is analysed using Computational Fluid Dynamics (CFD) simulations coupled with Central Composite Design (CCD) and the Response Surface Methodology (RSM). Prior to the optimisation analysis, the CFD model was verified through a grid convergence study and validated against towing tank experimental data, showing good agreement. The optimisation was conducted through three scenarios: hull form optimisation, trim optimisation, and integrated optimisation, which combined both strategies. The statistical analysis revealed that longitudinal parameters play a dominant role in resistance reduction. In particular, the longitudinal centre of buoyancy (LCB) was identified as the most influential parameter in hull form optimisation, while the longitudinal centre of gravity (LCG) was the dominant parameter in trim optimisation. The results show that hull form optimisation alone reduced resistance by approximately 6%, while trim optimisation achieved a reduction of about 4%. The integrated optimisation strategy produced the greatest improvement, resulting in resistance reduction of nearly 10% compared with the baseline configuration. The findings highlight the importance of integrating design-stage optimisation and operational optimisation in improving ship hydrodynamic performance. However, the optimisation was limited to calm-water conditions.</description>
	<pubDate>2026-05-18</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 122: Multi-Scenario Resistance Optimisation of an Indonesian Pioneer Vessel Through Response Surface Method</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/122">doi: 10.3390/fluids11050122</a></p>
	<p>Authors:
		Muhammad Iqbal
		Andi Trimulyono
		Ammarunissa Noor Asiyah Raihannanda
		Azka Maulana Widestra
		Berlian Arswendo Adietya
		Ahmad Firdhaus
		</p>
	<p>Improving ship hydrodynamic efficiency is an important strategy for reducing fuel consumption and operational costs. This study investigates the optimisation of ship resistance through a combined approach involving hull form modification and operational trim adjustment. The research focuses on a pioneer vessel model, where hydrodynamic performance is analysed using Computational Fluid Dynamics (CFD) simulations coupled with Central Composite Design (CCD) and the Response Surface Methodology (RSM). Prior to the optimisation analysis, the CFD model was verified through a grid convergence study and validated against towing tank experimental data, showing good agreement. The optimisation was conducted through three scenarios: hull form optimisation, trim optimisation, and integrated optimisation, which combined both strategies. The statistical analysis revealed that longitudinal parameters play a dominant role in resistance reduction. In particular, the longitudinal centre of buoyancy (LCB) was identified as the most influential parameter in hull form optimisation, while the longitudinal centre of gravity (LCG) was the dominant parameter in trim optimisation. The results show that hull form optimisation alone reduced resistance by approximately 6%, while trim optimisation achieved a reduction of about 4%. The integrated optimisation strategy produced the greatest improvement, resulting in resistance reduction of nearly 10% compared with the baseline configuration. The findings highlight the importance of integrating design-stage optimisation and operational optimisation in improving ship hydrodynamic performance. However, the optimisation was limited to calm-water conditions.</p>
	]]></content:encoded>

	<dc:title>Multi-Scenario Resistance Optimisation of an Indonesian Pioneer Vessel Through Response Surface Method</dc:title>
			<dc:creator>Muhammad Iqbal</dc:creator>
			<dc:creator>Andi Trimulyono</dc:creator>
			<dc:creator>Ammarunissa Noor Asiyah Raihannanda</dc:creator>
			<dc:creator>Azka Maulana Widestra</dc:creator>
			<dc:creator>Berlian Arswendo Adietya</dc:creator>
			<dc:creator>Ahmad Firdhaus</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050122</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-18</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-18</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>122</prism:startingPage>
		<prism:doi>10.3390/fluids11050122</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/122</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/121">

	<title>Fluids, Vol. 11, Pages 121: Active Flow Control for High-Speed Trains: From Local Flow Manipulation to Mission-Adaptive Aerodynamic Control</title>
	<link>https://www.mdpi.com/2311-5521/11/5/121</link>
	<description>High-speed train aerodynamics have mainly been improved by passive design methods, such as streamlined noses, local fairings, and surface smoothing. These methods have achieved clear benefits, but several important aerodynamic problems remain difficult to solve by geometry optimization alone. Open-air drag is still affected by tail flow separation, base-pressure recovery, and disturbances around bogies and the underbody; crosswind safety is influenced by unsteady leeward-side separation and wake asymmetry; slipstream behavior depends on wake vortices, boundary-layer development, and complex near-ground underbody flow; and tunnel-related pressure transients arise from compression-wave generation, propagation, and reflection. These coupled effects mean that one fixed train shape cannot perform optimally in all operating conditions. For this reason, this review proposes that active flow control (AFC) should not be regarded only as a drag-reduction or stability-improvement technique for high-speed trains. Instead, it should be understood as a mission-adaptive aerodynamic control framework, in which different control actions are used for different operating scenarios. This paper first clarifies that passive optimization is increasingly subject to diminishing returns under multi-objective and engineering constraints. It then reviews AFC studies on drag reduction, base-pressure recovery, wake and slipstream control, underbody flow conditioning, crosswind mitigation, and tunnel pressure-wave suppression. Related AFC studies on bluff bodies, road vehicles, and other separated flows are included only when their physical relevance to trains is clear. The review further distinguishes gross aerodynamic improvement from net energy gain and identifies actuator power, durability, maintainability, acoustic impact, validation level, and full-scale transferability as decisive feasibility factors. Current research is still dominated by open-loop numerical studies with simplified actuation. Future work should therefore move toward multi-objective, closed-loop, energy-aware, sensor&amp;amp;ndash;actuator-integrated, and explainable machine-learning-assisted AFC. The main message is that the next step in train aerodynamics is not simply a better fixed shape, but a control-enabled train that can selectively redistribute aerodynamic authority across its mission profile.</description>
	<pubDate>2026-05-17</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 121: Active Flow Control for High-Speed Trains: From Local Flow Manipulation to Mission-Adaptive Aerodynamic Control</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/121">doi: 10.3390/fluids11050121</a></p>
	<p>Authors:
		Li Sheng
		Kaimin Wang
		Xiaodong Chen
		Yujun Liu
		Tanghong Liu
		</p>
	<p>High-speed train aerodynamics have mainly been improved by passive design methods, such as streamlined noses, local fairings, and surface smoothing. These methods have achieved clear benefits, but several important aerodynamic problems remain difficult to solve by geometry optimization alone. Open-air drag is still affected by tail flow separation, base-pressure recovery, and disturbances around bogies and the underbody; crosswind safety is influenced by unsteady leeward-side separation and wake asymmetry; slipstream behavior depends on wake vortices, boundary-layer development, and complex near-ground underbody flow; and tunnel-related pressure transients arise from compression-wave generation, propagation, and reflection. These coupled effects mean that one fixed train shape cannot perform optimally in all operating conditions. For this reason, this review proposes that active flow control (AFC) should not be regarded only as a drag-reduction or stability-improvement technique for high-speed trains. Instead, it should be understood as a mission-adaptive aerodynamic control framework, in which different control actions are used for different operating scenarios. This paper first clarifies that passive optimization is increasingly subject to diminishing returns under multi-objective and engineering constraints. It then reviews AFC studies on drag reduction, base-pressure recovery, wake and slipstream control, underbody flow conditioning, crosswind mitigation, and tunnel pressure-wave suppression. Related AFC studies on bluff bodies, road vehicles, and other separated flows are included only when their physical relevance to trains is clear. The review further distinguishes gross aerodynamic improvement from net energy gain and identifies actuator power, durability, maintainability, acoustic impact, validation level, and full-scale transferability as decisive feasibility factors. Current research is still dominated by open-loop numerical studies with simplified actuation. Future work should therefore move toward multi-objective, closed-loop, energy-aware, sensor&amp;amp;ndash;actuator-integrated, and explainable machine-learning-assisted AFC. The main message is that the next step in train aerodynamics is not simply a better fixed shape, but a control-enabled train that can selectively redistribute aerodynamic authority across its mission profile.</p>
	]]></content:encoded>

	<dc:title>Active Flow Control for High-Speed Trains: From Local Flow Manipulation to Mission-Adaptive Aerodynamic Control</dc:title>
			<dc:creator>Li Sheng</dc:creator>
			<dc:creator>Kaimin Wang</dc:creator>
			<dc:creator>Xiaodong Chen</dc:creator>
			<dc:creator>Yujun Liu</dc:creator>
			<dc:creator>Tanghong Liu</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050121</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-17</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-17</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Review</prism:section>
	<prism:startingPage>121</prism:startingPage>
		<prism:doi>10.3390/fluids11050121</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/121</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/120">

	<title>Fluids, Vol. 11, Pages 120: Development of Methods for Real-Time In-Line Monitoring of Yield Stress for Non-Newtonian Fluid Using Pressure Drop and Liquid Rise Method During the Transfer of Radioactive Waste</title>
	<link>https://www.mdpi.com/2311-5521/11/5/120</link>
	<description>Real-Time In-Line Monitoring (RTIM) of rheological properties such as slurry yield stress is important in different industries for its various benefits such as significant time savings and increased safety/efficiency of processes while reducing secondary waste due to sampling or inaccurate procedures. This paper discusses two methods for characterizing yield stress in real time: the Pressure Loss method and the Liquid Rise method. The Liquid Rise method uses the height of the slurry in a vertical column and the pressure difference to quantify the yield stress. The Pressure Loss method uses the drop of pressure in a laminar flow of slurry to determine the yield stress. Kaolin&amp;amp;ndash;water slurry is used as a simulant of the non-Newtonian fluid. An experimental setup is built to demonstrate the methods, and data obtained from the experimental setup is compared with the yield stress obtained from a conventional table-top rheometer (baseline rheology). The results show a good agreement between the experimental yield stress and baseline rheology.</description>
	<pubDate>2026-05-15</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 120: Development of Methods for Real-Time In-Line Monitoring of Yield Stress for Non-Newtonian Fluid Using Pressure Drop and Liquid Rise Method During the Transfer of Radioactive Waste</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/120">doi: 10.3390/fluids11050120</a></p>
	<p>Authors:
		Anirban Saha
		Michael Poirier
		Dwayne McDaniel
		</p>
	<p>Real-Time In-Line Monitoring (RTIM) of rheological properties such as slurry yield stress is important in different industries for its various benefits such as significant time savings and increased safety/efficiency of processes while reducing secondary waste due to sampling or inaccurate procedures. This paper discusses two methods for characterizing yield stress in real time: the Pressure Loss method and the Liquid Rise method. The Liquid Rise method uses the height of the slurry in a vertical column and the pressure difference to quantify the yield stress. The Pressure Loss method uses the drop of pressure in a laminar flow of slurry to determine the yield stress. Kaolin&amp;amp;ndash;water slurry is used as a simulant of the non-Newtonian fluid. An experimental setup is built to demonstrate the methods, and data obtained from the experimental setup is compared with the yield stress obtained from a conventional table-top rheometer (baseline rheology). The results show a good agreement between the experimental yield stress and baseline rheology.</p>
	]]></content:encoded>

	<dc:title>Development of Methods for Real-Time In-Line Monitoring of Yield Stress for Non-Newtonian Fluid Using Pressure Drop and Liquid Rise Method During the Transfer of Radioactive Waste</dc:title>
			<dc:creator>Anirban Saha</dc:creator>
			<dc:creator>Michael Poirier</dc:creator>
			<dc:creator>Dwayne McDaniel</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050120</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-15</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-15</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>120</prism:startingPage>
		<prism:doi>10.3390/fluids11050120</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/120</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/119">

	<title>Fluids, Vol. 11, Pages 119: Transient CFD Study of Aerodynamic Interaction Between Heavy-Duty Trucks During Highway Merging and Platoon Formation Under Crosswind</title>
	<link>https://www.mdpi.com/2311-5521/11/5/119</link>
	<description>Highway merging and platoon formation are critical scenarios in heavy-duty vehicle aerodynamics. This study presents a transient computational fluid dynamics (CFD) analysis of two trucks undergoing a merging maneuver and subsequent platoon formation. A three-dimensional unsteady Reynolds-Averaged Navier&amp;amp;ndash;Stokes (uRANS) approach with the SST k&amp;amp;ndash;&amp;amp;omega; turbulence model is employed under zero-crosswind and yawed inflow conditions. The present work provides a time-resolved characterization of truck&amp;amp;ndash;truck aerodynamic interactions during dynamic spacing evolution, enabling the capture of unsteady wake effects that are not accessible in steady-state formulations commonly used in cooperative driving studies. Unlike previous steady analyses, the approach resolves transient wake development, vortex shedding, and their direct impact on instantaneous aerodynamic loads. Results identify three interaction regimes: weak interaction, strong wake interaction during wake impingement, and wake recovery at larger spacing. Under zero-crosswind conditions, significant drag reduction is observed, confirming platooning benefits. However, crosswind conditions substantially reduce this benefit and increase lateral loads due to asymmetric pressure distribution and wake deflection. A non-linear spacing&amp;amp;ndash;drag relationship is observed, governed by wake evolution and shear-layer interaction. These findings provide quantitative insight into transient aerodynamic interactions and highlight the importance of accounting for unsteady and crosswind effects in platoon performance assessment.</description>
	<pubDate>2026-05-15</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 119: Transient CFD Study of Aerodynamic Interaction Between Heavy-Duty Trucks During Highway Merging and Platoon Formation Under Crosswind</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/119">doi: 10.3390/fluids11050119</a></p>
	<p>Authors:
		Daniela Delia Alic
		Imre Zsolt Miklos
		Cristina Carmen Miklos
		</p>
	<p>Highway merging and platoon formation are critical scenarios in heavy-duty vehicle aerodynamics. This study presents a transient computational fluid dynamics (CFD) analysis of two trucks undergoing a merging maneuver and subsequent platoon formation. A three-dimensional unsteady Reynolds-Averaged Navier&amp;amp;ndash;Stokes (uRANS) approach with the SST k&amp;amp;ndash;&amp;amp;omega; turbulence model is employed under zero-crosswind and yawed inflow conditions. The present work provides a time-resolved characterization of truck&amp;amp;ndash;truck aerodynamic interactions during dynamic spacing evolution, enabling the capture of unsteady wake effects that are not accessible in steady-state formulations commonly used in cooperative driving studies. Unlike previous steady analyses, the approach resolves transient wake development, vortex shedding, and their direct impact on instantaneous aerodynamic loads. Results identify three interaction regimes: weak interaction, strong wake interaction during wake impingement, and wake recovery at larger spacing. Under zero-crosswind conditions, significant drag reduction is observed, confirming platooning benefits. However, crosswind conditions substantially reduce this benefit and increase lateral loads due to asymmetric pressure distribution and wake deflection. A non-linear spacing&amp;amp;ndash;drag relationship is observed, governed by wake evolution and shear-layer interaction. These findings provide quantitative insight into transient aerodynamic interactions and highlight the importance of accounting for unsteady and crosswind effects in platoon performance assessment.</p>
	]]></content:encoded>

	<dc:title>Transient CFD Study of Aerodynamic Interaction Between Heavy-Duty Trucks During Highway Merging and Platoon Formation Under Crosswind</dc:title>
			<dc:creator>Daniela Delia Alic</dc:creator>
			<dc:creator>Imre Zsolt Miklos</dc:creator>
			<dc:creator>Cristina Carmen Miklos</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050119</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-15</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-15</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>119</prism:startingPage>
		<prism:doi>10.3390/fluids11050119</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/119</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/118">

	<title>Fluids, Vol. 11, Pages 118: Haematocrit Distribution in Coronary Arteries: A ROM-PINN and Data-Driven Approach for Predicting Multiphase Flow</title>
	<link>https://www.mdpi.com/2311-5521/11/5/118</link>
	<description>Blood is a multiphase fluid, constituted of a plasma phase and a red blood cell (RBC) phase. Predicting the distribution of the RBC phase has applications in terms of medical device design, and for the characterisation of the risk of thrombus formation where atherosclerosis is present on coronary arteries. Computational fluid dynamics (CFD) can be used to simulate the multiphase flow of blood, but is time-consuming and requires a high level of technical expertise. This study evaluates the use of artificial neural networks (ANNs), as an alternative to CFD, to predict RBC distribution as part of blood flow through a coronary artery bifurcation model, both including and excluding stenosis. ANNs were trained on a dataset of 80 simulations generated using steady-state multiphase CFD. The initial data-driven ANNs encountered issues with overfitting and high errors in velocity component predictions. A physics-informed neural network (PINN) was employed, using a reduced order model (ROM), to enhance velocity component predictions, achieving average percentage error (APE) within 8.5% of CFD. These improved predictions were integrated into a hybrid model combining the PINN and the data-driven ANN to predict RBC distribution more effectively. The hybrid model achieved APEs ranging from 0.04% to 0.05%. Moreover, the hybrid model&amp;amp;rsquo;s predictions were 14 times faster than CFD transient runs, demonstrating potential for translation into clinical use. In conclusion, a combined ROM-PINN and data-driven approach enables fast high-accuracy predictions of flow for multiphase fluids such as blood when compared to CFD.</description>
	<pubDate>2026-05-14</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 118: Haematocrit Distribution in Coronary Arteries: A ROM-PINN and Data-Driven Approach for Predicting Multiphase Flow</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/118">doi: 10.3390/fluids11050118</a></p>
	<p>Authors:
		Bharath Sharma
		William Fox
		Jianhua Chen
		Daniel M. Espino
		Marco Castellani
		</p>
	<p>Blood is a multiphase fluid, constituted of a plasma phase and a red blood cell (RBC) phase. Predicting the distribution of the RBC phase has applications in terms of medical device design, and for the characterisation of the risk of thrombus formation where atherosclerosis is present on coronary arteries. Computational fluid dynamics (CFD) can be used to simulate the multiphase flow of blood, but is time-consuming and requires a high level of technical expertise. This study evaluates the use of artificial neural networks (ANNs), as an alternative to CFD, to predict RBC distribution as part of blood flow through a coronary artery bifurcation model, both including and excluding stenosis. ANNs were trained on a dataset of 80 simulations generated using steady-state multiphase CFD. The initial data-driven ANNs encountered issues with overfitting and high errors in velocity component predictions. A physics-informed neural network (PINN) was employed, using a reduced order model (ROM), to enhance velocity component predictions, achieving average percentage error (APE) within 8.5% of CFD. These improved predictions were integrated into a hybrid model combining the PINN and the data-driven ANN to predict RBC distribution more effectively. The hybrid model achieved APEs ranging from 0.04% to 0.05%. Moreover, the hybrid model&amp;amp;rsquo;s predictions were 14 times faster than CFD transient runs, demonstrating potential for translation into clinical use. In conclusion, a combined ROM-PINN and data-driven approach enables fast high-accuracy predictions of flow for multiphase fluids such as blood when compared to CFD.</p>
	]]></content:encoded>

	<dc:title>Haematocrit Distribution in Coronary Arteries: A ROM-PINN and Data-Driven Approach for Predicting Multiphase Flow</dc:title>
			<dc:creator>Bharath Sharma</dc:creator>
			<dc:creator>William Fox</dc:creator>
			<dc:creator>Jianhua Chen</dc:creator>
			<dc:creator>Daniel M. Espino</dc:creator>
			<dc:creator>Marco Castellani</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050118</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-14</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-14</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>118</prism:startingPage>
		<prism:doi>10.3390/fluids11050118</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/118</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/117">

	<title>Fluids, Vol. 11, Pages 117: A Calculation Method and Application Research in Gas-Lift Reverse Circulation Bottom-Hole Pressure Based on Gas&amp;ndash;Liquid Two-Phase Flow Theory</title>
	<link>https://www.mdpi.com/2311-5521/11/5/117</link>
	<description>Gas-lift reverse circulation drilling technology is one of the typical &amp;amp;ldquo;bottom-hole negative pressure&amp;amp;rdquo; drilling technologies. This technology can significantly reduce wellbore circulation pressure loss, alleviate the bottom-hole pressure holding effect, and effectively lower the probability of lost circulation. The core theory underlying this technology is multiphase flow in the wellbore. Based on gas&amp;amp;ndash;liquid two-phase flow theory, this paper develops a method for calculating bottom-hole pressure during gas-lift reverse circulation. The effects of key operational parameters on bottom-hole pressure were analyzed. The results show that bottom-hole pressure decreases as gas injection rate increases and as the gas injection point deepens. Moreover, the deeper the gas injection point, the greater the pressure reduction. Compared with the results from gas-lift reverse circulation drilling design and monitoring software applied to a shale gas well in southern Sichuan, the two sets of data differ by approximately 3%. The proposed calculation method can predict bottom-hole pressure under gas-lift reverse circulation conditions, overcoming the low accuracy of empirical formulas traditionally used in such operations. This has significant implications for advancing gas-lift reverse circulation technology in oil and gas well drilling.</description>
	<pubDate>2026-05-14</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 117: A Calculation Method and Application Research in Gas-Lift Reverse Circulation Bottom-Hole Pressure Based on Gas&amp;ndash;Liquid Two-Phase Flow Theory</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/117">doi: 10.3390/fluids11050117</a></p>
	<p>Authors:
		Pu Liu
		Chuanhua Ge
		Ruiqi Zhang
		Ruifeng Tan
		Shanquan Fan
		</p>
	<p>Gas-lift reverse circulation drilling technology is one of the typical &amp;amp;ldquo;bottom-hole negative pressure&amp;amp;rdquo; drilling technologies. This technology can significantly reduce wellbore circulation pressure loss, alleviate the bottom-hole pressure holding effect, and effectively lower the probability of lost circulation. The core theory underlying this technology is multiphase flow in the wellbore. Based on gas&amp;amp;ndash;liquid two-phase flow theory, this paper develops a method for calculating bottom-hole pressure during gas-lift reverse circulation. The effects of key operational parameters on bottom-hole pressure were analyzed. The results show that bottom-hole pressure decreases as gas injection rate increases and as the gas injection point deepens. Moreover, the deeper the gas injection point, the greater the pressure reduction. Compared with the results from gas-lift reverse circulation drilling design and monitoring software applied to a shale gas well in southern Sichuan, the two sets of data differ by approximately 3%. The proposed calculation method can predict bottom-hole pressure under gas-lift reverse circulation conditions, overcoming the low accuracy of empirical formulas traditionally used in such operations. This has significant implications for advancing gas-lift reverse circulation technology in oil and gas well drilling.</p>
	]]></content:encoded>

	<dc:title>A Calculation Method and Application Research in Gas-Lift Reverse Circulation Bottom-Hole Pressure Based on Gas&amp;amp;ndash;Liquid Two-Phase Flow Theory</dc:title>
			<dc:creator>Pu Liu</dc:creator>
			<dc:creator>Chuanhua Ge</dc:creator>
			<dc:creator>Ruiqi Zhang</dc:creator>
			<dc:creator>Ruifeng Tan</dc:creator>
			<dc:creator>Shanquan Fan</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050117</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-14</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-14</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>117</prism:startingPage>
		<prism:doi>10.3390/fluids11050117</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/117</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/116">

	<title>Fluids, Vol. 11, Pages 116: An Overview of Highly Viscous Fluid Flows in Straight and Elbow Pipes: II Gas&amp;ndash;Liquid Flows</title>
	<link>https://www.mdpi.com/2311-5521/11/5/116</link>
	<description>This review summarizes the latest research concerning the horizontal flow of two-phase mixtures with viscosities ranging from 0.2 Pa&amp;amp;middot;s to 6.4 &amp;amp;times; 104 Pa&amp;amp;middot;s. Although our survey is concerned with Newtonian fluids, a short section is included to briefly discuss certain rheological aspects that should be generally considered. In contrast with previous work reporting on the progress in specific domains (e.g., in the oil and gas, chemical, or geophysical contexts), we seek to provide a comprehensive overview of the methods and results used in different contexts. Accordingly, the scope is widened to encompass a broader range of industrial applications and naturally occurring flows. The interest in high-viscosity flows is motivated by the operational challenges occurring in certain systems, most notably in the oil and gas industry, where the production of heavy and extra-heavy crude oils reduces the margins for a safe and efficient operation. Furthermore, this review underlines the cross-field analogies appearing in a broad range of scales and applications. It emphasizes the fundamental role of viscosity in determining the flow patterns, as experimental evidence suggests that the transition boundaries are largely altered at higher viscosities. Some gaps that could be addressed in future work are briefly discussed.</description>
	<pubDate>2026-05-12</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 116: An Overview of Highly Viscous Fluid Flows in Straight and Elbow Pipes: II Gas&amp;ndash;Liquid Flows</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/116">doi: 10.3390/fluids11050116</a></p>
	<p>Authors:
		Enrique Guzmán
		Leonardo Di G. Sigalotti
		Lizeth Torres
		Jaime Klapp
		</p>
	<p>This review summarizes the latest research concerning the horizontal flow of two-phase mixtures with viscosities ranging from 0.2 Pa&amp;amp;middot;s to 6.4 &amp;amp;times; 104 Pa&amp;amp;middot;s. Although our survey is concerned with Newtonian fluids, a short section is included to briefly discuss certain rheological aspects that should be generally considered. In contrast with previous work reporting on the progress in specific domains (e.g., in the oil and gas, chemical, or geophysical contexts), we seek to provide a comprehensive overview of the methods and results used in different contexts. Accordingly, the scope is widened to encompass a broader range of industrial applications and naturally occurring flows. The interest in high-viscosity flows is motivated by the operational challenges occurring in certain systems, most notably in the oil and gas industry, where the production of heavy and extra-heavy crude oils reduces the margins for a safe and efficient operation. Furthermore, this review underlines the cross-field analogies appearing in a broad range of scales and applications. It emphasizes the fundamental role of viscosity in determining the flow patterns, as experimental evidence suggests that the transition boundaries are largely altered at higher viscosities. Some gaps that could be addressed in future work are briefly discussed.</p>
	]]></content:encoded>

	<dc:title>An Overview of Highly Viscous Fluid Flows in Straight and Elbow Pipes: II Gas&amp;amp;ndash;Liquid Flows</dc:title>
			<dc:creator>Enrique Guzmán</dc:creator>
			<dc:creator>Leonardo Di G. Sigalotti</dc:creator>
			<dc:creator>Lizeth Torres</dc:creator>
			<dc:creator>Jaime Klapp</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050116</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-12</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-12</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Review</prism:section>
	<prism:startingPage>116</prism:startingPage>
		<prism:doi>10.3390/fluids11050116</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/116</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/115">

	<title>Fluids, Vol. 11, Pages 115: Boundary Conditions and Algorithms for 2D and 3D Lattice Boltzmann Simulations of Heterogeneous Reactions</title>
	<link>https://www.mdpi.com/2311-5521/11/5/115</link>
	<description>In this paper, the formulation and method of implementation of boundary conditions for heterogeneous reactions in porous media are elaborated. These are implemented into a previously validated lattice Boltzmann model for the simulation of heterogeneous reactions in porous media, extending it on multiple fronts. The formulation of the boundary conditions is validated thoroughly. The conversion of solid carbon to CO and CO2 is chosen as a specific case of application. An extensive parametric study is conducted with a specific geometry consisting of spherical substrate particles, coated with a reactive soot layer, to highlight the capability of the code. The code was able to capture the expected evolution of a combustion front and the influence of process parameters onto its propagation velocity. The propagation speed linearly increased with an increase in the reactant mass fraction and exponentially increased with P&amp;amp;eacute;clet number. Also, the CO/CO2 ratio obtained from experimental data could be reproduced with good accuracy. Furthermore, an algorithm for the correct evaluation of the specific surface is presented, which is necessary for evolving solid domains based on realistic geometries containing enclosed cavities. The method of implementation, computational overhead and acceleration technique are discussed. Finally, the model and all boundary conditions are extended to 3D and validated.</description>
	<pubDate>2026-05-06</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 115: Boundary Conditions and Algorithms for 2D and 3D Lattice Boltzmann Simulations of Heterogeneous Reactions</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/115">doi: 10.3390/fluids11050115</a></p>
	<p>Authors:
		Claudius Stockinger
		Antonio Raiolo
		Ulrich Nieken
		Abdellah Hadjadj
		Mostafa Safdari Shadloo
		</p>
	<p>In this paper, the formulation and method of implementation of boundary conditions for heterogeneous reactions in porous media are elaborated. These are implemented into a previously validated lattice Boltzmann model for the simulation of heterogeneous reactions in porous media, extending it on multiple fronts. The formulation of the boundary conditions is validated thoroughly. The conversion of solid carbon to CO and CO2 is chosen as a specific case of application. An extensive parametric study is conducted with a specific geometry consisting of spherical substrate particles, coated with a reactive soot layer, to highlight the capability of the code. The code was able to capture the expected evolution of a combustion front and the influence of process parameters onto its propagation velocity. The propagation speed linearly increased with an increase in the reactant mass fraction and exponentially increased with P&amp;amp;eacute;clet number. Also, the CO/CO2 ratio obtained from experimental data could be reproduced with good accuracy. Furthermore, an algorithm for the correct evaluation of the specific surface is presented, which is necessary for evolving solid domains based on realistic geometries containing enclosed cavities. The method of implementation, computational overhead and acceleration technique are discussed. Finally, the model and all boundary conditions are extended to 3D and validated.</p>
	]]></content:encoded>

	<dc:title>Boundary Conditions and Algorithms for 2D and 3D Lattice Boltzmann Simulations of Heterogeneous Reactions</dc:title>
			<dc:creator>Claudius Stockinger</dc:creator>
			<dc:creator>Antonio Raiolo</dc:creator>
			<dc:creator>Ulrich Nieken</dc:creator>
			<dc:creator>Abdellah Hadjadj</dc:creator>
			<dc:creator>Mostafa Safdari Shadloo</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050115</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-06</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-06</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>115</prism:startingPage>
		<prism:doi>10.3390/fluids11050115</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/115</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/114">

	<title>Fluids, Vol. 11, Pages 114: Editorial for Mass Transfer in Multiphase Reactors</title>
	<link>https://www.mdpi.com/2311-5521/11/5/114</link>
	<description>Gas&amp;amp;ndash;liquid reactors (especially bubble columns (BCs)) are the most widely used in both the chemical and biochemical industries [...]</description>
	<pubDate>2026-05-03</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 114: Editorial for Mass Transfer in Multiphase Reactors</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/114">doi: 10.3390/fluids11050114</a></p>
	<p>Authors:
		Stoyan Nedeltchev
		</p>
	<p>Gas&amp;amp;ndash;liquid reactors (especially bubble columns (BCs)) are the most widely used in both the chemical and biochemical industries [...]</p>
	]]></content:encoded>

	<dc:title>Editorial for Mass Transfer in Multiphase Reactors</dc:title>
			<dc:creator>Stoyan Nedeltchev</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050114</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-05-03</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-05-03</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Editorial</prism:section>
	<prism:startingPage>114</prism:startingPage>
		<prism:doi>10.3390/fluids11050114</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/114</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/113">

	<title>Fluids, Vol. 11, Pages 113: Air Knives: Going Beyond the Classical Midspan Pressure Distributions</title>
	<link>https://www.mdpi.com/2311-5521/11/5/113</link>
	<description>Air knives are extensively employed in many cold rolling or tin plate production lines for drying purposes. Generally, these systems are oversized, resulting in excessive energy consumption, a consequence of insufficient understanding of their performance. Considering this deficiency, an empirical exploration was initiated to analyze the functionality of an air knife oriented perpendicularly to a given surface. Given the scarcity of information within the current body of literature, particular emphasis was placed on the regions affected by the finite dimensions of the device. Impingement pressure distributions were measured at the midspan plane and planes parallel to the midspan but extending beyond the projection of the air knife. The midspan impingement pressure profile aligned with the established bell-shaped distribution, whereas the outcomes beyond the air knife&amp;amp;rsquo;s projection conformed to an analytically fitted similarity principle. Consequently, the mathematical formulations introduced in this study facilitate the mapping of the impingement pressure within the whole impingement plane, encompassing areas influenced by the finite length of the air knife, thereby representing the innovative contribution of this research.</description>
	<pubDate>2026-04-30</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 113: Air Knives: Going Beyond the Classical Midspan Pressure Distributions</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/113">doi: 10.3390/fluids11050113</a></p>
	<p>Authors:
		Celia Miguel-González
		Aitor Vega-Valladares
		Manuel García-Díaz
		Alejandro Rodrígurez de Castro
		José González Pérez
		Bruno Pereiras
		</p>
	<p>Air knives are extensively employed in many cold rolling or tin plate production lines for drying purposes. Generally, these systems are oversized, resulting in excessive energy consumption, a consequence of insufficient understanding of their performance. Considering this deficiency, an empirical exploration was initiated to analyze the functionality of an air knife oriented perpendicularly to a given surface. Given the scarcity of information within the current body of literature, particular emphasis was placed on the regions affected by the finite dimensions of the device. Impingement pressure distributions were measured at the midspan plane and planes parallel to the midspan but extending beyond the projection of the air knife. The midspan impingement pressure profile aligned with the established bell-shaped distribution, whereas the outcomes beyond the air knife&amp;amp;rsquo;s projection conformed to an analytically fitted similarity principle. Consequently, the mathematical formulations introduced in this study facilitate the mapping of the impingement pressure within the whole impingement plane, encompassing areas influenced by the finite length of the air knife, thereby representing the innovative contribution of this research.</p>
	]]></content:encoded>

	<dc:title>Air Knives: Going Beyond the Classical Midspan Pressure Distributions</dc:title>
			<dc:creator>Celia Miguel-González</dc:creator>
			<dc:creator>Aitor Vega-Valladares</dc:creator>
			<dc:creator>Manuel García-Díaz</dc:creator>
			<dc:creator>Alejandro Rodrígurez de Castro</dc:creator>
			<dc:creator>José González Pérez</dc:creator>
			<dc:creator>Bruno Pereiras</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050113</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-30</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-30</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>113</prism:startingPage>
		<prism:doi>10.3390/fluids11050113</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/113</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/112">

	<title>Fluids, Vol. 11, Pages 112: Comparative Study of the Performance Characteristics of Annular Jet Pumps Conveying Newtonian and Shear-Thinning Non-Newtonian Fluids</title>
	<link>https://www.mdpi.com/2311-5521/11/5/112</link>
	<description>This study investigates the factors influencing the performance characteristics of annular jet pumps (AJPs) conveying non-Newtonian fluids, to enhance their suction capability for marine organisms such as jellyfish, which exhibit properties close to non-Newtonian fluids. Based on the power-law fluid model, realizable k-&amp;amp;epsilon; model, and volume of fluid (VOF) model, shear-thinning carboxymethyl cellulose (CMC) was selected to simulate marine organisms like jellyfish. Fluent software was employed to numerically simulate the performance characteristics and internal flow field of the annular jet pumps. The results demonstrate that the shear-thinning effect of non-Newtonian fluids reduces the maximum efficiency point of annular jet pumps and decreases the flow rate ratio corresponding to this efficiency point. As the concentration of CMC solution increased to 0.5%, the maximum efficiency point decreased by 5.5%, and the flow rate ratio corresponding to this efficiency point dropped from 1 to 0.8. These findings provide reference and insights for analyzing the full flow field of annular jet pumps pumping shear-thinning non-Newtonian fluids and for structural design of such pumps.</description>
	<pubDate>2026-04-30</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 112: Comparative Study of the Performance Characteristics of Annular Jet Pumps Conveying Newtonian and Shear-Thinning Non-Newtonian Fluids</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/112">doi: 10.3390/fluids11050112</a></p>
	<p>Authors:
		Tianle Li
		Peng Wang
		Wang Zheng
		Donghua Lu
		Xin Xia
		Hanghui Zhou
		Qiaorui Si
		</p>
	<p>This study investigates the factors influencing the performance characteristics of annular jet pumps (AJPs) conveying non-Newtonian fluids, to enhance their suction capability for marine organisms such as jellyfish, which exhibit properties close to non-Newtonian fluids. Based on the power-law fluid model, realizable k-&amp;amp;epsilon; model, and volume of fluid (VOF) model, shear-thinning carboxymethyl cellulose (CMC) was selected to simulate marine organisms like jellyfish. Fluent software was employed to numerically simulate the performance characteristics and internal flow field of the annular jet pumps. The results demonstrate that the shear-thinning effect of non-Newtonian fluids reduces the maximum efficiency point of annular jet pumps and decreases the flow rate ratio corresponding to this efficiency point. As the concentration of CMC solution increased to 0.5%, the maximum efficiency point decreased by 5.5%, and the flow rate ratio corresponding to this efficiency point dropped from 1 to 0.8. These findings provide reference and insights for analyzing the full flow field of annular jet pumps pumping shear-thinning non-Newtonian fluids and for structural design of such pumps.</p>
	]]></content:encoded>

	<dc:title>Comparative Study of the Performance Characteristics of Annular Jet Pumps Conveying Newtonian and Shear-Thinning Non-Newtonian Fluids</dc:title>
			<dc:creator>Tianle Li</dc:creator>
			<dc:creator>Peng Wang</dc:creator>
			<dc:creator>Wang Zheng</dc:creator>
			<dc:creator>Donghua Lu</dc:creator>
			<dc:creator>Xin Xia</dc:creator>
			<dc:creator>Hanghui Zhou</dc:creator>
			<dc:creator>Qiaorui Si</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050112</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-30</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-30</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>112</prism:startingPage>
		<prism:doi>10.3390/fluids11050112</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/112</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/111">

	<title>Fluids, Vol. 11, Pages 111: Developing Bingham Fluid Flow in the Entrance Region Between Parallel Plates</title>
	<link>https://www.mdpi.com/2311-5521/11/5/111</link>
	<description>Bingham fluids, also called Bingham plastics, are used in different industries including the production of food, pharmaceuticals, household products, construction and oil and gas drilling. The behavior of Bingham fluids is viscous above a critical shear stress and rigid-body below the threshold stress value. Knowledge of the size of the entrance region has several applications including hemodynamics and microfluidics. A model for steady Bingham fluid flow in the entrance region between parallel plates is developed using the inlet-filled region concept. A boundary layer model is used to solve the fluid flow dynamics in the inlet region up to the point where the critical shear stress is reached at the edge of the boundary layer. Beyond that point, the boundary layer does not grow, while the velocity profile keeps readjusting in the filled region to asymptotically reach the fully developed flow. The results include boundary layer thickness profiles, dimensionless pressure drop, centerline velocity, friction factor and inlet and entrance region sizes as functions of the Bingham number. The results are validated against the results for the Newtonian fluid case (Bingham fluid yield stress equal to zero) and CFD results, using the finite element method, for nonzero Bingham numbers. In addition, the results are found to asymptotically reach the fully developed flow values for the general Bingham fluid flow case. The effects of the Bingham number are addressed and compared with the literature. The present model is largely analytical, requiring minor numerical tasks.</description>
	<pubDate>2026-04-29</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 111: Developing Bingham Fluid Flow in the Entrance Region Between Parallel Plates</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/111">doi: 10.3390/fluids11050111</a></p>
	<p>Authors:
		Rachid Chebbi
		</p>
	<p>Bingham fluids, also called Bingham plastics, are used in different industries including the production of food, pharmaceuticals, household products, construction and oil and gas drilling. The behavior of Bingham fluids is viscous above a critical shear stress and rigid-body below the threshold stress value. Knowledge of the size of the entrance region has several applications including hemodynamics and microfluidics. A model for steady Bingham fluid flow in the entrance region between parallel plates is developed using the inlet-filled region concept. A boundary layer model is used to solve the fluid flow dynamics in the inlet region up to the point where the critical shear stress is reached at the edge of the boundary layer. Beyond that point, the boundary layer does not grow, while the velocity profile keeps readjusting in the filled region to asymptotically reach the fully developed flow. The results include boundary layer thickness profiles, dimensionless pressure drop, centerline velocity, friction factor and inlet and entrance region sizes as functions of the Bingham number. The results are validated against the results for the Newtonian fluid case (Bingham fluid yield stress equal to zero) and CFD results, using the finite element method, for nonzero Bingham numbers. In addition, the results are found to asymptotically reach the fully developed flow values for the general Bingham fluid flow case. The effects of the Bingham number are addressed and compared with the literature. The present model is largely analytical, requiring minor numerical tasks.</p>
	]]></content:encoded>

	<dc:title>Developing Bingham Fluid Flow in the Entrance Region Between Parallel Plates</dc:title>
			<dc:creator>Rachid Chebbi</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050111</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-29</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-29</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>111</prism:startingPage>
		<prism:doi>10.3390/fluids11050111</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/111</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/110">

	<title>Fluids, Vol. 11, Pages 110: Frequency Variations of Two-Mode Interference Patterns Due to Internal Soliton Waves in Shallow Water</title>
	<link>https://www.mdpi.com/2311-5521/11/5/110</link>
	<description>This paper presents a theoretical analysis of frequency shifts in broadband acoustic field interference structures caused by an internal soliton wave in shallow water. It analyzes the spectral signature of interference-maxima frequency shifts within a coupled-mode framework that describes the scattering of acoustic normal modes under soliton-induced perturbations. Using the weak coupling approximation, analytical expressions are obtained for modal phase variations and the spectral peak frequency associated with the temporal evolution of frequency shifts induced by internal soliton waves. The analytical estimates obtained in the weak coupling approximation are extensively validated using numerical simulations under realistic ocean conditions without invoking it. This paper&amp;amp;rsquo;s theoretical analysis demonstrates that internal soliton wave-induced mode coupling produces frequency shift spectrum signatures that strongly depend on soliton parameters. These results suggest that it is potentially feasible to estimate key soliton parameters, such as propagation direction, velocity, and effective amplitude, from measured frequency shifts. Numerical simulations demonstrate the feasibility of solving this inverse problem. These findings highlight the potential of frequency shift analysis as a practical, robust tool for remote sensing of internal wave dynamics in ocean acoustics.</description>
	<pubDate>2026-04-29</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 110: Frequency Variations of Two-Mode Interference Patterns Due to Internal Soliton Waves in Shallow Water</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/110">doi: 10.3390/fluids11050110</a></p>
	<p>Authors:
		Matthias Ehrhardt
		Sergey Pereselkov
		Venedikt Kuz’kin
		Sergey Tkachenko
		Alexey Pereselkov
		</p>
	<p>This paper presents a theoretical analysis of frequency shifts in broadband acoustic field interference structures caused by an internal soliton wave in shallow water. It analyzes the spectral signature of interference-maxima frequency shifts within a coupled-mode framework that describes the scattering of acoustic normal modes under soliton-induced perturbations. Using the weak coupling approximation, analytical expressions are obtained for modal phase variations and the spectral peak frequency associated with the temporal evolution of frequency shifts induced by internal soliton waves. The analytical estimates obtained in the weak coupling approximation are extensively validated using numerical simulations under realistic ocean conditions without invoking it. This paper&amp;amp;rsquo;s theoretical analysis demonstrates that internal soliton wave-induced mode coupling produces frequency shift spectrum signatures that strongly depend on soliton parameters. These results suggest that it is potentially feasible to estimate key soliton parameters, such as propagation direction, velocity, and effective amplitude, from measured frequency shifts. Numerical simulations demonstrate the feasibility of solving this inverse problem. These findings highlight the potential of frequency shift analysis as a practical, robust tool for remote sensing of internal wave dynamics in ocean acoustics.</p>
	]]></content:encoded>

	<dc:title>Frequency Variations of Two-Mode Interference Patterns Due to Internal Soliton Waves in Shallow Water</dc:title>
			<dc:creator>Matthias Ehrhardt</dc:creator>
			<dc:creator>Sergey Pereselkov</dc:creator>
			<dc:creator>Venedikt Kuz’kin</dc:creator>
			<dc:creator>Sergey Tkachenko</dc:creator>
			<dc:creator>Alexey Pereselkov</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050110</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-29</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-29</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>110</prism:startingPage>
		<prism:doi>10.3390/fluids11050110</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/110</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/109">

	<title>Fluids, Vol. 11, Pages 109: Statistical Analysis of Velocity Skewness and Kurtosis Under Adverse Pressure Gradients in Turbulent Boundary Layers</title>
	<link>https://www.mdpi.com/2311-5521/11/5/109</link>
	<description>Skewness (S) and kurtosis (K) are statistical measures that provide insights into the characteristics of turbulence. This paper investigates the effects of adverse pressure gradients (APG) on S and K for mean and fluctuating velocities in the turbulent boundary layer (TBL), using the probability distribution function (PDF) and cumulative distribution function (CDF). The velocity distributions in the TBL are obtained experimentally. The experiments are conducted at Re ~ 1.12 &amp;amp;times; 105. According to the Clauser criterion, the APG parameter is &amp;amp;beta; = 0.62. Two test sections are examined: a straight duct (zero pressure gradient) and a straight diffuser with a divergence angle of 6&amp;amp;deg; and a cross-sectional area ratio of 1:4. Measurements are performed at five streamwise stations (x/c = 1, 1.5, 2, 3, and 4, where c = 100 mm). The results show that the APG does not influence the maximum or minimum values of the PDFs for mean and fluctuating velocities. Compared to the third and fourth moments, variations in the first and second moments are minimal. It is found that S values for the straight duct are lower than those for the straight diffuser. The largest difference is observed in the fourth moment of the PDF, i.e., K. Additionally, four PDF curve-fitting equations are presented for the mean velocity and velocity fluctuations in the TBL for both the straight duct and the straight diffuser. Differential entropy analysis indicates that the decrease in entropy resulting from wall shear and the turbulent boundary layer in the straight channel is more pronounced than the reduction in mean velocity entropy caused by the APG in the diffuser channel.</description>
	<pubDate>2026-04-29</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 109: Statistical Analysis of Velocity Skewness and Kurtosis Under Adverse Pressure Gradients in Turbulent Boundary Layers</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/109">doi: 10.3390/fluids11050109</a></p>
	<p>Authors:
		Omid Farghadani
		Abdolamir Bak Khoshnevis
		Morteza Bayareh
		</p>
	<p>Skewness (S) and kurtosis (K) are statistical measures that provide insights into the characteristics of turbulence. This paper investigates the effects of adverse pressure gradients (APG) on S and K for mean and fluctuating velocities in the turbulent boundary layer (TBL), using the probability distribution function (PDF) and cumulative distribution function (CDF). The velocity distributions in the TBL are obtained experimentally. The experiments are conducted at Re ~ 1.12 &amp;amp;times; 105. According to the Clauser criterion, the APG parameter is &amp;amp;beta; = 0.62. Two test sections are examined: a straight duct (zero pressure gradient) and a straight diffuser with a divergence angle of 6&amp;amp;deg; and a cross-sectional area ratio of 1:4. Measurements are performed at five streamwise stations (x/c = 1, 1.5, 2, 3, and 4, where c = 100 mm). The results show that the APG does not influence the maximum or minimum values of the PDFs for mean and fluctuating velocities. Compared to the third and fourth moments, variations in the first and second moments are minimal. It is found that S values for the straight duct are lower than those for the straight diffuser. The largest difference is observed in the fourth moment of the PDF, i.e., K. Additionally, four PDF curve-fitting equations are presented for the mean velocity and velocity fluctuations in the TBL for both the straight duct and the straight diffuser. Differential entropy analysis indicates that the decrease in entropy resulting from wall shear and the turbulent boundary layer in the straight channel is more pronounced than the reduction in mean velocity entropy caused by the APG in the diffuser channel.</p>
	]]></content:encoded>

	<dc:title>Statistical Analysis of Velocity Skewness and Kurtosis Under Adverse Pressure Gradients in Turbulent Boundary Layers</dc:title>
			<dc:creator>Omid Farghadani</dc:creator>
			<dc:creator>Abdolamir Bak Khoshnevis</dc:creator>
			<dc:creator>Morteza Bayareh</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050109</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-29</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-29</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>109</prism:startingPage>
		<prism:doi>10.3390/fluids11050109</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/109</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/108">

	<title>Fluids, Vol. 11, Pages 108: Cation-Dependent Role of Water on the Dynamics and Ionic Conductivity of Levulinate-Based Ionic Liquids</title>
	<link>https://www.mdpi.com/2311-5521/11/5/108</link>
	<description>The effect of water on the dynamics and ionic conductivity of the ionic liquids 1-ethyl-1-methylpyrrolidinium levulinate ([C2C1Pyr]Lev) and 1-butyl-1-methylpyrrolidinium levulinate ([C4C1Pyr]Lev) was investigated using differential scanning calorimetry (DSC) and broadband dielectric spectroscopy (BDS) over a wide temperature range. Although both ILs share the same levulinate anion, water induces markedly different dynamical responses depending on cation structure. In both systems, water acts as a plasticizer, lowering the glass transition temperature; however, the extent of plasticization and the resulting relaxation dynamics are cation-dependent. Stronger water&amp;amp;ndash;cation interactions are observed in [C2C1Pyr]Lev, whereas in [C4C1Pyr]Lev, water primarily disrupts alkyl-chain packing, enhancing ionic mobility. Increasing hydration shifts the main relaxation to higher frequencies and increases liquid fragility, while translational ionic motion remains decoupled from structural relaxation. These results demonstrate that water plays a cation-specific and mechanistically distinct role in levulinate-based ILs, providing new insights into hydration-controlled glassy dynamics and charge transport relevant to the design of IL-based electrolytes under non-anhydrous conditions.</description>
	<pubDate>2026-04-27</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 108: Cation-Dependent Role of Water on the Dynamics and Ionic Conductivity of Levulinate-Based Ionic Liquids</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/108">doi: 10.3390/fluids11050108</a></p>
	<p>Authors:
		Georgios Tsonos
		Sotiria Kripotou
		Georgios Mavroeidis
		Christos Tsonos
		Lorenzo Guazzelli
		Luca Guglielmero
		Ilias Stavrakas
		Konstantinos Moutzouris
		</p>
	<p>The effect of water on the dynamics and ionic conductivity of the ionic liquids 1-ethyl-1-methylpyrrolidinium levulinate ([C2C1Pyr]Lev) and 1-butyl-1-methylpyrrolidinium levulinate ([C4C1Pyr]Lev) was investigated using differential scanning calorimetry (DSC) and broadband dielectric spectroscopy (BDS) over a wide temperature range. Although both ILs share the same levulinate anion, water induces markedly different dynamical responses depending on cation structure. In both systems, water acts as a plasticizer, lowering the glass transition temperature; however, the extent of plasticization and the resulting relaxation dynamics are cation-dependent. Stronger water&amp;amp;ndash;cation interactions are observed in [C2C1Pyr]Lev, whereas in [C4C1Pyr]Lev, water primarily disrupts alkyl-chain packing, enhancing ionic mobility. Increasing hydration shifts the main relaxation to higher frequencies and increases liquid fragility, while translational ionic motion remains decoupled from structural relaxation. These results demonstrate that water plays a cation-specific and mechanistically distinct role in levulinate-based ILs, providing new insights into hydration-controlled glassy dynamics and charge transport relevant to the design of IL-based electrolytes under non-anhydrous conditions.</p>
	]]></content:encoded>

	<dc:title>Cation-Dependent Role of Water on the Dynamics and Ionic Conductivity of Levulinate-Based Ionic Liquids</dc:title>
			<dc:creator>Georgios Tsonos</dc:creator>
			<dc:creator>Sotiria Kripotou</dc:creator>
			<dc:creator>Georgios Mavroeidis</dc:creator>
			<dc:creator>Christos Tsonos</dc:creator>
			<dc:creator>Lorenzo Guazzelli</dc:creator>
			<dc:creator>Luca Guglielmero</dc:creator>
			<dc:creator>Ilias Stavrakas</dc:creator>
			<dc:creator>Konstantinos Moutzouris</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050108</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-27</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-27</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>108</prism:startingPage>
		<prism:doi>10.3390/fluids11050108</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/108</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/107">

	<title>Fluids, Vol. 11, Pages 107: The Development of a Data-Driven Surrogate Model for Enhancing Electric Vehicle Cabin Airflow Analysis</title>
	<link>https://www.mdpi.com/2311-5521/11/5/107</link>
	<description>This paper presents a data-driven surrogate model for predicting cabin airflow and its integration into system-level electric vehicle simulations for energy management analysis. The model employs a graph-based neural network with a mirror-symmetric predictor&amp;amp;ndash;corrector architecture and is trained on a dataset generated using computational fluid dynamics (CFD) covering a defined range of inlet velocities and temperatures. The surrogate appropriately reconstructs temperature fields and captures the dominant airflow structures at significantly lower computational cost than CFD. Quantitative evaluation shows high accuracy in passenger-relevant regions, while localized discrepancies remain confined mainly to shear-layer zones. The model enables near-real-time inference and is coupled with a system-level modeling framework for control-oriented simulations that are impractical with CFD. The study is tailored to a specific geometry and operating range, showing that targeted training strategies and physics-based extensions improve robustness, particularly under limited data conditions.</description>
	<pubDate>2026-04-25</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 107: The Development of a Data-Driven Surrogate Model for Enhancing Electric Vehicle Cabin Airflow Analysis</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/107">doi: 10.3390/fluids11050107</a></p>
	<p>Authors:
		Mirza Popovac
		Thomas Bäuml
		Dominik Dvorak
		Dragan Šimić
		</p>
	<p>This paper presents a data-driven surrogate model for predicting cabin airflow and its integration into system-level electric vehicle simulations for energy management analysis. The model employs a graph-based neural network with a mirror-symmetric predictor&amp;amp;ndash;corrector architecture and is trained on a dataset generated using computational fluid dynamics (CFD) covering a defined range of inlet velocities and temperatures. The surrogate appropriately reconstructs temperature fields and captures the dominant airflow structures at significantly lower computational cost than CFD. Quantitative evaluation shows high accuracy in passenger-relevant regions, while localized discrepancies remain confined mainly to shear-layer zones. The model enables near-real-time inference and is coupled with a system-level modeling framework for control-oriented simulations that are impractical with CFD. The study is tailored to a specific geometry and operating range, showing that targeted training strategies and physics-based extensions improve robustness, particularly under limited data conditions.</p>
	]]></content:encoded>

	<dc:title>The Development of a Data-Driven Surrogate Model for Enhancing Electric Vehicle Cabin Airflow Analysis</dc:title>
			<dc:creator>Mirza Popovac</dc:creator>
			<dc:creator>Thomas Bäuml</dc:creator>
			<dc:creator>Dominik Dvorak</dc:creator>
			<dc:creator>Dragan Šimić</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050107</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-25</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-25</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>107</prism:startingPage>
		<prism:doi>10.3390/fluids11050107</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/107</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/106">

	<title>Fluids, Vol. 11, Pages 106: Active Flow Control Techniques: Classification, Analysis, and Future Trends for Automotive Applications</title>
	<link>https://www.mdpi.com/2311-5521/11/5/106</link>
	<description>Active flow control represents a key enabling technology for advancing aerodynamic performance, offering significant potential improvements in drag reduction, lift enhancement, and overall efficiency. This paper reviews state-of-the-art active flow control techniques originally developed for aerospace applications and evaluates their applicability to automotive systems, considering constraints such as packaging, efficiency, cost, and integration. A structured classification of fluidic, surface-based (including morphing), and plasma-based approaches is presented, followed by a comparative and decision-oriented assessment of their performance, technological maturity, and feasibility. The results indicate that synthetic jet actuators and morphing-based solutions provide the most balanced compromise between aerodynamic effectiveness and practical implementation. In contrast, conventional fluidic methods are limited by low system efficiency, while plasma-based techniques, although highly responsive, face challenges related to scalability and integration.</description>
	<pubDate>2026-04-23</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 106: Active Flow Control Techniques: Classification, Analysis, and Future Trends for Automotive Applications</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/106">doi: 10.3390/fluids11050106</a></p>
	<p>Authors:
		Marco Robert Herberg
		Stefano De Pinto
		Marco Donato de Tullio
		Giuseppe Pascazio
		</p>
	<p>Active flow control represents a key enabling technology for advancing aerodynamic performance, offering significant potential improvements in drag reduction, lift enhancement, and overall efficiency. This paper reviews state-of-the-art active flow control techniques originally developed for aerospace applications and evaluates their applicability to automotive systems, considering constraints such as packaging, efficiency, cost, and integration. A structured classification of fluidic, surface-based (including morphing), and plasma-based approaches is presented, followed by a comparative and decision-oriented assessment of their performance, technological maturity, and feasibility. The results indicate that synthetic jet actuators and morphing-based solutions provide the most balanced compromise between aerodynamic effectiveness and practical implementation. In contrast, conventional fluidic methods are limited by low system efficiency, while plasma-based techniques, although highly responsive, face challenges related to scalability and integration.</p>
	]]></content:encoded>

	<dc:title>Active Flow Control Techniques: Classification, Analysis, and Future Trends for Automotive Applications</dc:title>
			<dc:creator>Marco Robert Herberg</dc:creator>
			<dc:creator>Stefano De Pinto</dc:creator>
			<dc:creator>Marco Donato de Tullio</dc:creator>
			<dc:creator>Giuseppe Pascazio</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050106</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-23</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-23</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Review</prism:section>
	<prism:startingPage>106</prism:startingPage>
		<prism:doi>10.3390/fluids11050106</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/106</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/5/105">

	<title>Fluids, Vol. 11, Pages 105: A Neural Network Approach for the Simulation of Real Fluid Two-Phase Combustion Using a Multi-Species (H2/O2) Mechanism</title>
	<link>https://www.mdpi.com/2311-5521/11/5/105</link>
	<description>Fully compressible two-phase flow configurations present many challenges for numerical modelling, requiring the development of Real Fluid Models (RFMs) able to simulate flows in subcritical, transcritical and supercritical regimes. Such an RFM has been recently developed at IFPEN based on physical properties lookup tables, mainly for binary and ternary chemical systems. This paper proposes an Artificial Neural Network (ANN) approach to overcome the limitations of lookup tables of thermodynamic properties and to apply RFM to multi-species combustion. A methodology for generating an optimized data set by combining a vapor&amp;amp;ndash;liquid equilibrium (VLE) thermodynamic solver and the in situ adaptive tabulation (ISAT) method is developed. It aims to improve the neural network training process for two-phase combustion simulations where many species are present. This ANN methodology has been implemented in the CONVERGE CFD solver and validated using a mixing layer (LOX/GH2) benchmark from the literature relevant to rocket conditions, and an academic gaseous (H2/O2) case relevant to hydrogen combustion. The results show that this ANN approach makes H2 combustion simulation possible when coupled to the RFM framework and using a 10-species kinetic mechanism.</description>
	<pubDate>2026-04-22</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 105: A Neural Network Approach for the Simulation of Real Fluid Two-Phase Combustion Using a Multi-Species (H2/O2) Mechanism</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/5/105">doi: 10.3390/fluids11050105</a></p>
	<p>Authors:
		Bruno Delhom
		Chaouki Habchi
		Olivier Colin
		Julien Bohbot
		</p>
	<p>Fully compressible two-phase flow configurations present many challenges for numerical modelling, requiring the development of Real Fluid Models (RFMs) able to simulate flows in subcritical, transcritical and supercritical regimes. Such an RFM has been recently developed at IFPEN based on physical properties lookup tables, mainly for binary and ternary chemical systems. This paper proposes an Artificial Neural Network (ANN) approach to overcome the limitations of lookup tables of thermodynamic properties and to apply RFM to multi-species combustion. A methodology for generating an optimized data set by combining a vapor&amp;amp;ndash;liquid equilibrium (VLE) thermodynamic solver and the in situ adaptive tabulation (ISAT) method is developed. It aims to improve the neural network training process for two-phase combustion simulations where many species are present. This ANN methodology has been implemented in the CONVERGE CFD solver and validated using a mixing layer (LOX/GH2) benchmark from the literature relevant to rocket conditions, and an academic gaseous (H2/O2) case relevant to hydrogen combustion. The results show that this ANN approach makes H2 combustion simulation possible when coupled to the RFM framework and using a 10-species kinetic mechanism.</p>
	]]></content:encoded>

	<dc:title>A Neural Network Approach for the Simulation of Real Fluid Two-Phase Combustion Using a Multi-Species (H2/O2) Mechanism</dc:title>
			<dc:creator>Bruno Delhom</dc:creator>
			<dc:creator>Chaouki Habchi</dc:creator>
			<dc:creator>Olivier Colin</dc:creator>
			<dc:creator>Julien Bohbot</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11050105</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-22</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-22</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>5</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>105</prism:startingPage>
		<prism:doi>10.3390/fluids11050105</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/5/105</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/104">

	<title>Fluids, Vol. 11, Pages 104: The Impact of Sample Size on X-Ray Microtomography Measurements of Fluid&amp;ndash;Fluid Interfacial Areas</title>
	<link>https://www.mdpi.com/2311-5521/11/4/104</link>
	<description>This work investigates the impact of sample size on the measurement of non-wetting/wetting interfacial areas in porous media by X-ray microtomography (XMT). Standard-sized small columns and significantly larger columns, both packed with sand, were imaged using the same industrial XMT system (IMT). Additional small columns were imaged using synchrotron XMT (SMT) to evaluate the comparability between the different systems. The mean bulk densities and porosities for all three imaged sets are statistically identical, indicating that column preparations were robust. The mean non-wetting/wetting interfacial areas measured for the large columns for the low and moderate NAPL saturations (Sn), were 11.3 cm&amp;amp;minus;1 (Sn = 0.13) and 15.3 cm&amp;amp;minus;1 (Sn = 0.22), respectively. The mean interfacial areas measured at the moderate Sn for the two small columns imaged by IMT (16.7 cm&amp;amp;minus;1, Sn = 0.24) and imaged by SMT (16.9 cm&amp;amp;minus;1, Sn = 0.21) are consistent with those of the larger column. In addition, the mean interfacial area measured at the lower Sn for the two small columns imaged by SMT (9.4 cm&amp;amp;minus;1, Sn = 0.12) is consistent with that of the larger column. The results indicate that the small imaged volumes typically used for XMT are sufficient to establish REV conditions for measurement of fluid&amp;amp;ndash;fluid interfacial areas in this sand.</description>
	<pubDate>2026-04-21</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 104: The Impact of Sample Size on X-Ray Microtomography Measurements of Fluid&amp;ndash;Fluid Interfacial Areas</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/104">doi: 10.3390/fluids11040104</a></p>
	<p>Authors:
		Juliana B. Araujo
		Kieran McDonald
		Kenneth C. Carroll
		Mark L. Brusseau
		</p>
	<p>This work investigates the impact of sample size on the measurement of non-wetting/wetting interfacial areas in porous media by X-ray microtomography (XMT). Standard-sized small columns and significantly larger columns, both packed with sand, were imaged using the same industrial XMT system (IMT). Additional small columns were imaged using synchrotron XMT (SMT) to evaluate the comparability between the different systems. The mean bulk densities and porosities for all three imaged sets are statistically identical, indicating that column preparations were robust. The mean non-wetting/wetting interfacial areas measured for the large columns for the low and moderate NAPL saturations (Sn), were 11.3 cm&amp;amp;minus;1 (Sn = 0.13) and 15.3 cm&amp;amp;minus;1 (Sn = 0.22), respectively. The mean interfacial areas measured at the moderate Sn for the two small columns imaged by IMT (16.7 cm&amp;amp;minus;1, Sn = 0.24) and imaged by SMT (16.9 cm&amp;amp;minus;1, Sn = 0.21) are consistent with those of the larger column. In addition, the mean interfacial area measured at the lower Sn for the two small columns imaged by SMT (9.4 cm&amp;amp;minus;1, Sn = 0.12) is consistent with that of the larger column. The results indicate that the small imaged volumes typically used for XMT are sufficient to establish REV conditions for measurement of fluid&amp;amp;ndash;fluid interfacial areas in this sand.</p>
	]]></content:encoded>

	<dc:title>The Impact of Sample Size on X-Ray Microtomography Measurements of Fluid&amp;amp;ndash;Fluid Interfacial Areas</dc:title>
			<dc:creator>Juliana B. Araujo</dc:creator>
			<dc:creator>Kieran McDonald</dc:creator>
			<dc:creator>Kenneth C. Carroll</dc:creator>
			<dc:creator>Mark L. Brusseau</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040104</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-21</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-21</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>104</prism:startingPage>
		<prism:doi>10.3390/fluids11040104</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/104</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/103">

	<title>Fluids, Vol. 11, Pages 103: Flow-Field Characterization of Multiple Low-Density Gas Jets Impinging on a Wall at a Short Distance Using PIV</title>
	<link>https://www.mdpi.com/2311-5521/11/4/103</link>
	<description>This paper studies the dynamics of a low-density gas directly injected onto a flat wall, focusing on the influence of different pressure ratios (PRs) and plate position. Due to safety reasons, Helium (He) was employed as substitute to reproduce the mixing characteristics of hydrogen. A Nd:YAG laser has been used to generate the luminous background in the constant volume chamber (CVC) and vegetable oil particles as trackers to identify the induced flow-field. Two configurations were investigated: the first, with a flat wall perpendicularly positioned at an axial distance of 10 mm from the injector tip, and the second with the same plate at 30 mm downstream of the injector, inclined at 30&amp;amp;deg;. The pressure of injection was swept from 20 to 50 bar, while the backpressure inside the CVC ranged from 2 to 6 bar to enable the reproduction of five different values of PRs: 3, 4, 7, 10 and 17. The comparison of the results in the two configurations has highlighted the role of the plate at short distance in decelerating the jet speed (230 m/s to 160 m/s) while improving the vorticity intensity (+10%). In addition, a stagnation region was observed to form on the flat wall, downstream of the injector axis for 10 mm configuration. In this area the velocity ranged from 50% to 60% compared to the average jet speed. This phenomenon was noted to be less pronounced with the 30 mm, 30&amp;amp;deg; configuration that led to a more contained speed reduction to 150&amp;amp;ndash;160%.</description>
	<pubDate>2026-04-19</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 103: Flow-Field Characterization of Multiple Low-Density Gas Jets Impinging on a Wall at a Short Distance Using PIV</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/103">doi: 10.3390/fluids11040103</a></p>
	<p>Authors:
		Giovanni Cecere
		Mats Andersson
		Simona Silvia Merola
		Adrian Irimescu
		</p>
	<p>This paper studies the dynamics of a low-density gas directly injected onto a flat wall, focusing on the influence of different pressure ratios (PRs) and plate position. Due to safety reasons, Helium (He) was employed as substitute to reproduce the mixing characteristics of hydrogen. A Nd:YAG laser has been used to generate the luminous background in the constant volume chamber (CVC) and vegetable oil particles as trackers to identify the induced flow-field. Two configurations were investigated: the first, with a flat wall perpendicularly positioned at an axial distance of 10 mm from the injector tip, and the second with the same plate at 30 mm downstream of the injector, inclined at 30&amp;amp;deg;. The pressure of injection was swept from 20 to 50 bar, while the backpressure inside the CVC ranged from 2 to 6 bar to enable the reproduction of five different values of PRs: 3, 4, 7, 10 and 17. The comparison of the results in the two configurations has highlighted the role of the plate at short distance in decelerating the jet speed (230 m/s to 160 m/s) while improving the vorticity intensity (+10%). In addition, a stagnation region was observed to form on the flat wall, downstream of the injector axis for 10 mm configuration. In this area the velocity ranged from 50% to 60% compared to the average jet speed. This phenomenon was noted to be less pronounced with the 30 mm, 30&amp;amp;deg; configuration that led to a more contained speed reduction to 150&amp;amp;ndash;160%.</p>
	]]></content:encoded>

	<dc:title>Flow-Field Characterization of Multiple Low-Density Gas Jets Impinging on a Wall at a Short Distance Using PIV</dc:title>
			<dc:creator>Giovanni Cecere</dc:creator>
			<dc:creator>Mats Andersson</dc:creator>
			<dc:creator>Simona Silvia Merola</dc:creator>
			<dc:creator>Adrian Irimescu</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040103</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-19</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-19</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>103</prism:startingPage>
		<prism:doi>10.3390/fluids11040103</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/103</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/102">

	<title>Fluids, Vol. 11, Pages 102: ElectroHydroDynamic Manipulation of Rising Bubbles</title>
	<link>https://www.mdpi.com/2311-5521/11/4/102</link>
	<description>This study examines the electrohydrodynamic (EHD) behavior of air bubbles rising in deionized water under a non-uniform electric field, with particular emphasis on the influence of applied voltage (0.5&amp;amp;ndash;3.0 kV) and gas flow rates of 30 and 40 mL min&amp;amp;minus;1 (corresponding to Reynolds numbers of Reg=107&amp;amp;ndash;142) on bubble dynamics. High-speed imaging reveals bubbles with equivalent diameters in the range of deq&amp;amp;asymp;0.8&amp;amp;ndash;3.5 mm, enabling a detailed characterization of their deformation, trajectory, and interfacial response under coupled hydrodynamic and electric stresses. At Reg=107, bubbles exhibited stable vertical trajectories with negligible lateral displacement, whereas at Reg=142, inertial and wake effects induced deviations. Increasing BoE reduced lateral displacement, restoring alignment with the electric field. Bubble rise velocities increased by &amp;amp;sim;20&amp;amp;ndash;30% with applied voltage due to polarization-driven EHD forces. A transition from hydrodynamically dominated to EHD-dominated regimes was identified. While polarization forces govern the initial bubble motion under a strong electric field, bubbles progressively transition downstream to a hydrodynamic regime as the electric field weakens, reducing the influence of polarization effects. These findings provide quantitative insight into coupled hydrodynamic&amp;amp;ndash;electrohydrodynamic interactions and support the development of predictive models for controlling bubble trajectories, with implications for electrically tunable multiphase and microfluidic systems.</description>
	<pubDate>2026-04-17</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 102: ElectroHydroDynamic Manipulation of Rising Bubbles</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/102">doi: 10.3390/fluids11040102</a></p>
	<p>Authors:
		Aaron Albuja
		Juan Bacuy
		Fernando Almeida
		Luis Carrión
		Byron Cortez
		Josué Pazmiño
		César Portero
		Wilmer Suárez
		Christian Narváez-Muñoz
		</p>
	<p>This study examines the electrohydrodynamic (EHD) behavior of air bubbles rising in deionized water under a non-uniform electric field, with particular emphasis on the influence of applied voltage (0.5&amp;amp;ndash;3.0 kV) and gas flow rates of 30 and 40 mL min&amp;amp;minus;1 (corresponding to Reynolds numbers of Reg=107&amp;amp;ndash;142) on bubble dynamics. High-speed imaging reveals bubbles with equivalent diameters in the range of deq&amp;amp;asymp;0.8&amp;amp;ndash;3.5 mm, enabling a detailed characterization of their deformation, trajectory, and interfacial response under coupled hydrodynamic and electric stresses. At Reg=107, bubbles exhibited stable vertical trajectories with negligible lateral displacement, whereas at Reg=142, inertial and wake effects induced deviations. Increasing BoE reduced lateral displacement, restoring alignment with the electric field. Bubble rise velocities increased by &amp;amp;sim;20&amp;amp;ndash;30% with applied voltage due to polarization-driven EHD forces. A transition from hydrodynamically dominated to EHD-dominated regimes was identified. While polarization forces govern the initial bubble motion under a strong electric field, bubbles progressively transition downstream to a hydrodynamic regime as the electric field weakens, reducing the influence of polarization effects. These findings provide quantitative insight into coupled hydrodynamic&amp;amp;ndash;electrohydrodynamic interactions and support the development of predictive models for controlling bubble trajectories, with implications for electrically tunable multiphase and microfluidic systems.</p>
	]]></content:encoded>

	<dc:title>ElectroHydroDynamic Manipulation of Rising Bubbles</dc:title>
			<dc:creator>Aaron Albuja</dc:creator>
			<dc:creator>Juan Bacuy</dc:creator>
			<dc:creator>Fernando Almeida</dc:creator>
			<dc:creator>Luis Carrión</dc:creator>
			<dc:creator>Byron Cortez</dc:creator>
			<dc:creator>Josué Pazmiño</dc:creator>
			<dc:creator>César Portero</dc:creator>
			<dc:creator>Wilmer Suárez</dc:creator>
			<dc:creator>Christian Narváez-Muñoz</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040102</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-17</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-17</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>102</prism:startingPage>
		<prism:doi>10.3390/fluids11040102</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/102</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/101">

	<title>Fluids, Vol. 11, Pages 101: Friction Drag Characteristics of Non-Newtonian Weighted Fracturing Fluids in Pipe Flows</title>
	<link>https://www.mdpi.com/2311-5521/11/4/101</link>
	<description>Non-Newtonian weighted fracturing fluids are used to carry out hydraulic fracturing operations into the deep and ultra-deep earth for oil and gas extraction, though their flow and friction drag characteristics are largely unknown. This study aims to understand the abovementioned characteristics. An engineering-oriented cost-effective numerical scheme is deployed, incorporating LES with a generalized Newtonian fluid constitutive equation, for predicting the non-Newtonian pipe flow and friction drag coefficient Cf. The weighted fracturing fluid is described as a power-law fluid, i.e., viscosity &amp;amp;mu;(&amp;amp;gamma;&amp;amp;#729;)=K&amp;amp;gamma;&amp;amp;#729;n&amp;amp;minus;1, where both K and n are coefficients related to fluid rheology, and &amp;amp;gamma;&amp;amp;#729; is the shear rate. The influences of fluid density &amp;amp;rho;, mean velocity U and pipe diameter D, as well as K and n on Cf were documented and compared with a water pipe flow. It was found that Cf = f1 (K, n, &amp;amp;rho;, U, D) may be reduced to Cf = f2 (Reg), where the scaling factor Reg = &amp;amp;rho;U2&amp;amp;minus;nDn/(K8n&amp;amp;minus;1) is the generalized Reynolds number. This scaling law can reasonably well predict the friction drag variation in the pipe flow of non-Newtonian weighted fracturing fluids throughout a range of interests and engineering applications.</description>
	<pubDate>2026-04-17</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 101: Friction Drag Characteristics of Non-Newtonian Weighted Fracturing Fluids in Pipe Flows</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/101">doi: 10.3390/fluids11040101</a></p>
	<p>Authors:
		Jianxin Peng
		Liwei Wang
		Xin Qiao
		Ju Liu
		Sixin Li
		Wen Zhang
		Yanyan Feng
		Zhanying Zheng
		Yu Zhou
		</p>
	<p>Non-Newtonian weighted fracturing fluids are used to carry out hydraulic fracturing operations into the deep and ultra-deep earth for oil and gas extraction, though their flow and friction drag characteristics are largely unknown. This study aims to understand the abovementioned characteristics. An engineering-oriented cost-effective numerical scheme is deployed, incorporating LES with a generalized Newtonian fluid constitutive equation, for predicting the non-Newtonian pipe flow and friction drag coefficient Cf. The weighted fracturing fluid is described as a power-law fluid, i.e., viscosity &amp;amp;mu;(&amp;amp;gamma;&amp;amp;#729;)=K&amp;amp;gamma;&amp;amp;#729;n&amp;amp;minus;1, where both K and n are coefficients related to fluid rheology, and &amp;amp;gamma;&amp;amp;#729; is the shear rate. The influences of fluid density &amp;amp;rho;, mean velocity U and pipe diameter D, as well as K and n on Cf were documented and compared with a water pipe flow. It was found that Cf = f1 (K, n, &amp;amp;rho;, U, D) may be reduced to Cf = f2 (Reg), where the scaling factor Reg = &amp;amp;rho;U2&amp;amp;minus;nDn/(K8n&amp;amp;minus;1) is the generalized Reynolds number. This scaling law can reasonably well predict the friction drag variation in the pipe flow of non-Newtonian weighted fracturing fluids throughout a range of interests and engineering applications.</p>
	]]></content:encoded>

	<dc:title>Friction Drag Characteristics of Non-Newtonian Weighted Fracturing Fluids in Pipe Flows</dc:title>
			<dc:creator>Jianxin Peng</dc:creator>
			<dc:creator>Liwei Wang</dc:creator>
			<dc:creator>Xin Qiao</dc:creator>
			<dc:creator>Ju Liu</dc:creator>
			<dc:creator>Sixin Li</dc:creator>
			<dc:creator>Wen Zhang</dc:creator>
			<dc:creator>Yanyan Feng</dc:creator>
			<dc:creator>Zhanying Zheng</dc:creator>
			<dc:creator>Yu Zhou</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040101</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-17</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-17</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>101</prism:startingPage>
		<prism:doi>10.3390/fluids11040101</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/101</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/100">

	<title>Fluids, Vol. 11, Pages 100: A Novel Neural Network-Based Symbolic Approach for Shallow-Water Waves with Surface Tension</title>
	<link>https://www.mdpi.com/2311-5521/11/4/100</link>
	<description>This paper examines the sixth-order generalized Boussinesq equation, which describes the dynamics of shallow-water waves, including the effects of surface tension. The study introduces Kudryashov&amp;amp;rsquo;s R-function neural network approach for the first time, aiming to provide exact solutions to the nonlinear differential equation that represents the mathematical model of the sixth-order generalized Boussinesq equation. This technique incorporates the solutions of a nonlinear differential equation into neural networks, using them as an activation function within the hidden layer. In line with previous research on this topic, two categories of solutions are derived: solitary wave and shock wave solutions. Additionally, this paper includes 3D and 2D graphs to visually represent the solutions obtained.</description>
	<pubDate>2026-04-15</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 100: A Novel Neural Network-Based Symbolic Approach for Shallow-Water Waves with Surface Tension</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/100">doi: 10.3390/fluids11040100</a></p>
	<p>Authors:
		Oswaldo González-Gaxiola
		Milisha Hart-Simmons
		Husham M. Ahmed
		Anjan Biswas
		</p>
	<p>This paper examines the sixth-order generalized Boussinesq equation, which describes the dynamics of shallow-water waves, including the effects of surface tension. The study introduces Kudryashov&amp;amp;rsquo;s R-function neural network approach for the first time, aiming to provide exact solutions to the nonlinear differential equation that represents the mathematical model of the sixth-order generalized Boussinesq equation. This technique incorporates the solutions of a nonlinear differential equation into neural networks, using them as an activation function within the hidden layer. In line with previous research on this topic, two categories of solutions are derived: solitary wave and shock wave solutions. Additionally, this paper includes 3D and 2D graphs to visually represent the solutions obtained.</p>
	]]></content:encoded>

	<dc:title>A Novel Neural Network-Based Symbolic Approach for Shallow-Water Waves with Surface Tension</dc:title>
			<dc:creator>Oswaldo González-Gaxiola</dc:creator>
			<dc:creator>Milisha Hart-Simmons</dc:creator>
			<dc:creator>Husham M. Ahmed</dc:creator>
			<dc:creator>Anjan Biswas</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040100</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-15</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-15</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>100</prism:startingPage>
		<prism:doi>10.3390/fluids11040100</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/100</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/99">

	<title>Fluids, Vol. 11, Pages 99: A New Wall-Dependent Identification Method for Coherent Streamwise Streaks in Turbulent Channel Flows</title>
	<link>https://www.mdpi.com/2311-5521/11/4/99</link>
	<description>A wall-dependent identification method for low-speed streamwise streaks in turbulent channel flows is presented to overcome a key limitation of uniform thresholds, which tend to produce either an excess of detected structures near the wall or an apparent lack of streaks farther from it. The method is constructed following wall-dependent threshold requirements established in the literature and is applied to DNS data of Couette&amp;amp;ndash;Poiseuille flows at Re&amp;amp;tau;&amp;amp;asymp;250 using percolation analysis and clustering to extract three-dimensional objects. In addition, a percolation study at a significantly higher Reynolds number is included to assess the effect and robustness of the filter beyond the reference case. Although some global trends remain consistent with previous results obtained using uniform thresholds, the present work provides a direct comparison between both approaches and shows more clearly how the threshold definition affects the identification of streaks away from the wall. The detected structures are classified into wall-attached and wall-detached families, separated by a transition region at ymin+=20, and both exhibit self-similar geometric trends. Their spatial distribution is also analysed, showing differences mainly associated with the alignment of attached streaks in pure Poiseuille and pure Couette flows.</description>
	<pubDate>2026-04-12</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 99: A New Wall-Dependent Identification Method for Coherent Streamwise Streaks in Turbulent Channel Flows</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/99">doi: 10.3390/fluids11040099</a></p>
	<p>Authors:
		Sergio Gandía-Barberá
		Sergio Hoyas
		María J. Pérez-Quiles
		</p>
	<p>A wall-dependent identification method for low-speed streamwise streaks in turbulent channel flows is presented to overcome a key limitation of uniform thresholds, which tend to produce either an excess of detected structures near the wall or an apparent lack of streaks farther from it. The method is constructed following wall-dependent threshold requirements established in the literature and is applied to DNS data of Couette&amp;amp;ndash;Poiseuille flows at Re&amp;amp;tau;&amp;amp;asymp;250 using percolation analysis and clustering to extract three-dimensional objects. In addition, a percolation study at a significantly higher Reynolds number is included to assess the effect and robustness of the filter beyond the reference case. Although some global trends remain consistent with previous results obtained using uniform thresholds, the present work provides a direct comparison between both approaches and shows more clearly how the threshold definition affects the identification of streaks away from the wall. The detected structures are classified into wall-attached and wall-detached families, separated by a transition region at ymin+=20, and both exhibit self-similar geometric trends. Their spatial distribution is also analysed, showing differences mainly associated with the alignment of attached streaks in pure Poiseuille and pure Couette flows.</p>
	]]></content:encoded>

	<dc:title>A New Wall-Dependent Identification Method for Coherent Streamwise Streaks in Turbulent Channel Flows</dc:title>
			<dc:creator>Sergio Gandía-Barberá</dc:creator>
			<dc:creator>Sergio Hoyas</dc:creator>
			<dc:creator>María J. Pérez-Quiles</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040099</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-12</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-12</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>99</prism:startingPage>
		<prism:doi>10.3390/fluids11040099</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/99</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/98">

	<title>Fluids, Vol. 11, Pages 98: Numerical Study on Flow Characteristics of the Slurry-Feeding System in a Hydrojet Shield</title>
	<link>https://www.mdpi.com/2311-5521/11/4/98</link>
	<description>The hydrojet-shield machine, a rapidly advancing shield machine type, uses slurry for excavation and muck removal via a pipeline system. The pipeline includes a flushed feeding system that injects slurry into areas at risk of obstruction. This study provides a computational fluid dynamics (CFD) analysis of the flow characteristics of a large hydraulic shield machine, proposing the Particle Lifting Coefficient (L) and Regional Improvement Ratio (I) as innovative criteria to evaluate the effects of flow rate distribution and cutting wheel rotational velocity. By adjusting the proportion of scouring flow in the lower part of the chambers to 30%, 50%, and 100%, three flow distribution strategies, labeled as FC1, FC2, and FC3, were obtained to suit normal slurry transport conditions, address cutterhead mud accumulation, and deal with the deposition of rock and soil particles at the bottom of the chamber, respectively. The FC3 strategy amplifies the flow of symmetric jets in the lower scouring region, strengthening the upward flow that entrains surrounding fluid, thereby significantly increasing the L and I values in the targeted area and showing great potential for inhibiting the settlement and deposition of rock and soil debris. This study also emphasizes the need to integrate slurry jet distribution strategies with real-time monitoring of cutterhead mud accumulation and chamber deposition, while adjusting cutterhead rotation speed based on geological conditions.</description>
	<pubDate>2026-04-12</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 98: Numerical Study on Flow Characteristics of the Slurry-Feeding System in a Hydrojet Shield</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/98">doi: 10.3390/fluids11040098</a></p>
	<p>Authors:
		Hao Jia
		Hao Feng
		Yapeng Wang
		Jiuchun Sun
		Xiaopeng Sun
		Yunlong Sang
		Haitao Wang
		</p>
	<p>The hydrojet-shield machine, a rapidly advancing shield machine type, uses slurry for excavation and muck removal via a pipeline system. The pipeline includes a flushed feeding system that injects slurry into areas at risk of obstruction. This study provides a computational fluid dynamics (CFD) analysis of the flow characteristics of a large hydraulic shield machine, proposing the Particle Lifting Coefficient (L) and Regional Improvement Ratio (I) as innovative criteria to evaluate the effects of flow rate distribution and cutting wheel rotational velocity. By adjusting the proportion of scouring flow in the lower part of the chambers to 30%, 50%, and 100%, three flow distribution strategies, labeled as FC1, FC2, and FC3, were obtained to suit normal slurry transport conditions, address cutterhead mud accumulation, and deal with the deposition of rock and soil particles at the bottom of the chamber, respectively. The FC3 strategy amplifies the flow of symmetric jets in the lower scouring region, strengthening the upward flow that entrains surrounding fluid, thereby significantly increasing the L and I values in the targeted area and showing great potential for inhibiting the settlement and deposition of rock and soil debris. This study also emphasizes the need to integrate slurry jet distribution strategies with real-time monitoring of cutterhead mud accumulation and chamber deposition, while adjusting cutterhead rotation speed based on geological conditions.</p>
	]]></content:encoded>

	<dc:title>Numerical Study on Flow Characteristics of the Slurry-Feeding System in a Hydrojet Shield</dc:title>
			<dc:creator>Hao Jia</dc:creator>
			<dc:creator>Hao Feng</dc:creator>
			<dc:creator>Yapeng Wang</dc:creator>
			<dc:creator>Jiuchun Sun</dc:creator>
			<dc:creator>Xiaopeng Sun</dc:creator>
			<dc:creator>Yunlong Sang</dc:creator>
			<dc:creator>Haitao Wang</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040098</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-12</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-12</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>98</prism:startingPage>
		<prism:doi>10.3390/fluids11040098</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/98</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/97">

	<title>Fluids, Vol. 11, Pages 97: Pressure Fluctuation and Cavitation Generation Downstream of a Jet in Crossflow</title>
	<link>https://www.mdpi.com/2311-5521/11/4/97</link>
	<description>Pressure fluctuations caused by a jet in crossflow (JICF) can induce cavitation and potentially damage wall surfaces. In mercury targets for a pulsed spallation neutron source, where cavitation damage progresses due to thermal shock, mercury is confined within a vessel that incorporates a double-wall structure&amp;amp;mdash;comprising a narrow channel and a main flow channel&amp;amp;mdash;to form parallel flows and suppress damage. However, as the damage progressed, penetration holes were formed in the inner wall separating these flows, and characteristic damage patterns were observed that suggest accelerated damage progression caused by JICF, in which a jet flows from the narrow channel into the main channel. The mechanism underlying this phenomenon has not been fully clarified. Therefore, the flow field and pressure fluctuations around the penetration hole were evaluated using PIV measurements in a water loop and numerical simulations of single-phase flow, with varying jet velocity and jet width. The results revealed that inflow through the penetration in the inner wall generates JICF, which produces vortices downstream of the inflow jet and induces pressure fluctuations that may be associated with cavitation.</description>
	<pubDate>2026-04-10</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 97: Pressure Fluctuation and Cavitation Generation Downstream of a Jet in Crossflow</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/97">doi: 10.3390/fluids11040097</a></p>
	<p>Authors:
		Hiroyuki Kogawa
		Yoshiki Maeda
		Masatoshi Futakawa
		Yanrong Li
		</p>
	<p>Pressure fluctuations caused by a jet in crossflow (JICF) can induce cavitation and potentially damage wall surfaces. In mercury targets for a pulsed spallation neutron source, where cavitation damage progresses due to thermal shock, mercury is confined within a vessel that incorporates a double-wall structure&amp;amp;mdash;comprising a narrow channel and a main flow channel&amp;amp;mdash;to form parallel flows and suppress damage. However, as the damage progressed, penetration holes were formed in the inner wall separating these flows, and characteristic damage patterns were observed that suggest accelerated damage progression caused by JICF, in which a jet flows from the narrow channel into the main channel. The mechanism underlying this phenomenon has not been fully clarified. Therefore, the flow field and pressure fluctuations around the penetration hole were evaluated using PIV measurements in a water loop and numerical simulations of single-phase flow, with varying jet velocity and jet width. The results revealed that inflow through the penetration in the inner wall generates JICF, which produces vortices downstream of the inflow jet and induces pressure fluctuations that may be associated with cavitation.</p>
	]]></content:encoded>

	<dc:title>Pressure Fluctuation and Cavitation Generation Downstream of a Jet in Crossflow</dc:title>
			<dc:creator>Hiroyuki Kogawa</dc:creator>
			<dc:creator>Yoshiki Maeda</dc:creator>
			<dc:creator>Masatoshi Futakawa</dc:creator>
			<dc:creator>Yanrong Li</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040097</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-10</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-10</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>97</prism:startingPage>
		<prism:doi>10.3390/fluids11040097</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/97</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/96">

	<title>Fluids, Vol. 11, Pages 96: Study of Supercritical CO2 Pipeline Flow Leaks: Effects of Equation of State, Impurity, and Outlet Diameter</title>
	<link>https://www.mdpi.com/2311-5521/11/4/96</link>
	<description>The growing need to mitigate climate change has accelerated the development of Carbon Capture, Utilization, and Storage (CCUS) technologies, where the safe transport of supercritical CO2 (sCO2) through pipelines is a key challenge. The flow behavior in such systems is strongly influenced by phase-change processes under transient conditions such as decompression and heat transfer and is further complicated by the presence of impurities (e.g., N2, CH4, and Ar). These impurities modify thermodynamic properties and phase boundaries, thereby affecting the overall flow dynamics. In this study, the influence of impurities on leakage, mass flow rate, and decompression wave propagation in sCO2 pipelines is investigated using computational fluid dynamics (CFD) simulations. A real-fluid model (RFM) implemented in the CONVERGE CFD solver is employed, with a tabulation-based approach to accurately capture thermodynamic and transport properties across multiphase regimes. The simulations were validated against available experimental data and performed for varying impurity concentrations to assess their impact on key flow variables, including pressure, temperature, and wave speed. Although simplifying assumptions were used, the results are in fairly good agreement with experimental observations and provide a better understanding of the phase behavior induced by impurities during transient decompression. Additionally, the effects of outlet geometry, pipeline configuration, and the choice of equation of state are examined, highlighting their influence on the predicted flow response. The validity of the RFM modeling framework is further demonstrated by simulations of a large-scale pipeline configuration representative of industrial conditions, which will serve as a benchmark for future improvements.</description>
	<pubDate>2026-04-09</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 96: Study of Supercritical CO2 Pipeline Flow Leaks: Effects of Equation of State, Impurity, and Outlet Diameter</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/96">doi: 10.3390/fluids11040096</a></p>
	<p>Authors:
		Krishna Kant
		Chaouki Habchi
		Martha Hajiw-Riberaud
		Al-Hassan Afailal
		Jean-Charles de Hemptinne
		</p>
	<p>The growing need to mitigate climate change has accelerated the development of Carbon Capture, Utilization, and Storage (CCUS) technologies, where the safe transport of supercritical CO2 (sCO2) through pipelines is a key challenge. The flow behavior in such systems is strongly influenced by phase-change processes under transient conditions such as decompression and heat transfer and is further complicated by the presence of impurities (e.g., N2, CH4, and Ar). These impurities modify thermodynamic properties and phase boundaries, thereby affecting the overall flow dynamics. In this study, the influence of impurities on leakage, mass flow rate, and decompression wave propagation in sCO2 pipelines is investigated using computational fluid dynamics (CFD) simulations. A real-fluid model (RFM) implemented in the CONVERGE CFD solver is employed, with a tabulation-based approach to accurately capture thermodynamic and transport properties across multiphase regimes. The simulations were validated against available experimental data and performed for varying impurity concentrations to assess their impact on key flow variables, including pressure, temperature, and wave speed. Although simplifying assumptions were used, the results are in fairly good agreement with experimental observations and provide a better understanding of the phase behavior induced by impurities during transient decompression. Additionally, the effects of outlet geometry, pipeline configuration, and the choice of equation of state are examined, highlighting their influence on the predicted flow response. The validity of the RFM modeling framework is further demonstrated by simulations of a large-scale pipeline configuration representative of industrial conditions, which will serve as a benchmark for future improvements.</p>
	]]></content:encoded>

	<dc:title>Study of Supercritical CO2 Pipeline Flow Leaks: Effects of Equation of State, Impurity, and Outlet Diameter</dc:title>
			<dc:creator>Krishna Kant</dc:creator>
			<dc:creator>Chaouki Habchi</dc:creator>
			<dc:creator>Martha Hajiw-Riberaud</dc:creator>
			<dc:creator>Al-Hassan Afailal</dc:creator>
			<dc:creator>Jean-Charles de Hemptinne</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040096</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-09</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-09</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>96</prism:startingPage>
		<prism:doi>10.3390/fluids11040096</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/96</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/95">

	<title>Fluids, Vol. 11, Pages 95: Multidisciplinary Analysis of Dripping and Leakage Problems in Kitchenware: Design, Material, and Ergonomic Approaches to the Teapot Effect</title>
	<link>https://www.mdpi.com/2311-5521/11/4/95</link>
	<description>This study investigates the dripping and leakage problem in kitchenware known as the &amp;amp;ldquo;teapot effect&amp;amp;rdquo; through a multidisciplinary experimental approach encompassing fluid mechanics, material science, and ergonomic design. Unlike previous studies confined to idealized geometries and single-fluid analyses, this work systematically examines 32 distinct spout geometries from commercially available teapots, coffee pots, and milk jugs under realistic operating conditions. Experiments were performed using three fluids with contrasting rheological properties: boiling black tea, cow&amp;amp;rsquo;s milk, and Turkish coffee on a precision rotating platform operating at quasi-static (1&amp;amp;deg;/s) to isolate surface tension, gravitational, and geometric effects from inertial forces. Three quantitative parameters were measured for each specimen: capillary dome angle, teapot effect angle range, and optimum pouring angle. Results demonstrate that spout tip geometry is the dominant controlling parameter. Thin-lipped elliptical cross-sections effectively suppressed dripping, whereas triangular and wide curved geometries produced the teapot effect across broad pouring angle ranges reaching up to 70&amp;amp;deg;. A spout outlet extension length of 4&amp;amp;ndash;5 mm combined with a spout tip radius below 4 mm was found necessary and sufficient for clean flow separation. Furthermore, suspended particles and proteins in milk and Turkish coffee were shown to intensify the teapot effect by disrupting contact line dynamics at the spout tip. These findings provide quantitative design thresholds directly applicable to industrial kitchenware development.</description>
	<pubDate>2026-04-07</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 95: Multidisciplinary Analysis of Dripping and Leakage Problems in Kitchenware: Design, Material, and Ergonomic Approaches to the Teapot Effect</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/95">doi: 10.3390/fluids11040095</a></p>
	<p>Authors:
		Batuhan Göçen
		</p>
	<p>This study investigates the dripping and leakage problem in kitchenware known as the &amp;amp;ldquo;teapot effect&amp;amp;rdquo; through a multidisciplinary experimental approach encompassing fluid mechanics, material science, and ergonomic design. Unlike previous studies confined to idealized geometries and single-fluid analyses, this work systematically examines 32 distinct spout geometries from commercially available teapots, coffee pots, and milk jugs under realistic operating conditions. Experiments were performed using three fluids with contrasting rheological properties: boiling black tea, cow&amp;amp;rsquo;s milk, and Turkish coffee on a precision rotating platform operating at quasi-static (1&amp;amp;deg;/s) to isolate surface tension, gravitational, and geometric effects from inertial forces. Three quantitative parameters were measured for each specimen: capillary dome angle, teapot effect angle range, and optimum pouring angle. Results demonstrate that spout tip geometry is the dominant controlling parameter. Thin-lipped elliptical cross-sections effectively suppressed dripping, whereas triangular and wide curved geometries produced the teapot effect across broad pouring angle ranges reaching up to 70&amp;amp;deg;. A spout outlet extension length of 4&amp;amp;ndash;5 mm combined with a spout tip radius below 4 mm was found necessary and sufficient for clean flow separation. Furthermore, suspended particles and proteins in milk and Turkish coffee were shown to intensify the teapot effect by disrupting contact line dynamics at the spout tip. These findings provide quantitative design thresholds directly applicable to industrial kitchenware development.</p>
	]]></content:encoded>

	<dc:title>Multidisciplinary Analysis of Dripping and Leakage Problems in Kitchenware: Design, Material, and Ergonomic Approaches to the Teapot Effect</dc:title>
			<dc:creator>Batuhan Göçen</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040095</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-07</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-07</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>95</prism:startingPage>
		<prism:doi>10.3390/fluids11040095</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/95</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/94">

	<title>Fluids, Vol. 11, Pages 94: Evaluating Alternatives for Combined Modeling of Gas Cavities and Unsteady Friction in Closed-Pipe Transients</title>
	<link>https://www.mdpi.com/2311-5521/11/4/94</link>
	<description>Hydraulic transients in pressurized pipe systems are significantly influenced by the presence of entrapped air, which alters wave propagation through increased compressibility and energy dissipation. Traditional discrete cavity models, such as the Discrete Gas Cavity Model (DGCM), often assume a constant wave celerity, which limits their accuracy under high gas content conditions. This study evaluated different approaches for representing the effects of gas cavities and unsteady friction in closed pipe transients. The work introduces the Adjustable-celerity Gas Cavity Model (AGCM), a formulation that explicitly couples local air volume and pressure to dynamically adjusted celerity values. Two variants are considered, a non-iterative (AGCM.v1) and an iterative approach (AGCM.v2), the latter ensuring consistency between pressure head and celerity at each time step. The models were evaluated through numerical simulations using both experimental datasets and a hypothetical test case with increasing air fractions. Results show that the AGCM was able to represent celerity magnitudes in unsteady flows with large fractions of air. Also, while constant-celerity models perform well under low-air conditions, variable-celerity formulations offer superior consistency in predicting wave amplitudes and celerity dynamics as gas content increases. These findings underscore the importance of dynamic celerity coupling in transient flow modeling and validate the AGCM as a useful approach for transient modeling in conditions with higher air phase fractions.</description>
	<pubDate>2026-04-03</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 94: Evaluating Alternatives for Combined Modeling of Gas Cavities and Unsteady Friction in Closed-Pipe Transients</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/94">doi: 10.3390/fluids11040094</a></p>
	<p>Authors:
		Stephanie Iris G. Pinto
		Jose G. Vasconcelos
		Alexandre K. Soares
		</p>
	<p>Hydraulic transients in pressurized pipe systems are significantly influenced by the presence of entrapped air, which alters wave propagation through increased compressibility and energy dissipation. Traditional discrete cavity models, such as the Discrete Gas Cavity Model (DGCM), often assume a constant wave celerity, which limits their accuracy under high gas content conditions. This study evaluated different approaches for representing the effects of gas cavities and unsteady friction in closed pipe transients. The work introduces the Adjustable-celerity Gas Cavity Model (AGCM), a formulation that explicitly couples local air volume and pressure to dynamically adjusted celerity values. Two variants are considered, a non-iterative (AGCM.v1) and an iterative approach (AGCM.v2), the latter ensuring consistency between pressure head and celerity at each time step. The models were evaluated through numerical simulations using both experimental datasets and a hypothetical test case with increasing air fractions. Results show that the AGCM was able to represent celerity magnitudes in unsteady flows with large fractions of air. Also, while constant-celerity models perform well under low-air conditions, variable-celerity formulations offer superior consistency in predicting wave amplitudes and celerity dynamics as gas content increases. These findings underscore the importance of dynamic celerity coupling in transient flow modeling and validate the AGCM as a useful approach for transient modeling in conditions with higher air phase fractions.</p>
	]]></content:encoded>

	<dc:title>Evaluating Alternatives for Combined Modeling of Gas Cavities and Unsteady Friction in Closed-Pipe Transients</dc:title>
			<dc:creator>Stephanie Iris G. Pinto</dc:creator>
			<dc:creator>Jose G. Vasconcelos</dc:creator>
			<dc:creator>Alexandre K. Soares</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040094</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-03</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-03</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>94</prism:startingPage>
		<prism:doi>10.3390/fluids11040094</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/94</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/93">

	<title>Fluids, Vol. 11, Pages 93: A Vorticity-Enhanced Physics-Informed Neural Network with Logarithmic Reynolds Embedding</title>
	<link>https://www.mdpi.com/2311-5521/11/4/93</link>
	<description>To improve unified modeling of steady two-dimensional lid-driven cavity flow across a wide range of Reynolds numbers, this study proposes a Vorticity-Enhanced Physics-Informed Neural Network (VE-PINN). The method augments a standard velocity-pressure PINN with a vorticity-transport residual and uses a logarithmic Reynolds-number embedding, log10Re, for multi-regime training. Using CFD benchmark data as supervision and evaluation, we conduct systematic ablation studies on network architecture, loss weighting, sampling density, input embedding, and physical constraint over Re=1000&amp;amp;minus;50000, together with out-of-range extrapolation tests. The results show that the logarithmic Reynolds-number embedding improves cross-regime training stability and reduces the multi-regime mean relative error, while the vorticity-transport constraint improves the reconstruction of velocity fields and secondary vortical structures with only a modest increase in training cost. Further comparisons based on contour fields, centerline velocity profiles, vortex-core locations, and vorticity intensity indicate that VE-PINN provides improved accuracy, physical consistency, and generalization relative to the baseline PINN in the present benchmark. These findings suggest that, for the steady cavity-flow problem considered here, combining logarithmic parameter embedding with derivative-level physical constraint is a practical and effective strategy for parametric PINN modeling.</description>
	<pubDate>2026-04-02</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 93: A Vorticity-Enhanced Physics-Informed Neural Network with Logarithmic Reynolds Embedding</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/93">doi: 10.3390/fluids11040093</a></p>
	<p>Authors:
		Yaxiong Zheng
		Fei Peng
		Zhanzhi Wang
		Jianming Lei
		Shan Pian
		</p>
	<p>To improve unified modeling of steady two-dimensional lid-driven cavity flow across a wide range of Reynolds numbers, this study proposes a Vorticity-Enhanced Physics-Informed Neural Network (VE-PINN). The method augments a standard velocity-pressure PINN with a vorticity-transport residual and uses a logarithmic Reynolds-number embedding, log10Re, for multi-regime training. Using CFD benchmark data as supervision and evaluation, we conduct systematic ablation studies on network architecture, loss weighting, sampling density, input embedding, and physical constraint over Re=1000&amp;amp;minus;50000, together with out-of-range extrapolation tests. The results show that the logarithmic Reynolds-number embedding improves cross-regime training stability and reduces the multi-regime mean relative error, while the vorticity-transport constraint improves the reconstruction of velocity fields and secondary vortical structures with only a modest increase in training cost. Further comparisons based on contour fields, centerline velocity profiles, vortex-core locations, and vorticity intensity indicate that VE-PINN provides improved accuracy, physical consistency, and generalization relative to the baseline PINN in the present benchmark. These findings suggest that, for the steady cavity-flow problem considered here, combining logarithmic parameter embedding with derivative-level physical constraint is a practical and effective strategy for parametric PINN modeling.</p>
	]]></content:encoded>

	<dc:title>A Vorticity-Enhanced Physics-Informed Neural Network with Logarithmic Reynolds Embedding</dc:title>
			<dc:creator>Yaxiong Zheng</dc:creator>
			<dc:creator>Fei Peng</dc:creator>
			<dc:creator>Zhanzhi Wang</dc:creator>
			<dc:creator>Jianming Lei</dc:creator>
			<dc:creator>Shan Pian</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040093</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-04-02</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-04-02</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>93</prism:startingPage>
		<prism:doi>10.3390/fluids11040093</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/93</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/92">

	<title>Fluids, Vol. 11, Pages 92: Hydrodynamic Shielding and Oxidation Suppression in Merging Lazy Plumes</title>
	<link>https://www.mdpi.com/2311-5521/11/4/92</link>
	<description>This paper investigates the combustion dynamics of interacting lazy multi-component gas plumes (i.e., buoyancy-dominated gas releases with a low initial momentum flux), a configuration relevant to coal mining waste emissions. By coupling a three-dimensional large eddy simulation (mesh size of 10&amp;amp;minus;2 m; paralleling with 2048 processors) with detailed chemical kinetics (GRI-Mech 3.0), we analyzed the sensitivity of the flow structure and plume stabilization to the vent spacing of twin hydrogen-rich multi-component gas plumes (H2-CO-CH4-air). The results identified a distinct topological transition. While gas plumes from vents spaced at &amp;amp;delta;/D=5 (&amp;amp;delta; and D are the spacing and width of gas vents, respectively) evolve independently, those at closely spaced sources (&amp;amp;delta;/D=5/4) exhibit rapid coalescence driven by hydrodynamic shielding. This hydrodynamic merging results in a unified column with an effective hydraulic diameter of Deff&amp;amp;asymp;2D. This leads to a significant reduction in the surface-to-volume ratio available for ambient air entrainment, maintaining a coherent combustible-rich core to higher altitudes than isolated-source correlations would predict. However, despite this mass retention, the rapid vertical acceleration of buoyancy-dominated flows induces high strain rates, significantly disrupting the reaction zone structure. These findings establish that, for clustered emission sources, the dispersion hazard is governed by a coupling between hydrodynamic coalescence, which maintains reactant concentration, and finite-rate chemistry, restricting oxidation efficiency. This paper provides critical insights for designing gas capture infrastructure and assessing flammability limits in multi-vent systems.</description>
	<pubDate>2026-03-30</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 92: Hydrodynamic Shielding and Oxidation Suppression in Merging Lazy Plumes</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/92">doi: 10.3390/fluids11040092</a></p>
	<p>Authors:
		Atsuyoshi Sato
		Arata Kioka
		Masami Nakagawa
		Takeshi Tsuji
		</p>
	<p>This paper investigates the combustion dynamics of interacting lazy multi-component gas plumes (i.e., buoyancy-dominated gas releases with a low initial momentum flux), a configuration relevant to coal mining waste emissions. By coupling a three-dimensional large eddy simulation (mesh size of 10&amp;amp;minus;2 m; paralleling with 2048 processors) with detailed chemical kinetics (GRI-Mech 3.0), we analyzed the sensitivity of the flow structure and plume stabilization to the vent spacing of twin hydrogen-rich multi-component gas plumes (H2-CO-CH4-air). The results identified a distinct topological transition. While gas plumes from vents spaced at &amp;amp;delta;/D=5 (&amp;amp;delta; and D are the spacing and width of gas vents, respectively) evolve independently, those at closely spaced sources (&amp;amp;delta;/D=5/4) exhibit rapid coalescence driven by hydrodynamic shielding. This hydrodynamic merging results in a unified column with an effective hydraulic diameter of Deff&amp;amp;asymp;2D. This leads to a significant reduction in the surface-to-volume ratio available for ambient air entrainment, maintaining a coherent combustible-rich core to higher altitudes than isolated-source correlations would predict. However, despite this mass retention, the rapid vertical acceleration of buoyancy-dominated flows induces high strain rates, significantly disrupting the reaction zone structure. These findings establish that, for clustered emission sources, the dispersion hazard is governed by a coupling between hydrodynamic coalescence, which maintains reactant concentration, and finite-rate chemistry, restricting oxidation efficiency. This paper provides critical insights for designing gas capture infrastructure and assessing flammability limits in multi-vent systems.</p>
	]]></content:encoded>

	<dc:title>Hydrodynamic Shielding and Oxidation Suppression in Merging Lazy Plumes</dc:title>
			<dc:creator>Atsuyoshi Sato</dc:creator>
			<dc:creator>Arata Kioka</dc:creator>
			<dc:creator>Masami Nakagawa</dc:creator>
			<dc:creator>Takeshi Tsuji</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040092</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-30</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-30</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>92</prism:startingPage>
		<prism:doi>10.3390/fluids11040092</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/92</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/91">

	<title>Fluids, Vol. 11, Pages 91: Non-Newtonian Flow: Interfacial and Bulk Phenomena</title>
	<link>https://www.mdpi.com/2311-5521/11/4/91</link>
	<description>Nearly all biological fluids and a vast number of non-biological fluids are, to some extent, non-Newtonian, with many also exhibiting viscoelastic responses [...]</description>
	<pubDate>2026-03-29</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 91: Non-Newtonian Flow: Interfacial and Bulk Phenomena</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/91">doi: 10.3390/fluids11040091</a></p>
	<p>Authors:
		Amir H. Hirsa
		</p>
	<p>Nearly all biological fluids and a vast number of non-biological fluids are, to some extent, non-Newtonian, with many also exhibiting viscoelastic responses [...]</p>
	]]></content:encoded>

	<dc:title>Non-Newtonian Flow: Interfacial and Bulk Phenomena</dc:title>
			<dc:creator>Amir H. Hirsa</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040091</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-29</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-29</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Editorial</prism:section>
	<prism:startingPage>91</prism:startingPage>
		<prism:doi>10.3390/fluids11040091</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/91</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/90">

	<title>Fluids, Vol. 11, Pages 90: Experimentally Validated Discrete Phase Model for PM2.5 and PM10 with Numerical Transport Mapping</title>
	<link>https://www.mdpi.com/2311-5521/11/4/90</link>
	<description>Indoor exposure to particulate matter (PM) depends on ventilation-driven transport, yet sensor placement in real rooms is often based on limited point data. This study develops and experimentally validates a transient CFD framework, using RANS airflow coupled with Lagrangian discrete phase tracking, to map PM2.5 and PM10 in a full-scale 2.0 &amp;amp;times; 3.0 &amp;amp;times; 2.5 m bedroom with a fixed, non-oscillating pedestal fan and an open window. Airflow was verified by grid independence and validated against 10-point velocity measurements (RMSE = 0.108 m&amp;amp;middot;s&amp;amp;minus;1). Incense experiments (&amp;amp;asymp;31 min burn) provided PM time series over the first 60 min at 16 locations on two heights; emission rate, burning time, and air-change rate (1.96&amp;amp;ndash;5.39 ACH) were calibrated so that accepted models achieved aggregate R2 &amp;amp;gt; 0.90. Spatial mapping on a 0.5 m grid shows that PM behavior is governed primarily by airflow-defined accumulation pockets rather than by source proximity alone. A near-source region consistently captured strong early-time peaks, whereas remote low-exchange pockets remained elevated during the decay phase. For PM2.5, the most persistent hotspot is a ceiling-adjacent recirculation pocket, while for PM10, gravitational settling shifted the dominant hotspots toward floor-layer, low-velocity regions. An exposure score combining normalized peak and time-averaged concentrations, interpreted together with particle-track persistence metrics, distinguished transiently traversed regions from true retention pockets. The results show that sensor placement should follow the monitoring objective: near-source regions are more responsive to peak events, ceiling pockets are more suitable for persistent PM2.5 monitoring, and floor hotspots are more critical for PM10. No single fixed sensor location adequately represents both particle sizes in the present bedroom and ventilation configuration.</description>
	<pubDate>2026-03-29</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 90: Experimentally Validated Discrete Phase Model for PM2.5 and PM10 with Numerical Transport Mapping</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/90">doi: 10.3390/fluids11040090</a></p>
	<p>Authors:
		Ren Paulo Estaquio
		Ma Kevina Canlas
		Neil Astrologo
		Job Immanuel Encarnacion
		Joshua Agar
		Ken Bryan Fernandez
		Julius Rhoan Lustro
		Joseph Gerard Reyes
		</p>
	<p>Indoor exposure to particulate matter (PM) depends on ventilation-driven transport, yet sensor placement in real rooms is often based on limited point data. This study develops and experimentally validates a transient CFD framework, using RANS airflow coupled with Lagrangian discrete phase tracking, to map PM2.5 and PM10 in a full-scale 2.0 &amp;amp;times; 3.0 &amp;amp;times; 2.5 m bedroom with a fixed, non-oscillating pedestal fan and an open window. Airflow was verified by grid independence and validated against 10-point velocity measurements (RMSE = 0.108 m&amp;amp;middot;s&amp;amp;minus;1). Incense experiments (&amp;amp;asymp;31 min burn) provided PM time series over the first 60 min at 16 locations on two heights; emission rate, burning time, and air-change rate (1.96&amp;amp;ndash;5.39 ACH) were calibrated so that accepted models achieved aggregate R2 &amp;amp;gt; 0.90. Spatial mapping on a 0.5 m grid shows that PM behavior is governed primarily by airflow-defined accumulation pockets rather than by source proximity alone. A near-source region consistently captured strong early-time peaks, whereas remote low-exchange pockets remained elevated during the decay phase. For PM2.5, the most persistent hotspot is a ceiling-adjacent recirculation pocket, while for PM10, gravitational settling shifted the dominant hotspots toward floor-layer, low-velocity regions. An exposure score combining normalized peak and time-averaged concentrations, interpreted together with particle-track persistence metrics, distinguished transiently traversed regions from true retention pockets. The results show that sensor placement should follow the monitoring objective: near-source regions are more responsive to peak events, ceiling pockets are more suitable for persistent PM2.5 monitoring, and floor hotspots are more critical for PM10. No single fixed sensor location adequately represents both particle sizes in the present bedroom and ventilation configuration.</p>
	]]></content:encoded>

	<dc:title>Experimentally Validated Discrete Phase Model for PM2.5 and PM10 with Numerical Transport Mapping</dc:title>
			<dc:creator>Ren Paulo Estaquio</dc:creator>
			<dc:creator>Ma Kevina Canlas</dc:creator>
			<dc:creator>Neil Astrologo</dc:creator>
			<dc:creator>Job Immanuel Encarnacion</dc:creator>
			<dc:creator>Joshua Agar</dc:creator>
			<dc:creator>Ken Bryan Fernandez</dc:creator>
			<dc:creator>Julius Rhoan Lustro</dc:creator>
			<dc:creator>Joseph Gerard Reyes</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040090</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-29</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-29</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>90</prism:startingPage>
		<prism:doi>10.3390/fluids11040090</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/90</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/89">

	<title>Fluids, Vol. 11, Pages 89: Sound Wave Propagation in Binary Gas Mixtures Flowing Through Microchannels According to a BGK-Type Kinetic Model for General Intermolecular Potentials and Maxwell Boundary Conditions</title>
	<link>https://www.mdpi.com/2311-5521/11/4/89</link>
	<description>In this work, we assess the reliability of a new Bhatnagar&amp;amp;ndash;Gross&amp;amp;ndash;Krook (BGK)-type model of the linearized Boltzmann equation for binary gas mixtures by investigating the propagation of high-frequency sound waves in microchannels. In order to take into account the different gas&amp;amp;ndash;wall interaction properties experienced by the mixture components, we solve the kinetic equations assuming Maxwell boundary conditions, with different accommodation coefficients for the two species. Unlike other BGK models existing in the literature, the newly proposed model can describe general intermolecular forces. Therefore, in order to test this ability, we specialize our computations to mixtures with two components of very different masses (disparate-mass gas mixtures like He-Xe), since, in this case, the intermolecular forces play a more significant role compared to mixtures with species of similar masses. Then, we compare the results with those obtained by the McCormack model, which has been shown to correctly reproduce many experimental data.</description>
	<pubDate>2026-03-28</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 89: Sound Wave Propagation in Binary Gas Mixtures Flowing Through Microchannels According to a BGK-Type Kinetic Model for General Intermolecular Potentials and Maxwell Boundary Conditions</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/89">doi: 10.3390/fluids11040089</a></p>
	<p>Authors:
		Silvia Lorenzani
		</p>
	<p>In this work, we assess the reliability of a new Bhatnagar&amp;amp;ndash;Gross&amp;amp;ndash;Krook (BGK)-type model of the linearized Boltzmann equation for binary gas mixtures by investigating the propagation of high-frequency sound waves in microchannels. In order to take into account the different gas&amp;amp;ndash;wall interaction properties experienced by the mixture components, we solve the kinetic equations assuming Maxwell boundary conditions, with different accommodation coefficients for the two species. Unlike other BGK models existing in the literature, the newly proposed model can describe general intermolecular forces. Therefore, in order to test this ability, we specialize our computations to mixtures with two components of very different masses (disparate-mass gas mixtures like He-Xe), since, in this case, the intermolecular forces play a more significant role compared to mixtures with species of similar masses. Then, we compare the results with those obtained by the McCormack model, which has been shown to correctly reproduce many experimental data.</p>
	]]></content:encoded>

	<dc:title>Sound Wave Propagation in Binary Gas Mixtures Flowing Through Microchannels According to a BGK-Type Kinetic Model for General Intermolecular Potentials and Maxwell Boundary Conditions</dc:title>
			<dc:creator>Silvia Lorenzani</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040089</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-28</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-28</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>89</prism:startingPage>
		<prism:doi>10.3390/fluids11040089</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/89</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/88">

	<title>Fluids, Vol. 11, Pages 88: Numerical Study of Shark-Skin Memetic Riblets on the Trailing Vortex and Boundary Layer Flow of the Wind Turbine Airfoil</title>
	<link>https://www.mdpi.com/2311-5521/11/4/88</link>
	<description>Shark skin grooves, known to reduce hydrodynamic drag, have inspired riblet structures for flow control. This study investigates their application to airfoils, where flow separation at high angles of attack (AOA) compromises aerodynamic stability and wind turbine performance. Numerical simulations were conducted using the SST k&amp;amp;ndash;&amp;amp;omega; model in ANSYS Fluent to analyze riblets placed on the suction surface (SS) of an airfoil. The riblets&amp;amp;mdash;oriented perpendicular to the flow&amp;amp;mdash;have a fixed height and width of 1 mm, with total lengths varying from 0.1, 0.2, 0.5, and 0.7 of the chord length. The influence of riblet geometry on trailing-edge (TE) vortex shedding and drag reduction under stall conditions is examined in detail. The results indicate that appropriately sized riblets suppress secondary vortex formation and extend the 2S vortex-shedding regime. Conversely, poorly dimensioned riblets can advance Hopf bifurcation in the wake. Analysis of the transient boundary layer structure reveals that the suppression of vortex shedding is primarily due to riblets attenuating fluid pulsation and Reynolds stresses caused by turbulent bursts.</description>
	<pubDate>2026-03-27</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 88: Numerical Study of Shark-Skin Memetic Riblets on the Trailing Vortex and Boundary Layer Flow of the Wind Turbine Airfoil</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/88">doi: 10.3390/fluids11040088</a></p>
	<p>Authors:
		Xiaopei Yang
		Renzhong Wang
		Bin Zuo
		Boyan Jiang
		</p>
	<p>Shark skin grooves, known to reduce hydrodynamic drag, have inspired riblet structures for flow control. This study investigates their application to airfoils, where flow separation at high angles of attack (AOA) compromises aerodynamic stability and wind turbine performance. Numerical simulations were conducted using the SST k&amp;amp;ndash;&amp;amp;omega; model in ANSYS Fluent to analyze riblets placed on the suction surface (SS) of an airfoil. The riblets&amp;amp;mdash;oriented perpendicular to the flow&amp;amp;mdash;have a fixed height and width of 1 mm, with total lengths varying from 0.1, 0.2, 0.5, and 0.7 of the chord length. The influence of riblet geometry on trailing-edge (TE) vortex shedding and drag reduction under stall conditions is examined in detail. The results indicate that appropriately sized riblets suppress secondary vortex formation and extend the 2S vortex-shedding regime. Conversely, poorly dimensioned riblets can advance Hopf bifurcation in the wake. Analysis of the transient boundary layer structure reveals that the suppression of vortex shedding is primarily due to riblets attenuating fluid pulsation and Reynolds stresses caused by turbulent bursts.</p>
	]]></content:encoded>

	<dc:title>Numerical Study of Shark-Skin Memetic Riblets on the Trailing Vortex and Boundary Layer Flow of the Wind Turbine Airfoil</dc:title>
			<dc:creator>Xiaopei Yang</dc:creator>
			<dc:creator>Renzhong Wang</dc:creator>
			<dc:creator>Bin Zuo</dc:creator>
			<dc:creator>Boyan Jiang</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040088</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-27</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-27</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>88</prism:startingPage>
		<prism:doi>10.3390/fluids11040088</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/88</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/87">

	<title>Fluids, Vol. 11, Pages 87: Flow Mechanism Analysis of Engine Valve Deviation Under Braking Conditions</title>
	<link>https://www.mdpi.com/2311-5521/11/4/87</link>
	<description>The valve serves as the actuating component within the valve mechanism. Under braking conditions, the valve is prone to swaying, which significantly compromises the reliability and service life of the engine. Hence, this paper focuses on researching the deviation characteristics of engine valves. Through a three-dimensional numerical simulation, we analyze the flow field around the valve in the instantaneous states. Our research has revealed that the flow surrounding the valve exhibits a complex multi-vortex structure. Specifically, we observed the evolution pattern of the asymmetric multi-vortex flow along the valve axis within three distinct zones: the asymmetry increase zone, the symmetric development zone, and the asymmetry re-increase zone. The asymmetry increase zone and the asymmetry re-increase zone are located in the curved section and the cylindrical body of the valve, respectively. These zones are the primary contributors to the lateral force acting on the valve, which in turn induces deviation. Based on these analysis results, further research must be conducted on the dynamic characteristics of the flow during valve movement and on optimizing the valve structure through flow control strategies.</description>
	<pubDate>2026-03-27</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 87: Flow Mechanism Analysis of Engine Valve Deviation Under Braking Conditions</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/87">doi: 10.3390/fluids11040087</a></p>
	<p>Authors:
		Wenchao Mo
		Zhancheng Dou
		Qiang Sun
		Zhihang Chen
		</p>
	<p>The valve serves as the actuating component within the valve mechanism. Under braking conditions, the valve is prone to swaying, which significantly compromises the reliability and service life of the engine. Hence, this paper focuses on researching the deviation characteristics of engine valves. Through a three-dimensional numerical simulation, we analyze the flow field around the valve in the instantaneous states. Our research has revealed that the flow surrounding the valve exhibits a complex multi-vortex structure. Specifically, we observed the evolution pattern of the asymmetric multi-vortex flow along the valve axis within three distinct zones: the asymmetry increase zone, the symmetric development zone, and the asymmetry re-increase zone. The asymmetry increase zone and the asymmetry re-increase zone are located in the curved section and the cylindrical body of the valve, respectively. These zones are the primary contributors to the lateral force acting on the valve, which in turn induces deviation. Based on these analysis results, further research must be conducted on the dynamic characteristics of the flow during valve movement and on optimizing the valve structure through flow control strategies.</p>
	]]></content:encoded>

	<dc:title>Flow Mechanism Analysis of Engine Valve Deviation Under Braking Conditions</dc:title>
			<dc:creator>Wenchao Mo</dc:creator>
			<dc:creator>Zhancheng Dou</dc:creator>
			<dc:creator>Qiang Sun</dc:creator>
			<dc:creator>Zhihang Chen</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040087</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-27</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-27</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>87</prism:startingPage>
		<prism:doi>10.3390/fluids11040087</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/87</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/85">

	<title>Fluids, Vol. 11, Pages 85: Optimization of Airflow Field and Experimental Verification for Wheat Cleaning Device Based on CFD-DEM</title>
	<link>https://www.mdpi.com/2311-5521/11/4/85</link>
	<description>To address the issues of high impurity rates and grain loss during the wheat cleaning process, a coupled Computational Fluid Dynamics (CFD) and Discrete Element Method (DEM) approach was employed to investigate the internal airflow field and the fluid&amp;amp;ndash;solid coupling process of the wheat cleaning device. The numerical simulation of the three-dimensional internal flow field is carried out in the high-Reynolds-number turbulent region, and the transient double precision solver based on the pressure&amp;amp;ndash;velocity coupling algorithm is used. The effects of the air inlet velocity and angle on the airflow field distribution and air separation efficiency were analyzed through CFD simulation. Based on this, the structure of the cleaning device was optimized, and the movement characteristics of materials under various wind forces were compared through CFD-DEM coupling simulation. The results showed that the optimal air separation parameters were an air inlet velocity of 10 m/s and an air inlet angle of 20 degrees. Under these conditions, the airflow distribution in the air separation box was uniform, and the impurity separation efficiency reached the highest level. After optimizing the equipment by installing a high-pressure fan, the number of impurities in the wheat collection box under windy conditions was 265, a reduction of 53.8% compared to 573 under windless conditions. Finally, through repeated experiments on the entire machine, it was verified that the impurity rate of the optimized device was 1.722% and the loss rate was 0.622%, which were 0.23% and 0.12% lower than those of the existing equipment, respectively, consistent with the simulation results. This study provides theoretical basis and technical support for the optimization design of wheat cleaning equipment.</description>
	<pubDate>2026-03-26</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 85: Optimization of Airflow Field and Experimental Verification for Wheat Cleaning Device Based on CFD-DEM</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/85">doi: 10.3390/fluids11040085</a></p>
	<p>Authors:
		Chunyan Zhang
		Junrong He
		Sai Yang
		Yinhu Qiao
		Lele Zhou
		Leifeng Dai
		</p>
	<p>To address the issues of high impurity rates and grain loss during the wheat cleaning process, a coupled Computational Fluid Dynamics (CFD) and Discrete Element Method (DEM) approach was employed to investigate the internal airflow field and the fluid&amp;amp;ndash;solid coupling process of the wheat cleaning device. The numerical simulation of the three-dimensional internal flow field is carried out in the high-Reynolds-number turbulent region, and the transient double precision solver based on the pressure&amp;amp;ndash;velocity coupling algorithm is used. The effects of the air inlet velocity and angle on the airflow field distribution and air separation efficiency were analyzed through CFD simulation. Based on this, the structure of the cleaning device was optimized, and the movement characteristics of materials under various wind forces were compared through CFD-DEM coupling simulation. The results showed that the optimal air separation parameters were an air inlet velocity of 10 m/s and an air inlet angle of 20 degrees. Under these conditions, the airflow distribution in the air separation box was uniform, and the impurity separation efficiency reached the highest level. After optimizing the equipment by installing a high-pressure fan, the number of impurities in the wheat collection box under windy conditions was 265, a reduction of 53.8% compared to 573 under windless conditions. Finally, through repeated experiments on the entire machine, it was verified that the impurity rate of the optimized device was 1.722% and the loss rate was 0.622%, which were 0.23% and 0.12% lower than those of the existing equipment, respectively, consistent with the simulation results. This study provides theoretical basis and technical support for the optimization design of wheat cleaning equipment.</p>
	]]></content:encoded>

	<dc:title>Optimization of Airflow Field and Experimental Verification for Wheat Cleaning Device Based on CFD-DEM</dc:title>
			<dc:creator>Chunyan Zhang</dc:creator>
			<dc:creator>Junrong He</dc:creator>
			<dc:creator>Sai Yang</dc:creator>
			<dc:creator>Yinhu Qiao</dc:creator>
			<dc:creator>Lele Zhou</dc:creator>
			<dc:creator>Leifeng Dai</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040085</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-26</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-26</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>85</prism:startingPage>
		<prism:doi>10.3390/fluids11040085</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/85</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/86">

	<title>Fluids, Vol. 11, Pages 86: Rational Design of High-Performance Viscosifying Polymers in Confined Systems via a Machine-Learning-Accelerated Multiscale Framework for Enhanced Hydrocarbon Recovery</title>
	<link>https://www.mdpi.com/2311-5521/11/4/86</link>
	<description>Rational design of high-performance viscosifying polymers is critical for enhancing supercritical CO2 flooding efficiency in enhanced oil recovery (EOR). Traditional experimental and simulation approaches are limited in exploring the vast design space of polymer architecture, flexibility, and intermolecular interactions. This work presents an integrated machine learning (ML) and mesoscopic simulation framework using Dissipative Particle Dynamics (DPD) to accelerate the development of tailored polymeric thickeners. We systematically investigate synergistic effects of linear and branched polymer blends on solvent viscosity under Poiseuille flow, representative of flow in micro-fractures and pore throats. Key molecular descriptors are varied to generate a comprehensive rheological database. This data trains a deep neural network (DNN) surrogate model linking molecular parameters to macroscopic viscosity. The DNN is coupled with gradient ascent optimization for inverse design, enabling rapid virtual screening of thousands of formulations. A focused case study demonstrates that the star-like architectures with associative cores and semi-flexible backbones outperform linear analogs for supercritical CO2 viscosity enhancement. The optimal candidate&amp;amp;mdash;a four-arm star polymer with linear side chains&amp;amp;mdash;was validated by DPD simulation. This multiscale &amp;amp;ldquo;simulation-to-surrogate&amp;amp;rdquo; methodology bridges molecular design with continuum-scale flow behavior, offering a transformative tool for formulating cost-effective, efficient, and sustainable next-generation EOR chemicals.</description>
	<pubDate>2026-03-26</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 86: Rational Design of High-Performance Viscosifying Polymers in Confined Systems via a Machine-Learning-Accelerated Multiscale Framework for Enhanced Hydrocarbon Recovery</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/86">doi: 10.3390/fluids11040086</a></p>
	<p>Authors:
		Arturo Alvarez-Cruz
		Estela Mayoral-Villa
		Alfonso Ramón García-Márquez
		Jaime Klapp
		</p>
	<p>Rational design of high-performance viscosifying polymers is critical for enhancing supercritical CO2 flooding efficiency in enhanced oil recovery (EOR). Traditional experimental and simulation approaches are limited in exploring the vast design space of polymer architecture, flexibility, and intermolecular interactions. This work presents an integrated machine learning (ML) and mesoscopic simulation framework using Dissipative Particle Dynamics (DPD) to accelerate the development of tailored polymeric thickeners. We systematically investigate synergistic effects of linear and branched polymer blends on solvent viscosity under Poiseuille flow, representative of flow in micro-fractures and pore throats. Key molecular descriptors are varied to generate a comprehensive rheological database. This data trains a deep neural network (DNN) surrogate model linking molecular parameters to macroscopic viscosity. The DNN is coupled with gradient ascent optimization for inverse design, enabling rapid virtual screening of thousands of formulations. A focused case study demonstrates that the star-like architectures with associative cores and semi-flexible backbones outperform linear analogs for supercritical CO2 viscosity enhancement. The optimal candidate&amp;amp;mdash;a four-arm star polymer with linear side chains&amp;amp;mdash;was validated by DPD simulation. This multiscale &amp;amp;ldquo;simulation-to-surrogate&amp;amp;rdquo; methodology bridges molecular design with continuum-scale flow behavior, offering a transformative tool for formulating cost-effective, efficient, and sustainable next-generation EOR chemicals.</p>
	]]></content:encoded>

	<dc:title>Rational Design of High-Performance Viscosifying Polymers in Confined Systems via a Machine-Learning-Accelerated Multiscale Framework for Enhanced Hydrocarbon Recovery</dc:title>
			<dc:creator>Arturo Alvarez-Cruz</dc:creator>
			<dc:creator>Estela Mayoral-Villa</dc:creator>
			<dc:creator>Alfonso Ramón García-Márquez</dc:creator>
			<dc:creator>Jaime Klapp</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040086</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-26</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-26</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>86</prism:startingPage>
		<prism:doi>10.3390/fluids11040086</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/86</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/4/84">

	<title>Fluids, Vol. 11, Pages 84: Quantitative Sensitivity Analysis of Key Parameters in Impellers of Vane-Type Mixed-Flow Pumps Under High Gas Content Conditions</title>
	<link>https://www.mdpi.com/2311-5521/11/4/84</link>
	<description>Gas&amp;amp;ndash;liquid multiphase pumps are essential for deep-sea oil and gas production; however, their performance is severely limited under high gas volume fraction (GVF &amp;amp;gt; 30%) conditions due to inefficient energy transfer and flow instability. In this study, a hybrid sensitivity analysis framework combining the Morris screening method and Sobol global sensitivity analysis is developed to quantitatively investigate the effects of impeller geometric parameters on pump performance at a GVF of 80%. Euler&amp;amp;ndash;Euler two-phase CFD simulations coupled with Python-based automated sampling are employed. The results show that the impeller outer diameter, axial length, and blade wrap angle are the three most influential parameters. The impeller outer diameter contributes 35.7% to the pressure rise, while an axial length exceeding 44 mm induces axial backflow and reduces efficiency by 8.2%. A critical wrap angle of 114&amp;amp;deg; is identified for gas&amp;amp;ndash;liquid energy distribution, beyond which large-scale gas vortices intensify flow instability. Based on these findings, a hierarchical optimization strategy is proposed, resulting in a 6.8% improvement in efficiency and a 12.3% increase in pressure rise.</description>
	<pubDate>2026-03-25</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 84: Quantitative Sensitivity Analysis of Key Parameters in Impellers of Vane-Type Mixed-Flow Pumps Under High Gas Content Conditions</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/4/84">doi: 10.3390/fluids11040084</a></p>
	<p>Authors:
		Minghao Zhou
		Guangtai Shi
		Yuanbo Shi
		Peng Li
		</p>
	<p>Gas&amp;amp;ndash;liquid multiphase pumps are essential for deep-sea oil and gas production; however, their performance is severely limited under high gas volume fraction (GVF &amp;amp;gt; 30%) conditions due to inefficient energy transfer and flow instability. In this study, a hybrid sensitivity analysis framework combining the Morris screening method and Sobol global sensitivity analysis is developed to quantitatively investigate the effects of impeller geometric parameters on pump performance at a GVF of 80%. Euler&amp;amp;ndash;Euler two-phase CFD simulations coupled with Python-based automated sampling are employed. The results show that the impeller outer diameter, axial length, and blade wrap angle are the three most influential parameters. The impeller outer diameter contributes 35.7% to the pressure rise, while an axial length exceeding 44 mm induces axial backflow and reduces efficiency by 8.2%. A critical wrap angle of 114&amp;amp;deg; is identified for gas&amp;amp;ndash;liquid energy distribution, beyond which large-scale gas vortices intensify flow instability. Based on these findings, a hierarchical optimization strategy is proposed, resulting in a 6.8% improvement in efficiency and a 12.3% increase in pressure rise.</p>
	]]></content:encoded>

	<dc:title>Quantitative Sensitivity Analysis of Key Parameters in Impellers of Vane-Type Mixed-Flow Pumps Under High Gas Content Conditions</dc:title>
			<dc:creator>Minghao Zhou</dc:creator>
			<dc:creator>Guangtai Shi</dc:creator>
			<dc:creator>Yuanbo Shi</dc:creator>
			<dc:creator>Peng Li</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11040084</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-25</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-25</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>4</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>84</prism:startingPage>
		<prism:doi>10.3390/fluids11040084</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/4/84</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/83">

	<title>Fluids, Vol. 11, Pages 83: Patient-Specific Computational Hemodynamic Modeling of the Right Pulmonary Artery Using CardioMEMS Data: Validation, Simplification, and Sensitivity Analysis</title>
	<link>https://www.mdpi.com/2311-5521/11/3/83</link>
	<description>This study investigates the application of computational hemodynamic modeling, involving both FSI and CFD models, using SimVascular to simulate blood flow in the right pulmonary artery for patient-specific cardiovascular assessment. The artery&amp;amp;rsquo;s three-dimensional geometry was reconstructed from a computed tomography (CT) image, and pressure measurements from a CardioMEMS&amp;amp;trade; device were used as clinical ground truth for validation. To represent the arterial hemodynamics, we initially formulated a fluid&amp;amp;ndash;structure interaction (FSI) approach to capture wall mechanics. However, given the high computational cost of fully patient-specific FSI simulations for routine clinical decision-making, we evaluated the validity of key simplifications by assuming rigid vessel walls coupled with a three-element Windkessel (3WK) model and applying a half-sine inflow waveform derived from the patient&amp;amp;rsquo;s cardiac output. These simplifications yielded results with minimal error: the rigid-wall assumption introduced a 1.1% deviation, while the idealized waveform resulted in a 0.56 mmHg offset. Crucially, while wall rigidity was acceptable, we found that arterial compliance in the boundary conditions is non-negotiable; reducing the model to a pure resistance approach resulted in non-physiological pressures (130 mmHg). A subsequent parametric analysis examined how varying resistance (R) and compliance (C) distinctively alter the pressure waveform morphology. The results underscore the potential of combining remote monitoring data with validated computational simulations to deepen the understanding of cardiovascular dynamics and enhance diagnostic and therapeutic approaches for cardiovascular diseases.</description>
	<pubDate>2026-03-19</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 83: Patient-Specific Computational Hemodynamic Modeling of the Right Pulmonary Artery Using CardioMEMS Data: Validation, Simplification, and Sensitivity Analysis</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/83">doi: 10.3390/fluids11030083</a></p>
	<p>Authors:
		Angélica Casero
		Laura G. Sánchez
		Felicia Alfano
		Pedro Navas
		Juan F. Oteo
		Carlos Arellano-Serrano
		Manuel Gómez-Bueno
		</p>
	<p>This study investigates the application of computational hemodynamic modeling, involving both FSI and CFD models, using SimVascular to simulate blood flow in the right pulmonary artery for patient-specific cardiovascular assessment. The artery&amp;amp;rsquo;s three-dimensional geometry was reconstructed from a computed tomography (CT) image, and pressure measurements from a CardioMEMS&amp;amp;trade; device were used as clinical ground truth for validation. To represent the arterial hemodynamics, we initially formulated a fluid&amp;amp;ndash;structure interaction (FSI) approach to capture wall mechanics. However, given the high computational cost of fully patient-specific FSI simulations for routine clinical decision-making, we evaluated the validity of key simplifications by assuming rigid vessel walls coupled with a three-element Windkessel (3WK) model and applying a half-sine inflow waveform derived from the patient&amp;amp;rsquo;s cardiac output. These simplifications yielded results with minimal error: the rigid-wall assumption introduced a 1.1% deviation, while the idealized waveform resulted in a 0.56 mmHg offset. Crucially, while wall rigidity was acceptable, we found that arterial compliance in the boundary conditions is non-negotiable; reducing the model to a pure resistance approach resulted in non-physiological pressures (130 mmHg). A subsequent parametric analysis examined how varying resistance (R) and compliance (C) distinctively alter the pressure waveform morphology. The results underscore the potential of combining remote monitoring data with validated computational simulations to deepen the understanding of cardiovascular dynamics and enhance diagnostic and therapeutic approaches for cardiovascular diseases.</p>
	]]></content:encoded>

	<dc:title>Patient-Specific Computational Hemodynamic Modeling of the Right Pulmonary Artery Using CardioMEMS Data: Validation, Simplification, and Sensitivity Analysis</dc:title>
			<dc:creator>Angélica Casero</dc:creator>
			<dc:creator>Laura G. Sánchez</dc:creator>
			<dc:creator>Felicia Alfano</dc:creator>
			<dc:creator>Pedro Navas</dc:creator>
			<dc:creator>Juan F. Oteo</dc:creator>
			<dc:creator>Carlos Arellano-Serrano</dc:creator>
			<dc:creator>Manuel Gómez-Bueno</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030083</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-19</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-19</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>83</prism:startingPage>
		<prism:doi>10.3390/fluids11030083</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/83</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/82">

	<title>Fluids, Vol. 11, Pages 82: Deposition Mechanisms of Suspended Sediment in an Estuarine Artificial Lake: A Case Study of the Jiaojiang Estuary</title>
	<link>https://www.mdpi.com/2311-5521/11/3/82</link>
	<description>Artificial seawater lakes constructed in estuarine environments are highly susceptible to the intrusion of water containing high concentrations of suspended sediment, which can degrade water quality and threaten ecosystem stability. To clarify the settling mechanisms and sedimentation efficiency under high-turbidity conditions, this study investigated the Baishawan Artificial Lake in the Jiaojiang Estuary, eastern China, through field observations, controlled still-water sedimentation experiments, and a multi-particle size sedimentation efficiency model. Field measurements revealed significant spatiotemporal variability in suspended sediment concentration (SSC), with higher SSC during spring tides than neap tides and a spatial gradient decreasing from the near-estuary zone to the artificial lake and offshore waters. Grain-size analysis showed that suspended sediment was dominated by clay and silt (&amp;amp;gt;98%). Laboratory experiments indicated a two-stage settling process characterized by rapid initial sedimentation followed by gradual stabilization; under high concentration (1.32 kg/m3), SSC decreased by about 85% within 40 min due to concentration-enhanced flocculation, whereas under low-concentration conditions (0.24 kg/m3) approximately 14 h were required to reach the target concentration of 0.01 kg/m3. Model validation demonstrated that the multi-component sedimentation model effectively reproduced the temporal attenuation of SSC. Model application further suggested that when the initial SSC was 0.70 kg/m3 and the water depth was 5.7 m, the sedimentation tank could reduce the SSC to 0.01 kg/m3 within about 16&amp;amp;ndash;17 h, with an estimated annual sedimentation volume of ~65,000 m3 and a recommended dredging interval of five years. These results provide quantitative guidance for sedimentation tank operation and sediment management in estuarine artificial lakes and other high-turbidity coastal environments.</description>
	<pubDate>2026-03-17</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 82: Deposition Mechanisms of Suspended Sediment in an Estuarine Artificial Lake: A Case Study of the Jiaojiang Estuary</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/82">doi: 10.3390/fluids11030082</a></p>
	<p>Authors:
		Lele Wang
		Xiaoran Wei
		Yu Han
		Shichang Huang
		Huamin Zhou
		Maoming Sun
		Wenlong Cheng
		Yun Chen
		</p>
	<p>Artificial seawater lakes constructed in estuarine environments are highly susceptible to the intrusion of water containing high concentrations of suspended sediment, which can degrade water quality and threaten ecosystem stability. To clarify the settling mechanisms and sedimentation efficiency under high-turbidity conditions, this study investigated the Baishawan Artificial Lake in the Jiaojiang Estuary, eastern China, through field observations, controlled still-water sedimentation experiments, and a multi-particle size sedimentation efficiency model. Field measurements revealed significant spatiotemporal variability in suspended sediment concentration (SSC), with higher SSC during spring tides than neap tides and a spatial gradient decreasing from the near-estuary zone to the artificial lake and offshore waters. Grain-size analysis showed that suspended sediment was dominated by clay and silt (&amp;amp;gt;98%). Laboratory experiments indicated a two-stage settling process characterized by rapid initial sedimentation followed by gradual stabilization; under high concentration (1.32 kg/m3), SSC decreased by about 85% within 40 min due to concentration-enhanced flocculation, whereas under low-concentration conditions (0.24 kg/m3) approximately 14 h were required to reach the target concentration of 0.01 kg/m3. Model validation demonstrated that the multi-component sedimentation model effectively reproduced the temporal attenuation of SSC. Model application further suggested that when the initial SSC was 0.70 kg/m3 and the water depth was 5.7 m, the sedimentation tank could reduce the SSC to 0.01 kg/m3 within about 16&amp;amp;ndash;17 h, with an estimated annual sedimentation volume of ~65,000 m3 and a recommended dredging interval of five years. These results provide quantitative guidance for sedimentation tank operation and sediment management in estuarine artificial lakes and other high-turbidity coastal environments.</p>
	]]></content:encoded>

	<dc:title>Deposition Mechanisms of Suspended Sediment in an Estuarine Artificial Lake: A Case Study of the Jiaojiang Estuary</dc:title>
			<dc:creator>Lele Wang</dc:creator>
			<dc:creator>Xiaoran Wei</dc:creator>
			<dc:creator>Yu Han</dc:creator>
			<dc:creator>Shichang Huang</dc:creator>
			<dc:creator>Huamin Zhou</dc:creator>
			<dc:creator>Maoming Sun</dc:creator>
			<dc:creator>Wenlong Cheng</dc:creator>
			<dc:creator>Yun Chen</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030082</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-17</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-17</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>82</prism:startingPage>
		<prism:doi>10.3390/fluids11030082</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/82</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/81">

	<title>Fluids, Vol. 11, Pages 81: Machine Learning for Fluid-Agnostic Laminar Heat Transfer Predictions Under Supercritical Conditions</title>
	<link>https://www.mdpi.com/2311-5521/11/3/81</link>
	<description>Machine learning was employed to make fluid agnostic laminar heat transfer prediction in supercritical conditions, encompassing three fluids (sCO2, sH2O, sC10H22) representing a wide range of operating conditions. High-fidelity training data, consisting of both non-dimensional and dimensional (operating parameter) as inputs and Nu and Twall as outputs, were generated from grid-converged, steady-state, computational fluid dynamic (CFD) simulations. The Random Forest (RF) algorithm outperformed the artificial neural networks (ANNs) across all scenarios on the small multi-fluid dataset (~1600 data points) employed during the training process. When using non-dimensional parameters as inputs, Nu prediction fidelities were better than Twall predictions for both ML algorithms across both horizontal and vertical configurations. The RF model trained on data from a specific flow configuration (horizontal/vertical) could predict Twall within an accuracy of +/&amp;amp;minus;1% with dimensional, operational parameters as inputs while being agnostic to the working fluid. Furthermore, by including the gravity vector as an additional variable during the training process, the RF model could predict Twall accurately in a mixed, multi-fluid dataset containing data from both horizontal and vertical configurations.</description>
	<pubDate>2026-03-16</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 81: Machine Learning for Fluid-Agnostic Laminar Heat Transfer Predictions Under Supercritical Conditions</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/81">doi: 10.3390/fluids11030081</a></p>
	<p>Authors:
		Luke Holtshouser
		Gautham Krishnamoorthy
		Krishnamoorthy Viswanathan
		</p>
	<p>Machine learning was employed to make fluid agnostic laminar heat transfer prediction in supercritical conditions, encompassing three fluids (sCO2, sH2O, sC10H22) representing a wide range of operating conditions. High-fidelity training data, consisting of both non-dimensional and dimensional (operating parameter) as inputs and Nu and Twall as outputs, were generated from grid-converged, steady-state, computational fluid dynamic (CFD) simulations. The Random Forest (RF) algorithm outperformed the artificial neural networks (ANNs) across all scenarios on the small multi-fluid dataset (~1600 data points) employed during the training process. When using non-dimensional parameters as inputs, Nu prediction fidelities were better than Twall predictions for both ML algorithms across both horizontal and vertical configurations. The RF model trained on data from a specific flow configuration (horizontal/vertical) could predict Twall within an accuracy of +/&amp;amp;minus;1% with dimensional, operational parameters as inputs while being agnostic to the working fluid. Furthermore, by including the gravity vector as an additional variable during the training process, the RF model could predict Twall accurately in a mixed, multi-fluid dataset containing data from both horizontal and vertical configurations.</p>
	]]></content:encoded>

	<dc:title>Machine Learning for Fluid-Agnostic Laminar Heat Transfer Predictions Under Supercritical Conditions</dc:title>
			<dc:creator>Luke Holtshouser</dc:creator>
			<dc:creator>Gautham Krishnamoorthy</dc:creator>
			<dc:creator>Krishnamoorthy Viswanathan</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030081</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-16</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-16</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>81</prism:startingPage>
		<prism:doi>10.3390/fluids11030081</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/81</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/80">

	<title>Fluids, Vol. 11, Pages 80: Design and Characterization of a Bench-Top Ludwieg Tube for Aerodynamic Measurements via Simultaneous Quantification of Mach Number and Velocity</title>
	<link>https://www.mdpi.com/2311-5521/11/3/80</link>
	<description>This article presents the design and detailed characterization of a new supersonic wind tunnel at the Aerospace Laboratory for Lasers, ElectroMagnetics, and Optics of Texas A&amp;amp;amp;M University, tailored for optical diagnostic development and sub-scale fundamental compressible fluid dynamics research. A Ludwieg tube tunnel architecture was selected due to its robustness, versatility, and low operational costs. The tunnel consists of a 50-foot-long driver tube constructed from modular Tri-Clamp spools, a Mach 4 nozzle with 3 in. exit diameter configured as a free jet, and a fast-acting valve with 14 ms opening time for high-duty-cycle operation. Such construction proved to be a robust, compact, and affordable solution for academic applications. Characterization methods consisted of simultaneous high-speed dot-schlieren, total and static pressure measurements, and femtosecond laser electronic excitation tagging. Average flow velocity for the first steady-state test time was measured via FLEET at (668.0 &amp;amp;plusmn; 5.7) m/s. The Mach number was calculated based on the angles of the attached oblique shocks formed near the 30&amp;amp;deg; cone model. Calculated Mach number was repeatable from run to run and had small oscillations near the average value of 3.96 &amp;amp;plusmn; 0.03. Based on the simultaneously measured velocity and Mach number, the static temperature was calculated to be between (68.6 &amp;amp;plusmn; 0.3) K and (66.3 &amp;amp;plusmn; 0.3) K throughout the 400 ms test time, completely defining the thermodynamic state of the generated freestream flow.</description>
	<pubDate>2026-03-15</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 80: Design and Characterization of a Bench-Top Ludwieg Tube for Aerodynamic Measurements via Simultaneous Quantification of Mach Number and Velocity</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/80">doi: 10.3390/fluids11030080</a></p>
	<p>Authors:
		Boris S. Leonov
		Richard Q. Binzley
		Nathan G. Phillips
		Roman Rosser
		Farhan Siddiqui
		Arthur Dogariu
		Richard B. Miles
		</p>
	<p>This article presents the design and detailed characterization of a new supersonic wind tunnel at the Aerospace Laboratory for Lasers, ElectroMagnetics, and Optics of Texas A&amp;amp;amp;M University, tailored for optical diagnostic development and sub-scale fundamental compressible fluid dynamics research. A Ludwieg tube tunnel architecture was selected due to its robustness, versatility, and low operational costs. The tunnel consists of a 50-foot-long driver tube constructed from modular Tri-Clamp spools, a Mach 4 nozzle with 3 in. exit diameter configured as a free jet, and a fast-acting valve with 14 ms opening time for high-duty-cycle operation. Such construction proved to be a robust, compact, and affordable solution for academic applications. Characterization methods consisted of simultaneous high-speed dot-schlieren, total and static pressure measurements, and femtosecond laser electronic excitation tagging. Average flow velocity for the first steady-state test time was measured via FLEET at (668.0 &amp;amp;plusmn; 5.7) m/s. The Mach number was calculated based on the angles of the attached oblique shocks formed near the 30&amp;amp;deg; cone model. Calculated Mach number was repeatable from run to run and had small oscillations near the average value of 3.96 &amp;amp;plusmn; 0.03. Based on the simultaneously measured velocity and Mach number, the static temperature was calculated to be between (68.6 &amp;amp;plusmn; 0.3) K and (66.3 &amp;amp;plusmn; 0.3) K throughout the 400 ms test time, completely defining the thermodynamic state of the generated freestream flow.</p>
	]]></content:encoded>

	<dc:title>Design and Characterization of a Bench-Top Ludwieg Tube for Aerodynamic Measurements via Simultaneous Quantification of Mach Number and Velocity</dc:title>
			<dc:creator>Boris S. Leonov</dc:creator>
			<dc:creator>Richard Q. Binzley</dc:creator>
			<dc:creator>Nathan G. Phillips</dc:creator>
			<dc:creator>Roman Rosser</dc:creator>
			<dc:creator>Farhan Siddiqui</dc:creator>
			<dc:creator>Arthur Dogariu</dc:creator>
			<dc:creator>Richard B. Miles</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030080</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-15</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-15</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>80</prism:startingPage>
		<prism:doi>10.3390/fluids11030080</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/80</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/79">

	<title>Fluids, Vol. 11, Pages 79: A Compact-Stencil Wetting Boundary Condition for Three-Dimensional Curved Surfaces in a Phase-Field Lattice Boltzmann Method</title>
	<link>https://www.mdpi.com/2311-5521/11/3/79</link>
	<description>Accurate numerical reproduction of contact line dynamics on three-dimensional curved solid surfaces remains a challenging issue in multiphase flow simulations. In this study, a wetting boundary condition applicable to curved surfaces is developed within a three-dimensional phase-field lattice Boltzmann framework. The proposed method extends an existing curved-surface wetting model and focuses on improving the evaluation of interface normals and order-parameter gradients on Cartesian lattices, while preserving the compact computational stencils and efficiency inherent to the lattice Boltzmann method. Three-dimensional simulations of liquid spreading on a concave spherical surface and droplet spreading on a convex solid sphere are performed over a wide range of prescribed contact angles. The results show that the proposed method eliminates nonphysical behaviors observed with conventional staircase-based boundary conditions, such as droplet sliding along the solid surface and droplet detachment into the surrounding gas phase. In the convex spherical surface cases, the droplet height converges stably to equilibrium through damped oscillations, and the equilibrium droplet shapes show good agreement with theoretical predictions derived from geometric considerations under zero-gravity conditions over a broad range of contact angles. These results demonstrate that the proposed wetting boundary condition can accurately reproduce wetting phenomena on three-dimensional curved solid surfaces.</description>
	<pubDate>2026-03-14</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 79: A Compact-Stencil Wetting Boundary Condition for Three-Dimensional Curved Surfaces in a Phase-Field Lattice Boltzmann Method</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/79">doi: 10.3390/fluids11030079</a></p>
	<p>Authors:
		Makoto Sugimoto
		Masayuki Kaneda
		Kazuhiko Suga
		Masaya Shigeta
		</p>
	<p>Accurate numerical reproduction of contact line dynamics on three-dimensional curved solid surfaces remains a challenging issue in multiphase flow simulations. In this study, a wetting boundary condition applicable to curved surfaces is developed within a three-dimensional phase-field lattice Boltzmann framework. The proposed method extends an existing curved-surface wetting model and focuses on improving the evaluation of interface normals and order-parameter gradients on Cartesian lattices, while preserving the compact computational stencils and efficiency inherent to the lattice Boltzmann method. Three-dimensional simulations of liquid spreading on a concave spherical surface and droplet spreading on a convex solid sphere are performed over a wide range of prescribed contact angles. The results show that the proposed method eliminates nonphysical behaviors observed with conventional staircase-based boundary conditions, such as droplet sliding along the solid surface and droplet detachment into the surrounding gas phase. In the convex spherical surface cases, the droplet height converges stably to equilibrium through damped oscillations, and the equilibrium droplet shapes show good agreement with theoretical predictions derived from geometric considerations under zero-gravity conditions over a broad range of contact angles. These results demonstrate that the proposed wetting boundary condition can accurately reproduce wetting phenomena on three-dimensional curved solid surfaces.</p>
	]]></content:encoded>

	<dc:title>A Compact-Stencil Wetting Boundary Condition for Three-Dimensional Curved Surfaces in a Phase-Field Lattice Boltzmann Method</dc:title>
			<dc:creator>Makoto Sugimoto</dc:creator>
			<dc:creator>Masayuki Kaneda</dc:creator>
			<dc:creator>Kazuhiko Suga</dc:creator>
			<dc:creator>Masaya Shigeta</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030079</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-14</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-14</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>79</prism:startingPage>
		<prism:doi>10.3390/fluids11030079</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/79</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/78">

	<title>Fluids, Vol. 11, Pages 78: Empirical Energy Dissipation Model for Variable-Slope Three-Section Stepped Spillways Validated Through Dimensional Analysis and CFD Simulation</title>
	<link>https://www.mdpi.com/2311-5521/11/3/78</link>
	<description>Energy dissipation in stepped weirs depends on the complex interaction between geometry, flow regime, and surface aeration. The research proposes a dimensionless empirical model (RE3T) to predict the overall energy dissipation in three-section stepped weirs with variable slopes. The formulation integrates dimensional analysis based on the Vaschy&amp;amp;ndash;Buckingham theorem, controlled physical experimentation, and three-dimensional numerical simulations using CFD employing the RANS&amp;amp;ndash;SST turbulence model implemented in ANSYS CFX. Eighteen numerical simulations were performed covering seven geometric configurations and four hydraulic inlet conditions, covering slug, transitional, and skimming flow regimes. The CFD model was previously validated by comparison with a physical scale model, obtaining a discrepancy of only 0.38% in relative energy dissipation. The validated dataset was then used to calibrate an empirical multiplicative correlation composed of eight dimensionless groups associated with sectional slopes, number of steps, overall geometric ratio, and upstream Froude number. The proposed model achieved a coefficient of determination R2 = 0.81, with relative errors generally less than 1% and a maximum deviation of 2.34%. The statistical indicators (RMSE, MAE, and bias) confirm the absence of significant systematic trends within the defined domain of validity. The results show that the Froude number and the slopes of the sections are the variables with the greatest influence on overall dissipation. The RE3T formulation is a physically consistent and computationally efficient predictive tool for the design and analysis of stepped weirs with variable slopes, extending the scope of traditional correlations developed for uniform slopes.</description>
	<pubDate>2026-03-13</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 78: Empirical Energy Dissipation Model for Variable-Slope Three-Section Stepped Spillways Validated Through Dimensional Analysis and CFD Simulation</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/78">doi: 10.3390/fluids11030078</a></p>
	<p>Authors:
		Luis Antonio Yataco-Pastor
		Ana Cristina Ybaceta-Valdivia
		Yoisdel Castillo Alvarez
		Reinier Jiménez Borges
		Luis Angel Iturralde Carrera
		José R. García-Martínez
		Juvenal Rodríguez-Reséndiz
		</p>
	<p>Energy dissipation in stepped weirs depends on the complex interaction between geometry, flow regime, and surface aeration. The research proposes a dimensionless empirical model (RE3T) to predict the overall energy dissipation in three-section stepped weirs with variable slopes. The formulation integrates dimensional analysis based on the Vaschy&amp;amp;ndash;Buckingham theorem, controlled physical experimentation, and three-dimensional numerical simulations using CFD employing the RANS&amp;amp;ndash;SST turbulence model implemented in ANSYS CFX. Eighteen numerical simulations were performed covering seven geometric configurations and four hydraulic inlet conditions, covering slug, transitional, and skimming flow regimes. The CFD model was previously validated by comparison with a physical scale model, obtaining a discrepancy of only 0.38% in relative energy dissipation. The validated dataset was then used to calibrate an empirical multiplicative correlation composed of eight dimensionless groups associated with sectional slopes, number of steps, overall geometric ratio, and upstream Froude number. The proposed model achieved a coefficient of determination R2 = 0.81, with relative errors generally less than 1% and a maximum deviation of 2.34%. The statistical indicators (RMSE, MAE, and bias) confirm the absence of significant systematic trends within the defined domain of validity. The results show that the Froude number and the slopes of the sections are the variables with the greatest influence on overall dissipation. The RE3T formulation is a physically consistent and computationally efficient predictive tool for the design and analysis of stepped weirs with variable slopes, extending the scope of traditional correlations developed for uniform slopes.</p>
	]]></content:encoded>

	<dc:title>Empirical Energy Dissipation Model for Variable-Slope Three-Section Stepped Spillways Validated Through Dimensional Analysis and CFD Simulation</dc:title>
			<dc:creator>Luis Antonio Yataco-Pastor</dc:creator>
			<dc:creator>Ana Cristina Ybaceta-Valdivia</dc:creator>
			<dc:creator>Yoisdel Castillo Alvarez</dc:creator>
			<dc:creator>Reinier Jiménez Borges</dc:creator>
			<dc:creator>Luis Angel Iturralde Carrera</dc:creator>
			<dc:creator>José R. García-Martínez</dc:creator>
			<dc:creator>Juvenal Rodríguez-Reséndiz</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030078</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-13</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-13</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>78</prism:startingPage>
		<prism:doi>10.3390/fluids11030078</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/78</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/77">

	<title>Fluids, Vol. 11, Pages 77: Sediment Erosion of a Centrifugal Pump During Startup and Shutdown Processes Considering of Transient Flow in Pump Station</title>
	<link>https://www.mdpi.com/2311-5521/11/3/77</link>
	<description>This study employed the Euler&amp;amp;ndash;Lagrange method and the Oka erosion model to numerically simulate sediment erosion in a centrifugal pump during the startup and shutdown processes. With a sediment particle size of 0.25 mm and a concentration of 0.135 kg/m3, the erosion distribution characteristics were analyzed considering the transient flow in the pump station. The results reveal that the impeller suffers the most severe erosion, and the erosion area is affected by the flow rate. At high flow rates, because of inertial and centrifugal forces, erosion concentrates near the shroud at the blade outlet. At low flow rates, vortices generated within the impeller passages cause particles to impact the mid-section of the blades, resulting in erosion in that area. In the inlet section, erosion primarily occurs on the outer wall surface with a relatively low severity at high flow rates, while vortices that occur at the outlet under low flow rates intensify localized erosion. Furthermore, owing to the hysteresis effect of the flow, the erosion during the startup process is more severe than during the shutdown process. In the fixed guide vane zone, at high flow rates, erosion is mainly concentrated in the leading edge and near the covers. At low flow rates, vortices generated between the fixed guide vanes lead to particle impacts on the vane surfaces near the inlet, causing severe localized erosion in this area. In the volute, erosion exhibits a spiral distribution pattern at high flow rates. When the flow rate changes rapidly, the flow field around the tongue region becomes unstable, inducing local erosion there.</description>
	<pubDate>2026-03-13</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 77: Sediment Erosion of a Centrifugal Pump During Startup and Shutdown Processes Considering of Transient Flow in Pump Station</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/77">doi: 10.3390/fluids11030077</a></p>
	<p>Authors:
		Weiguo Zhao
		Yahui Fan
		Honggang Fan
		</p>
	<p>This study employed the Euler&amp;amp;ndash;Lagrange method and the Oka erosion model to numerically simulate sediment erosion in a centrifugal pump during the startup and shutdown processes. With a sediment particle size of 0.25 mm and a concentration of 0.135 kg/m3, the erosion distribution characteristics were analyzed considering the transient flow in the pump station. The results reveal that the impeller suffers the most severe erosion, and the erosion area is affected by the flow rate. At high flow rates, because of inertial and centrifugal forces, erosion concentrates near the shroud at the blade outlet. At low flow rates, vortices generated within the impeller passages cause particles to impact the mid-section of the blades, resulting in erosion in that area. In the inlet section, erosion primarily occurs on the outer wall surface with a relatively low severity at high flow rates, while vortices that occur at the outlet under low flow rates intensify localized erosion. Furthermore, owing to the hysteresis effect of the flow, the erosion during the startup process is more severe than during the shutdown process. In the fixed guide vane zone, at high flow rates, erosion is mainly concentrated in the leading edge and near the covers. At low flow rates, vortices generated between the fixed guide vanes lead to particle impacts on the vane surfaces near the inlet, causing severe localized erosion in this area. In the volute, erosion exhibits a spiral distribution pattern at high flow rates. When the flow rate changes rapidly, the flow field around the tongue region becomes unstable, inducing local erosion there.</p>
	]]></content:encoded>

	<dc:title>Sediment Erosion of a Centrifugal Pump During Startup and Shutdown Processes Considering of Transient Flow in Pump Station</dc:title>
			<dc:creator>Weiguo Zhao</dc:creator>
			<dc:creator>Yahui Fan</dc:creator>
			<dc:creator>Honggang Fan</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030077</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-13</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-13</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>77</prism:startingPage>
		<prism:doi>10.3390/fluids11030077</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/77</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/76">

	<title>Fluids, Vol. 11, Pages 76: Parametrization of Subgrid Scales in Long-Term Simulations of the Shallow-Water Equations Using Machine Learning and Convex Limiting</title>
	<link>https://www.mdpi.com/2311-5521/11/3/76</link>
	<description>We present a method for parametrizing sub-grid processes in the shallow water equations. We define coarse variables and local spatial averages and use a feed-forward neural network to learn sub-grid fluxes. Our method results in a local parametrization that uses a four-point computational stencil, which has several advantages over globally coupled parametrizations. We demonstrate numerically that our method improves energy balance in long-term turbulent simulations and also accurately reproduces individual solutions. The long-term simulations refer to numerical studies where a fluid flow is simulated over a duration long enough to reach a statistical steady state. The neural network parametrization can be easily combined with flux limiting to reduce oscillations near shocks. More importantly, our method provides reliable parametrizations, even in dynamical regimes that are not included in the training data.</description>
	<pubDate>2026-03-12</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 76: Parametrization of Subgrid Scales in Long-Term Simulations of the Shallow-Water Equations Using Machine Learning and Convex Limiting</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/76">doi: 10.3390/fluids11030076</a></p>
	<p>Authors:
		Md Amran Hossan Mojamder
		Zhihang Xu
		Min Wang
		Ilya Timofeyev
		</p>
	<p>We present a method for parametrizing sub-grid processes in the shallow water equations. We define coarse variables and local spatial averages and use a feed-forward neural network to learn sub-grid fluxes. Our method results in a local parametrization that uses a four-point computational stencil, which has several advantages over globally coupled parametrizations. We demonstrate numerically that our method improves energy balance in long-term turbulent simulations and also accurately reproduces individual solutions. The long-term simulations refer to numerical studies where a fluid flow is simulated over a duration long enough to reach a statistical steady state. The neural network parametrization can be easily combined with flux limiting to reduce oscillations near shocks. More importantly, our method provides reliable parametrizations, even in dynamical regimes that are not included in the training data.</p>
	]]></content:encoded>

	<dc:title>Parametrization of Subgrid Scales in Long-Term Simulations of the Shallow-Water Equations Using Machine Learning and Convex Limiting</dc:title>
			<dc:creator>Md Amran Hossan Mojamder</dc:creator>
			<dc:creator>Zhihang Xu</dc:creator>
			<dc:creator>Min Wang</dc:creator>
			<dc:creator>Ilya Timofeyev</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030076</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-12</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-12</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>76</prism:startingPage>
		<prism:doi>10.3390/fluids11030076</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/76</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/75">

	<title>Fluids, Vol. 11, Pages 75: Vortex Formation in Axial Stirring Systems Under the Influence of Baffle Geometry and Number</title>
	<link>https://www.mdpi.com/2311-5521/11/3/75</link>
	<description>In stirred tank reactors, especially without using baffles, the liquid surface can deform, which in stirring technology is referred to a vortex. These vortices can be advantageous for some mixing tasks, such as obtaining emulsions, they can also impair a consistent product quality. Therefore, it is important for the production and process industry, to know whether a vortex occurs or not. Prediction is only possible with an outdated dimensionless baffle index and research on vortex formation with baffles is limited. In this study, two industrially important axial stirring systems&amp;amp;mdash;Propeller and Pitched-blade turbine&amp;amp;mdash;with different baffle geometries (rectangular, cylindrical, triangular) and numbers are assessed in regard to power input, vortex characteristics (depth, width, volume) and baffle state prediction. Power is recorded using strain gauges, while vortices are evaluated using an optical image evaluation method. The final vortex result is made dimensionless, accessible to the industry to enable improved predictions about the size of the vortices on an industrial scale in order to make the stirred tanks more economical and sustainable. Furthermore, an initial improvement of the baffle index for the investigated stirrers is given, because the original index incorrectly predicts the baffle state in 12.5% of cases.</description>
	<pubDate>2026-03-11</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 75: Vortex Formation in Axial Stirring Systems Under the Influence of Baffle Geometry and Number</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/75">doi: 10.3390/fluids11030075</a></p>
	<p>Authors:
		Laura Lenters
		Mathias Ulbricht
		Heyko Jürgen Schultz
		</p>
	<p>In stirred tank reactors, especially without using baffles, the liquid surface can deform, which in stirring technology is referred to a vortex. These vortices can be advantageous for some mixing tasks, such as obtaining emulsions, they can also impair a consistent product quality. Therefore, it is important for the production and process industry, to know whether a vortex occurs or not. Prediction is only possible with an outdated dimensionless baffle index and research on vortex formation with baffles is limited. In this study, two industrially important axial stirring systems&amp;amp;mdash;Propeller and Pitched-blade turbine&amp;amp;mdash;with different baffle geometries (rectangular, cylindrical, triangular) and numbers are assessed in regard to power input, vortex characteristics (depth, width, volume) and baffle state prediction. Power is recorded using strain gauges, while vortices are evaluated using an optical image evaluation method. The final vortex result is made dimensionless, accessible to the industry to enable improved predictions about the size of the vortices on an industrial scale in order to make the stirred tanks more economical and sustainable. Furthermore, an initial improvement of the baffle index for the investigated stirrers is given, because the original index incorrectly predicts the baffle state in 12.5% of cases.</p>
	]]></content:encoded>

	<dc:title>Vortex Formation in Axial Stirring Systems Under the Influence of Baffle Geometry and Number</dc:title>
			<dc:creator>Laura Lenters</dc:creator>
			<dc:creator>Mathias Ulbricht</dc:creator>
			<dc:creator>Heyko Jürgen Schultz</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030075</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-11</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-11</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>75</prism:startingPage>
		<prism:doi>10.3390/fluids11030075</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/75</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/74">

	<title>Fluids, Vol. 11, Pages 74: A Numerical Study of Frost Formation from Humid Air on Horizontal Cold Plate Surfaces Under Natural Convection</title>
	<link>https://www.mdpi.com/2311-5521/11/3/74</link>
	<description>Based on a previously proposed dimensionless phase-change-driven frosting model, this study numerically investigates frost formation on a horizontal cold plate under natural convection using a Eulerian multiphase framework coupled with species transport. The model is validated against experimental data, showing errors within 5&amp;amp;ndash;18%; the maximum deviation of 17.07% occurs at Tw = &amp;amp;minus;25 &amp;amp;deg;C, possibly due to increased experimental uncertainty at very low temperatures. Results demonstrate that lower cold plate temperatures lead to greater frost thickness and higher ice volume fraction. A key physical insight is that under natural convection, local convective circulation causes enhanced frosting at the plate edges, resulting in spatial non-uniformity in both thickness and density. The study covers cold plate temperatures from &amp;amp;minus;10 &amp;amp;deg;C to &amp;amp;minus;25 &amp;amp;deg;C at relative humidity of 60%. The frost growth rate and density at both ends of the cold plate exceed those in the central region, and this difference intensifies with decreasing temperature. Within the frost layer, humid air velocity is nearly zero, while maximum velocity occurs near the sides due to natural convection. The simulation results show good agreement with experimental data, confirming the model&amp;amp;rsquo;s reliability for natural convection scenarios.</description>
	<pubDate>2026-03-10</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 74: A Numerical Study of Frost Formation from Humid Air on Horizontal Cold Plate Surfaces Under Natural Convection</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/74">doi: 10.3390/fluids11030074</a></p>
	<p>Authors:
		Zhengsheng Yang
		Fan Shi
		Jiawang Li
		Shukun Liu
		</p>
	<p>Based on a previously proposed dimensionless phase-change-driven frosting model, this study numerically investigates frost formation on a horizontal cold plate under natural convection using a Eulerian multiphase framework coupled with species transport. The model is validated against experimental data, showing errors within 5&amp;amp;ndash;18%; the maximum deviation of 17.07% occurs at Tw = &amp;amp;minus;25 &amp;amp;deg;C, possibly due to increased experimental uncertainty at very low temperatures. Results demonstrate that lower cold plate temperatures lead to greater frost thickness and higher ice volume fraction. A key physical insight is that under natural convection, local convective circulation causes enhanced frosting at the plate edges, resulting in spatial non-uniformity in both thickness and density. The study covers cold plate temperatures from &amp;amp;minus;10 &amp;amp;deg;C to &amp;amp;minus;25 &amp;amp;deg;C at relative humidity of 60%. The frost growth rate and density at both ends of the cold plate exceed those in the central region, and this difference intensifies with decreasing temperature. Within the frost layer, humid air velocity is nearly zero, while maximum velocity occurs near the sides due to natural convection. The simulation results show good agreement with experimental data, confirming the model&amp;amp;rsquo;s reliability for natural convection scenarios.</p>
	]]></content:encoded>

	<dc:title>A Numerical Study of Frost Formation from Humid Air on Horizontal Cold Plate Surfaces Under Natural Convection</dc:title>
			<dc:creator>Zhengsheng Yang</dc:creator>
			<dc:creator>Fan Shi</dc:creator>
			<dc:creator>Jiawang Li</dc:creator>
			<dc:creator>Shukun Liu</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030074</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-10</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-10</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>74</prism:startingPage>
		<prism:doi>10.3390/fluids11030074</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/74</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/73">

	<title>Fluids, Vol. 11, Pages 73: A Reduced-Order Burgers-Type Vortex Model with Shear-Driven Gyroscopic Precession</title>
	<link>https://www.mdpi.com/2311-5521/11/3/73</link>
	<description>Slow lateral wandering and trochoidal-like motion are commonly observed in intense atmospheric vortices, yet most reduced-order vortex models assume a fixed axis or represent centre motion as purely advective. In this work, we propose a minimal reduced-order framework in which slow gyroscopic precession is introduced as an explicit degree of freedom superimposed on a rapidly rotating vortex core. The vortex is represented by a Burgers&amp;amp;ndash;Rott-type velocity field with time-dependent stretching rate and circulation, while the vortex centre undergoes a slow precessional motion governed by a time-dependent rate &amp;amp;Omega;p(t). The evolution of the vortex parameters is coupled to environmental variability through simple relaxation laws driven by standard large-scale diagnostics, including convective available potential energy, vertical shear, and background vorticity. A tracker-only analysis of tropical cyclone best-track data is used to constrain the appropriate dynamical regime at the track scale, indicating that observed centre wandering typically occurs in a slow-precession limit P = &amp;amp;Omega;p/&amp;amp;omega;c&amp;amp;#8810;1. Numerical demonstrations in cyclone-like configurations show that, despite the smallness of the precession number, cumulative lateral displacement and enhanced Lagrangian dispersion can develop over the vortex lifetime. The proposed framework is intended as a proof-of-concept reduced-order model that isolates the role of weak, environmentally forced precession in modulating vortex wandering and transport, and complements more detailed numerical and observational studies.</description>
	<pubDate>2026-03-10</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 73: A Reduced-Order Burgers-Type Vortex Model with Shear-Driven Gyroscopic Precession</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/73">doi: 10.3390/fluids11030073</a></p>
	<p>Authors:
		Waleed Mouhali
		</p>
	<p>Slow lateral wandering and trochoidal-like motion are commonly observed in intense atmospheric vortices, yet most reduced-order vortex models assume a fixed axis or represent centre motion as purely advective. In this work, we propose a minimal reduced-order framework in which slow gyroscopic precession is introduced as an explicit degree of freedom superimposed on a rapidly rotating vortex core. The vortex is represented by a Burgers&amp;amp;ndash;Rott-type velocity field with time-dependent stretching rate and circulation, while the vortex centre undergoes a slow precessional motion governed by a time-dependent rate &amp;amp;Omega;p(t). The evolution of the vortex parameters is coupled to environmental variability through simple relaxation laws driven by standard large-scale diagnostics, including convective available potential energy, vertical shear, and background vorticity. A tracker-only analysis of tropical cyclone best-track data is used to constrain the appropriate dynamical regime at the track scale, indicating that observed centre wandering typically occurs in a slow-precession limit P = &amp;amp;Omega;p/&amp;amp;omega;c&amp;amp;#8810;1. Numerical demonstrations in cyclone-like configurations show that, despite the smallness of the precession number, cumulative lateral displacement and enhanced Lagrangian dispersion can develop over the vortex lifetime. The proposed framework is intended as a proof-of-concept reduced-order model that isolates the role of weak, environmentally forced precession in modulating vortex wandering and transport, and complements more detailed numerical and observational studies.</p>
	]]></content:encoded>

	<dc:title>A Reduced-Order Burgers-Type Vortex Model with Shear-Driven Gyroscopic Precession</dc:title>
			<dc:creator>Waleed Mouhali</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030073</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-10</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-10</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>73</prism:startingPage>
		<prism:doi>10.3390/fluids11030073</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/73</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/72">

	<title>Fluids, Vol. 11, Pages 72: Low Reynolds Number Settling of Bent Rods in Quiescent Fluid</title>
	<link>https://www.mdpi.com/2311-5521/11/3/72</link>
	<description>This study experimentally investigates the settling behavior of bent (V-shaped and curved) and straight rods in a quiescent fluid at low and finite Reynolds numbers (Re&amp;amp;lt;3). The impact of the rod morphology on the terminal settling velocity and drag coefficient was examined, with a particular focus on V-shaped rods compared to straight rods of the same dimensions (diameter and length) and curved rods of the same dimensions and projected area. The results show that V-shaped rods consistently settle faster than straight rods, with velocity differences influenced by the bend angle. This velocity difference reaches a maximum of 57% for a V-shaped rod with a diameter of 0.50 mm, an aspect ratio of 90, and a bend angle of 45 degrees. When compared to curved rods, V-shaped rods exhibit slightly higher terminal velocities, with a maximum difference of 4% in this study, attributed to differences in mean inclination angles. Furthermore, the drag coefficient trends reflect the interplay between the settling velocity and projected area changes with the rod geometry. A new semi-empirical model with an RMS error of 7.1% was also developed to predict the drag coefficients and terminal velocities of straight and bent rods within the ranges studied. These findings and the model presented underscore the significance of the fibre shape in accurately predicting settling dynamics, with implications for atmospheric transport modeling and industrial applications involving fibrous particles.</description>
	<pubDate>2026-03-09</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 72: Low Reynolds Number Settling of Bent Rods in Quiescent Fluid</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/72">doi: 10.3390/fluids11030072</a></p>
	<p>Authors:
		Amirhossein Hamidi
		Daniel Daramsing
		Mark D. Gordon
		Ronald E. Hanson
		</p>
	<p>This study experimentally investigates the settling behavior of bent (V-shaped and curved) and straight rods in a quiescent fluid at low and finite Reynolds numbers (Re&amp;amp;lt;3). The impact of the rod morphology on the terminal settling velocity and drag coefficient was examined, with a particular focus on V-shaped rods compared to straight rods of the same dimensions (diameter and length) and curved rods of the same dimensions and projected area. The results show that V-shaped rods consistently settle faster than straight rods, with velocity differences influenced by the bend angle. This velocity difference reaches a maximum of 57% for a V-shaped rod with a diameter of 0.50 mm, an aspect ratio of 90, and a bend angle of 45 degrees. When compared to curved rods, V-shaped rods exhibit slightly higher terminal velocities, with a maximum difference of 4% in this study, attributed to differences in mean inclination angles. Furthermore, the drag coefficient trends reflect the interplay between the settling velocity and projected area changes with the rod geometry. A new semi-empirical model with an RMS error of 7.1% was also developed to predict the drag coefficients and terminal velocities of straight and bent rods within the ranges studied. These findings and the model presented underscore the significance of the fibre shape in accurately predicting settling dynamics, with implications for atmospheric transport modeling and industrial applications involving fibrous particles.</p>
	]]></content:encoded>

	<dc:title>Low Reynolds Number Settling of Bent Rods in Quiescent Fluid</dc:title>
			<dc:creator>Amirhossein Hamidi</dc:creator>
			<dc:creator>Daniel Daramsing</dc:creator>
			<dc:creator>Mark D. Gordon</dc:creator>
			<dc:creator>Ronald E. Hanson</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030072</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-09</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-09</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>72</prism:startingPage>
		<prism:doi>10.3390/fluids11030072</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/72</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/71">

	<title>Fluids, Vol. 11, Pages 71: Design, Testing and Numerical Modelling of a Low-Speed Wind Tunnel Gust Generator</title>
	<link>https://www.mdpi.com/2311-5521/11/3/71</link>
	<description>Accurate reproduction of deterministic gusts in wind tunnels is essential for studying unsteady aerodynamics and aeroelastic response in aircraft, uninhabited aerial vehicles, and wind turbines. This work presents the design, experimental characterization, and numerical modelling of a low-speed gust generator based on oscillating vanes, capable of producing high-amplitude gusts in strongly unsteady flow regimes. Cross-flow hot-wire measurements are combined with time-accurate computational fluid dynamics simulations to analyze gust formation and propagation. Classical &amp;amp;lsquo;1-cos&amp;amp;rsquo; gusts are shown to exhibit pronounced negative velocity peaks associated with start&amp;amp;ndash;stop vortex shedding. A modified vane motion protocol is proposed that significantly reduces the negative peak factor while preserving a substantial gust ratio over a wide range of reduced frequencies. Measurements are supplemented with computational fluid dynamics (CFD) simulations. The CFD study included 2D and 3D URANS as well as higher fidelity DES simulations. Flow-field analysis reveals that secondary variations in gust angle arise from nonlinear interactions between vortices shed by adjacent vanes and are influenced by wind-tunnel confinement. The results provide physical insight into the limitations of oscillating-vane gust generators and guidance for the design of high-fidelity gust-generation systems.</description>
	<pubDate>2026-03-08</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 71: Design, Testing and Numerical Modelling of a Low-Speed Wind Tunnel Gust Generator</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/71">doi: 10.3390/fluids11030071</a></p>
	<p>Authors:
		Marinos Manolesos
		Christos Ampatis
		Dimitris Gkiolas
		Konstantinos Rekoumis
		George Papadakis
		</p>
	<p>Accurate reproduction of deterministic gusts in wind tunnels is essential for studying unsteady aerodynamics and aeroelastic response in aircraft, uninhabited aerial vehicles, and wind turbines. This work presents the design, experimental characterization, and numerical modelling of a low-speed gust generator based on oscillating vanes, capable of producing high-amplitude gusts in strongly unsteady flow regimes. Cross-flow hot-wire measurements are combined with time-accurate computational fluid dynamics simulations to analyze gust formation and propagation. Classical &amp;amp;lsquo;1-cos&amp;amp;rsquo; gusts are shown to exhibit pronounced negative velocity peaks associated with start&amp;amp;ndash;stop vortex shedding. A modified vane motion protocol is proposed that significantly reduces the negative peak factor while preserving a substantial gust ratio over a wide range of reduced frequencies. Measurements are supplemented with computational fluid dynamics (CFD) simulations. The CFD study included 2D and 3D URANS as well as higher fidelity DES simulations. Flow-field analysis reveals that secondary variations in gust angle arise from nonlinear interactions between vortices shed by adjacent vanes and are influenced by wind-tunnel confinement. The results provide physical insight into the limitations of oscillating-vane gust generators and guidance for the design of high-fidelity gust-generation systems.</p>
	]]></content:encoded>

	<dc:title>Design, Testing and Numerical Modelling of a Low-Speed Wind Tunnel Gust Generator</dc:title>
			<dc:creator>Marinos Manolesos</dc:creator>
			<dc:creator>Christos Ampatis</dc:creator>
			<dc:creator>Dimitris Gkiolas</dc:creator>
			<dc:creator>Konstantinos Rekoumis</dc:creator>
			<dc:creator>George Papadakis</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030071</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-08</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-08</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>71</prism:startingPage>
		<prism:doi>10.3390/fluids11030071</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/71</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/70">

	<title>Fluids, Vol. 11, Pages 70: Rheological Characterization and Viscosity Correlation for a 9.5 &amp;deg;API Extra-Heavy Crude Oil of the Southern Gulf of Mexico</title>
	<link>https://www.mdpi.com/2311-5521/11/3/70</link>
	<description>The rheological behavior of a 9.5 &amp;amp;deg;API extra-heavy dead crude oil produced in the southern Gulf of Mexico is experimentally investigated over the temperature range 30&amp;amp;nbsp;&amp;amp;deg;C&amp;amp;le;T&amp;amp;le;100&amp;amp;nbsp;&amp;amp;deg;C. Steady-shear measurements are used to characterize the stress&amp;amp;ndash;strain-rate response and apparent viscosity under controlled laboratory conditions representative of surface transport. Statistical analyses show that the oil exhibits a Bingham plastic behavior at 30 &amp;amp;deg;C, transitions to a Herschel&amp;amp;ndash;Bulkley-type response at 50 &amp;amp;deg;C, and displays a predominantly dilatant behavior at 100 &amp;amp;deg;C. Existing dead oil viscosity correlations commonly used in field applications are evaluated against the experimental data and are found to systematically underpredict the viscosity by approximately one order of magnitude within the studied temperature range. Motivated by the observed exponential dependence of viscosity on temperature, a crude-specific viscosity&amp;amp;ndash;temperature correlation is proposed for this specific crude oil. The new correlation provides a significantly improved representation of the experimental data and leads to substantially more accurate pressure drop predictions in a representative pipeline transport scenario. The results highlight the importance of crude-oil-specific rheological characterization and viscosity modeling for reliable flow assurance analyses involving extra-heavy crude oils.</description>
	<pubDate>2026-03-05</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 70: Rheological Characterization and Viscosity Correlation for a 9.5 &amp;deg;API Extra-Heavy Crude Oil of the Southern Gulf of Mexico</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/70">doi: 10.3390/fluids11030070</a></p>
	<p>Authors:
		Matei Badalan
		Enrique León Aboytes
		Leonardo Di G. Sigalotti
		Enrique Guzmán
		</p>
	<p>The rheological behavior of a 9.5 &amp;amp;deg;API extra-heavy dead crude oil produced in the southern Gulf of Mexico is experimentally investigated over the temperature range 30&amp;amp;nbsp;&amp;amp;deg;C&amp;amp;le;T&amp;amp;le;100&amp;amp;nbsp;&amp;amp;deg;C. Steady-shear measurements are used to characterize the stress&amp;amp;ndash;strain-rate response and apparent viscosity under controlled laboratory conditions representative of surface transport. Statistical analyses show that the oil exhibits a Bingham plastic behavior at 30 &amp;amp;deg;C, transitions to a Herschel&amp;amp;ndash;Bulkley-type response at 50 &amp;amp;deg;C, and displays a predominantly dilatant behavior at 100 &amp;amp;deg;C. Existing dead oil viscosity correlations commonly used in field applications are evaluated against the experimental data and are found to systematically underpredict the viscosity by approximately one order of magnitude within the studied temperature range. Motivated by the observed exponential dependence of viscosity on temperature, a crude-specific viscosity&amp;amp;ndash;temperature correlation is proposed for this specific crude oil. The new correlation provides a significantly improved representation of the experimental data and leads to substantially more accurate pressure drop predictions in a representative pipeline transport scenario. The results highlight the importance of crude-oil-specific rheological characterization and viscosity modeling for reliable flow assurance analyses involving extra-heavy crude oils.</p>
	]]></content:encoded>

	<dc:title>Rheological Characterization and Viscosity Correlation for a 9.5 &amp;amp;deg;API Extra-Heavy Crude Oil of the Southern Gulf of Mexico</dc:title>
			<dc:creator>Matei Badalan</dc:creator>
			<dc:creator>Enrique León Aboytes</dc:creator>
			<dc:creator>Leonardo Di G. Sigalotti</dc:creator>
			<dc:creator>Enrique Guzmán</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030070</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-05</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-05</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>70</prism:startingPage>
		<prism:doi>10.3390/fluids11030070</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/70</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/69">

	<title>Fluids, Vol. 11, Pages 69: 3D-Printed Tesla Valve with IoT-Based Flow and Pressure Sensing</title>
	<link>https://www.mdpi.com/2311-5521/11/3/69</link>
	<description>Tesla valves are passive flow-control devices that enables asymmetry without moving parts. In recent years, they have attracted renewed interest due to their wide range of applications, spanning from biomedical and agricultural systems to thermal and marine engineering. The performance of a 3D-printed double Tesla valve is experimentally investigated using an integrated low-cost Internet of Things (IoT) measurement system. The valve performance is evaluated for inlet volumetric flow rates ranging from 5 to 20 L/min. The results demonstrate a clear asymmetry between forward and reverse flow, with a maximum diodicity of 1.96 observed at the lowest (5&amp;amp;ndash;6 L/min) flow rate. The proposed low-cost experimental framework combines additive manufacturing and real-time IoT-based monitoring, offering a reproducible and accessible approach for investigating passive flow-control devices at flow-rate regimes beyond typical microfluidic applications.</description>
	<pubDate>2026-03-04</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 69: 3D-Printed Tesla Valve with IoT-Based Flow and Pressure Sensing</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/69">doi: 10.3390/fluids11030069</a></p>
	<p>Authors:
		Christos Liosis
		Dimitrios Nikolaos Pagonis
		Sofia Peppa
		Michail Drossos
		Ioannis Sarris
		</p>
	<p>Tesla valves are passive flow-control devices that enables asymmetry without moving parts. In recent years, they have attracted renewed interest due to their wide range of applications, spanning from biomedical and agricultural systems to thermal and marine engineering. The performance of a 3D-printed double Tesla valve is experimentally investigated using an integrated low-cost Internet of Things (IoT) measurement system. The valve performance is evaluated for inlet volumetric flow rates ranging from 5 to 20 L/min. The results demonstrate a clear asymmetry between forward and reverse flow, with a maximum diodicity of 1.96 observed at the lowest (5&amp;amp;ndash;6 L/min) flow rate. The proposed low-cost experimental framework combines additive manufacturing and real-time IoT-based monitoring, offering a reproducible and accessible approach for investigating passive flow-control devices at flow-rate regimes beyond typical microfluidic applications.</p>
	]]></content:encoded>

	<dc:title>3D-Printed Tesla Valve with IoT-Based Flow and Pressure Sensing</dc:title>
			<dc:creator>Christos Liosis</dc:creator>
			<dc:creator>Dimitrios Nikolaos Pagonis</dc:creator>
			<dc:creator>Sofia Peppa</dc:creator>
			<dc:creator>Michail Drossos</dc:creator>
			<dc:creator>Ioannis Sarris</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030069</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-04</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-04</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>69</prism:startingPage>
		<prism:doi>10.3390/fluids11030069</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/69</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/68">

	<title>Fluids, Vol. 11, Pages 68: Numerical Simulation of the Flow Around Cylinders for a Wide Range of Reynolds Numbers</title>
	<link>https://www.mdpi.com/2311-5521/11/3/68</link>
	<description>To support the increasing complexity of innovation, design, and performance evaluation in the maritime industry, a ship-specific computational fluid dynamics (CFD) software suite tailored to incompressible viscous flow is required. This study utilizes the MarineFlow marine fluid dynamics code to explore numerical simulation schemes for cylindrical flow problems across a broad range of Reynolds numbers (1–107) that are applicable to self-developed codes. Additionally, an analysis of the flow around a cylinder is conducted from the perspective of code developers. Various grid types and turbulence model schemes are employed to analyze and compare the drag coefficient, separation points, and pressure distribution characteristics of the cylinder. The results obtained from these simulations are then contrasted with those derived from commercial CFD software to assess their accuracy. Despite the presence of certain numerical artifacts, within the Reynolds number range of 1–105, the unstructured grids combined with the laminar flow models effectively capture experimental data. Further exploration of the transitional Reynolds number range (Re = 2×105–6×105) shows a consistent decreasing trend in the mean drag coefficient, although significant deviations from theoretical predictions are evident. From the perspective of code developers, this study aims to reveal the limitations of current computational schemes and code architecture in accurately capturing flow dynamics within the transitional Reynolds number range. This provides a crucial basis for future optimization of turbulence models and algorithmic improvements, which are essential for the continued development of self-developed CFD codes and their engineering applications.</description>
	<pubDate>2026-03-03</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 68: Numerical Simulation of the Flow Around Cylinders for a Wide Range of Reynolds Numbers</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/68">doi: 10.3390/fluids11030068</a></p>
	<p>Authors:
		Haowen Yao
		Tianli Hu
		Junya Yang
		Jianchun Wang
		Chengsheng Wu
		</p>
	<p>To support the increasing complexity of innovation, design, and performance evaluation in the maritime industry, a ship-specific computational fluid dynamics (CFD) software suite tailored to incompressible viscous flow is required. This study utilizes the MarineFlow marine fluid dynamics code to explore numerical simulation schemes for cylindrical flow problems across a broad range of Reynolds numbers (1–107) that are applicable to self-developed codes. Additionally, an analysis of the flow around a cylinder is conducted from the perspective of code developers. Various grid types and turbulence model schemes are employed to analyze and compare the drag coefficient, separation points, and pressure distribution characteristics of the cylinder. The results obtained from these simulations are then contrasted with those derived from commercial CFD software to assess their accuracy. Despite the presence of certain numerical artifacts, within the Reynolds number range of 1–105, the unstructured grids combined with the laminar flow models effectively capture experimental data. Further exploration of the transitional Reynolds number range (Re = 2×105–6×105) shows a consistent decreasing trend in the mean drag coefficient, although significant deviations from theoretical predictions are evident. From the perspective of code developers, this study aims to reveal the limitations of current computational schemes and code architecture in accurately capturing flow dynamics within the transitional Reynolds number range. This provides a crucial basis for future optimization of turbulence models and algorithmic improvements, which are essential for the continued development of self-developed CFD codes and their engineering applications.</p>
	]]></content:encoded>

	<dc:title>Numerical Simulation of the Flow Around Cylinders for a Wide Range of Reynolds Numbers</dc:title>
			<dc:creator>Haowen Yao</dc:creator>
			<dc:creator>Tianli Hu</dc:creator>
			<dc:creator>Junya Yang</dc:creator>
			<dc:creator>Jianchun Wang</dc:creator>
			<dc:creator>Chengsheng Wu</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030068</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-03</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-03</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>68</prism:startingPage>
		<prism:doi>10.3390/fluids11030068</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/68</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/67">

	<title>Fluids, Vol. 11, Pages 67: Spatiotemporal Analysis of Transient Liquid Film Shape</title>
	<link>https://www.mdpi.com/2311-5521/11/3/67</link>
	<description>Precise control of thin liquid film deposition is crucial in applications where film stability and internal liquid flow significantly impact the dry film shape or the efficiency of sample or drug delivery. No prior work has automated the extraction and measurement uncertainty quantification of film geometric parameters from dual-view optical visualization with minimal user input. We present Python-based software that extracts time-resolved film thickness, width, and the positions of three contact lines from visual data using computer vision. The utility of such analysis is demonstrated by depositing 30% glycerol on a flexible tape through a circular nozzle orifice. The nozzle is positioned at a distance of h = 0.3 mm from the tape at an angle of attack &amp;amp;alpha; = 45&amp;amp;deg;, with deposition controlled at a volume flow rate V&amp;amp;#729; = 30 &amp;amp;mu;L min&amp;amp;minus;1 and tape velocity v = 1.0 mm s&amp;amp;minus;1. Expanded measurement uncertainties are 21 &amp;amp;mu;m, 22 &amp;amp;mu;m, and 53 &amp;amp;mu;m for the upstream static, downstream static, and upstream dynamic contact line positions, respectively, with maximum relative uncertainties of 10.3% and 8.2% for film thickness and width. Static contact line oscillations remain within measurement uncertainty, whereas the upstream dynamic contact line exhibits resolvable oscillations. This dual-view framework provides high-resolution insights into liquid film dynamics, which is crucial for comprehensive control of liquid film deposition.</description>
	<pubDate>2026-03-03</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 67: Spatiotemporal Analysis of Transient Liquid Film Shape</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/67">doi: 10.3390/fluids11030067</a></p>
	<p>Authors:
		Gašper Vidic
		Saša Bajt
		Božidar Šarler
		</p>
	<p>Precise control of thin liquid film deposition is crucial in applications where film stability and internal liquid flow significantly impact the dry film shape or the efficiency of sample or drug delivery. No prior work has automated the extraction and measurement uncertainty quantification of film geometric parameters from dual-view optical visualization with minimal user input. We present Python-based software that extracts time-resolved film thickness, width, and the positions of three contact lines from visual data using computer vision. The utility of such analysis is demonstrated by depositing 30% glycerol on a flexible tape through a circular nozzle orifice. The nozzle is positioned at a distance of h = 0.3 mm from the tape at an angle of attack &amp;amp;alpha; = 45&amp;amp;deg;, with deposition controlled at a volume flow rate V&amp;amp;#729; = 30 &amp;amp;mu;L min&amp;amp;minus;1 and tape velocity v = 1.0 mm s&amp;amp;minus;1. Expanded measurement uncertainties are 21 &amp;amp;mu;m, 22 &amp;amp;mu;m, and 53 &amp;amp;mu;m for the upstream static, downstream static, and upstream dynamic contact line positions, respectively, with maximum relative uncertainties of 10.3% and 8.2% for film thickness and width. Static contact line oscillations remain within measurement uncertainty, whereas the upstream dynamic contact line exhibits resolvable oscillations. This dual-view framework provides high-resolution insights into liquid film dynamics, which is crucial for comprehensive control of liquid film deposition.</p>
	]]></content:encoded>

	<dc:title>Spatiotemporal Analysis of Transient Liquid Film Shape</dc:title>
			<dc:creator>Gašper Vidic</dc:creator>
			<dc:creator>Saša Bajt</dc:creator>
			<dc:creator>Božidar Šarler</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030067</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-03</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-03</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>67</prism:startingPage>
		<prism:doi>10.3390/fluids11030067</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/67</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/66">

	<title>Fluids, Vol. 11, Pages 66: Determination of the Boundary of the &amp;ldquo;Diffusion&amp;ndash;Gravitational Convection&amp;rdquo; Regimes Change in Three-Component Gas Mixtures Containing Real Gases, Taking into Account the Compressibility Factor of the Components Under Isothermal Conditions</title>
	<link>https://www.mdpi.com/2311-5521/11/3/66</link>
	<description>The stability analysis for isothermal three-component gas mixtures, in which one of the components exhibits real properties in the considered pressure range, is performed. The system of Navier&amp;amp;ndash;Stokes and diffusion equations in the Boussinesq approximation is considered, taking into account analogs of buoyancy effects in a density-stratified medium. The presented solution is obtained by the small-perturbation method using the principle of diffusion independence, while maintaining the condition of neutrality of convective perturbations. Expressions for the boundary between the &amp;amp;ldquo;diffusion&amp;amp;ndash;gravitational convection&amp;amp;rdquo; regimes are obtained in terms of partial Rayleigh numbers that account for the compressibility factor of the mixing components. The stability cartograms show that on the stability maps, the position of the boundary of the regimes change depends on the variation in the compressibility factor with a pressure change. When the compressibility factor changes, the values of the critical Rayleigh numbers, which are the intersection points of the boundary of the regimes change and the coordinate axes, decrease. It is established that the behavior of the partial Rayleigh numbers on the plane (Ra1, Ra2) is nonlinear for isothermal ternary mixtures, which have the general form H2 + N2O&amp;amp;ndash;N2 and He + CO2&amp;amp;ndash;N2, He + R12&amp;amp;ndash;Ar, at T = 298.0 K and elevated pressures. It is revealed that when taking into account the compressibility factor of the components, the partial Rayleigh numbers of the components decrease.</description>
	<pubDate>2026-03-02</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 66: Determination of the Boundary of the &amp;ldquo;Diffusion&amp;ndash;Gravitational Convection&amp;rdquo; Regimes Change in Three-Component Gas Mixtures Containing Real Gases, Taking into Account the Compressibility Factor of the Components Under Isothermal Conditions</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/66">doi: 10.3390/fluids11030066</a></p>
	<p>Authors:
		Vladimir Kossov
		Olga Fedorenko
		Holm Altenbach
		Madina Tuken
		</p>
	<p>The stability analysis for isothermal three-component gas mixtures, in which one of the components exhibits real properties in the considered pressure range, is performed. The system of Navier&amp;amp;ndash;Stokes and diffusion equations in the Boussinesq approximation is considered, taking into account analogs of buoyancy effects in a density-stratified medium. The presented solution is obtained by the small-perturbation method using the principle of diffusion independence, while maintaining the condition of neutrality of convective perturbations. Expressions for the boundary between the &amp;amp;ldquo;diffusion&amp;amp;ndash;gravitational convection&amp;amp;rdquo; regimes are obtained in terms of partial Rayleigh numbers that account for the compressibility factor of the mixing components. The stability cartograms show that on the stability maps, the position of the boundary of the regimes change depends on the variation in the compressibility factor with a pressure change. When the compressibility factor changes, the values of the critical Rayleigh numbers, which are the intersection points of the boundary of the regimes change and the coordinate axes, decrease. It is established that the behavior of the partial Rayleigh numbers on the plane (Ra1, Ra2) is nonlinear for isothermal ternary mixtures, which have the general form H2 + N2O&amp;amp;ndash;N2 and He + CO2&amp;amp;ndash;N2, He + R12&amp;amp;ndash;Ar, at T = 298.0 K and elevated pressures. It is revealed that when taking into account the compressibility factor of the components, the partial Rayleigh numbers of the components decrease.</p>
	]]></content:encoded>

	<dc:title>Determination of the Boundary of the &amp;amp;ldquo;Diffusion&amp;amp;ndash;Gravitational Convection&amp;amp;rdquo; Regimes Change in Three-Component Gas Mixtures Containing Real Gases, Taking into Account the Compressibility Factor of the Components Under Isothermal Conditions</dc:title>
			<dc:creator>Vladimir Kossov</dc:creator>
			<dc:creator>Olga Fedorenko</dc:creator>
			<dc:creator>Holm Altenbach</dc:creator>
			<dc:creator>Madina Tuken</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030066</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-03-02</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-03-02</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>66</prism:startingPage>
		<prism:doi>10.3390/fluids11030066</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/66</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/65">

	<title>Fluids, Vol. 11, Pages 65: Aerodynamic Characteristics Analysis of Floating Wind Turbine Subjected to Different Wind and Platform Movement Directions</title>
	<link>https://www.mdpi.com/2311-5521/11/3/65</link>
	<description>Floating offshore wind turbines (FOWTs) are subjected to complex oceanic environmental loads, which can result in non-collinear wind and wave directions that may not align with the rotor axis, potentially leading to complex variations in aerodynamic characteristics. In this study, the aerodynamic performance and wake of the NREL 5 MW wind turbine under different inflow angles and platform surge motions in various directions were investigated using the actuator line model (ALM) implemented in OpenFOAM. The results demonstrate that an increase in surge amplitude primarily amplifies the cyclic fluctuations in rotor thrust and torque, while the direction of surge motion has a negligible influence. In contrast, yawed inflow leads to a substantial reduction in both the mean and peak values of thrust and torque. Wake analysis further reveals that the mean wake recovery is predominantly governed by the yaw angle. Under aligned inflow conditions, the wake remains nearly symmetric and shows limited sensitivity to platform surge motion. Conversely, yawed inflow induces significant wake deflection with an asymmetric distribution of turbulent kinetic energy and enhanced mixing in the downstream region.</description>
	<pubDate>2026-02-28</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 65: Aerodynamic Characteristics Analysis of Floating Wind Turbine Subjected to Different Wind and Platform Movement Directions</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/65">doi: 10.3390/fluids11030065</a></p>
	<p>Authors:
		Bin Wang
		Yuyan Liu
		Guanming Zeng
		Yongqing Lai
		</p>
	<p>Floating offshore wind turbines (FOWTs) are subjected to complex oceanic environmental loads, which can result in non-collinear wind and wave directions that may not align with the rotor axis, potentially leading to complex variations in aerodynamic characteristics. In this study, the aerodynamic performance and wake of the NREL 5 MW wind turbine under different inflow angles and platform surge motions in various directions were investigated using the actuator line model (ALM) implemented in OpenFOAM. The results demonstrate that an increase in surge amplitude primarily amplifies the cyclic fluctuations in rotor thrust and torque, while the direction of surge motion has a negligible influence. In contrast, yawed inflow leads to a substantial reduction in both the mean and peak values of thrust and torque. Wake analysis further reveals that the mean wake recovery is predominantly governed by the yaw angle. Under aligned inflow conditions, the wake remains nearly symmetric and shows limited sensitivity to platform surge motion. Conversely, yawed inflow induces significant wake deflection with an asymmetric distribution of turbulent kinetic energy and enhanced mixing in the downstream region.</p>
	]]></content:encoded>

	<dc:title>Aerodynamic Characteristics Analysis of Floating Wind Turbine Subjected to Different Wind and Platform Movement Directions</dc:title>
			<dc:creator>Bin Wang</dc:creator>
			<dc:creator>Yuyan Liu</dc:creator>
			<dc:creator>Guanming Zeng</dc:creator>
			<dc:creator>Yongqing Lai</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030065</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-02-28</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-02-28</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>65</prism:startingPage>
		<prism:doi>10.3390/fluids11030065</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/65</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/64">

	<title>Fluids, Vol. 11, Pages 64: From Laboratory Measurements to AI-Driven Insights: Predicting Shaped Charge Performance with Advanced Machine Learning</title>
	<link>https://www.mdpi.com/2311-5521/11/3/64</link>
	<description>The accurate estimation of the perforation length is very vital to improve fluid flow as well as the management of charges. Traditional methods, including empirical correlations, analytical models, and API 19B surface tests, suffer from significant limitations in their scope, require frequent recalibration, and fail to capture the complex physics governing shaped charge penetration. This study develops and validates machine learning models for perforation length prediction using a comprehensive dataset of 1648 API 19B standardized tests encompassing diverse gun configurations, explosive properties, and completion parameters. The dataset was partitioned into 1318 tests for model training and hyperparameter optimization, with 330 independent tests reserved for blind validation. Ten regression algorithms were systematically evaluated, with XGBoost demonstrating superior performance, achieving an R2 coefficient of 0.956 on blind validation. Feature importance analysis revealed explosive weight as the dominant predictor, followed by temperature rating. The application of machine learning models offers an accurate, easier, instantaneous during planning and design workflows, and cheaper way of estimation as compared to traditional methods.</description>
	<pubDate>2026-02-27</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 64: From Laboratory Measurements to AI-Driven Insights: Predicting Shaped Charge Performance with Advanced Machine Learning</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/64">doi: 10.3390/fluids11030064</a></p>
	<p>Authors:
		Samuel Nashed
		Muhammad Abdullah
		Oluchi Ejehu
		Badr Mohamed
		Norhan Sedki
		Rouzbeh Moghanloo
		</p>
	<p>The accurate estimation of the perforation length is very vital to improve fluid flow as well as the management of charges. Traditional methods, including empirical correlations, analytical models, and API 19B surface tests, suffer from significant limitations in their scope, require frequent recalibration, and fail to capture the complex physics governing shaped charge penetration. This study develops and validates machine learning models for perforation length prediction using a comprehensive dataset of 1648 API 19B standardized tests encompassing diverse gun configurations, explosive properties, and completion parameters. The dataset was partitioned into 1318 tests for model training and hyperparameter optimization, with 330 independent tests reserved for blind validation. Ten regression algorithms were systematically evaluated, with XGBoost demonstrating superior performance, achieving an R2 coefficient of 0.956 on blind validation. Feature importance analysis revealed explosive weight as the dominant predictor, followed by temperature rating. The application of machine learning models offers an accurate, easier, instantaneous during planning and design workflows, and cheaper way of estimation as compared to traditional methods.</p>
	]]></content:encoded>

	<dc:title>From Laboratory Measurements to AI-Driven Insights: Predicting Shaped Charge Performance with Advanced Machine Learning</dc:title>
			<dc:creator>Samuel Nashed</dc:creator>
			<dc:creator>Muhammad Abdullah</dc:creator>
			<dc:creator>Oluchi Ejehu</dc:creator>
			<dc:creator>Badr Mohamed</dc:creator>
			<dc:creator>Norhan Sedki</dc:creator>
			<dc:creator>Rouzbeh Moghanloo</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030064</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-02-27</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-02-27</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>64</prism:startingPage>
		<prism:doi>10.3390/fluids11030064</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/64</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/63">

	<title>Fluids, Vol. 11, Pages 63: Effects of Nozzle Geometry on Fine Bubble Generation and Surface Cleaning Performance</title>
	<link>https://www.mdpi.com/2311-5521/11/3/63</link>
	<description>Fine bubbles have attracted attention in recent years due to their promising characteristics and extensive applications. One type of fine bubble generator, the Venturi tube, utilizes a sudden change in pressure inside the tube and is widely used due to its simple structure, high generation efficiency, and low power consumption. The volume of bubbles generated (generation yield) and their average diameter are key parameters in evaluating the performance of a Venturi tube generator, which depends on both the flow conditions and the geometric configuration of the generator. In this study, an oral irrigator incorporating fine bubble technology was developed, with a Venturi tube embedded in the irrigator for fine bubble generation. We designed Venturi tubes with various geometric configurations under different flow conditions to enhance fine bubble generation performance and cleaning efficiency through both experiments and numerical simulations. The results indicate that the generation performance and cleaning performance of fine bubbles are strongly influenced by the geometric parameters of the Venturi tube. Among the tested configurations, the Venturi tube with a divergent angle of 5&amp;amp;deg; and a divergent length of 30 mm demonstrated the best performance.</description>
	<pubDate>2026-02-27</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 63: Effects of Nozzle Geometry on Fine Bubble Generation and Surface Cleaning Performance</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/63">doi: 10.3390/fluids11030063</a></p>
	<p>Authors:
		Xin Jiang
		Ryota Matoyama
		Yumiko Otobe
		Masaki Shimazu
		Satoru Ogahara
		</p>
	<p>Fine bubbles have attracted attention in recent years due to their promising characteristics and extensive applications. One type of fine bubble generator, the Venturi tube, utilizes a sudden change in pressure inside the tube and is widely used due to its simple structure, high generation efficiency, and low power consumption. The volume of bubbles generated (generation yield) and their average diameter are key parameters in evaluating the performance of a Venturi tube generator, which depends on both the flow conditions and the geometric configuration of the generator. In this study, an oral irrigator incorporating fine bubble technology was developed, with a Venturi tube embedded in the irrigator for fine bubble generation. We designed Venturi tubes with various geometric configurations under different flow conditions to enhance fine bubble generation performance and cleaning efficiency through both experiments and numerical simulations. The results indicate that the generation performance and cleaning performance of fine bubbles are strongly influenced by the geometric parameters of the Venturi tube. Among the tested configurations, the Venturi tube with a divergent angle of 5&amp;amp;deg; and a divergent length of 30 mm demonstrated the best performance.</p>
	]]></content:encoded>

	<dc:title>Effects of Nozzle Geometry on Fine Bubble Generation and Surface Cleaning Performance</dc:title>
			<dc:creator>Xin Jiang</dc:creator>
			<dc:creator>Ryota Matoyama</dc:creator>
			<dc:creator>Yumiko Otobe</dc:creator>
			<dc:creator>Masaki Shimazu</dc:creator>
			<dc:creator>Satoru Ogahara</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030063</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-02-27</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-02-27</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>63</prism:startingPage>
		<prism:doi>10.3390/fluids11030063</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/63</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
        <item rdf:about="https://www.mdpi.com/2311-5521/11/3/62">

	<title>Fluids, Vol. 11, Pages 62: Line Thermals from Finite Sources in Neutral and Stable Environments, with Application to Thermal Plumes from Submarines</title>
	<link>https://www.mdpi.com/2311-5521/11/3/62</link>
	<description>The first application of theory of the rise of line thermals was to understand the rise of turbulent smoke plumes emitted from smoke stacks into a cross-wind. Initial solutions required numerical calculations. In this article analytical solutions are found, and these are used here to explore solutions for the rise of buoyant line wakes from submarine vehicles. Solutions cater for wakes in both neutral and stable environments, and for sources which have either negative or positive initial buoyancy. Account is also taken of sources with differing size and initial momentum. Practical examples of submarine thermal wake flows are given using neutral and typical stably stratified upper ocean conditions and a range of source conditions. A key result is that small-diameter submarine wakes with high temperatures produced in weakly stratified ocean waters will have a large height of rise, and may easily reach the surface. By contrast, large-source-diameter wakes, with temperatures close to ambient and emitted into strongly stratified oceans, will have very small heights of rise.</description>
	<pubDate>2026-02-26</pubDate>

	<content:encoded><![CDATA[
	<p><b>Fluids, Vol. 11, Pages 62: Line Thermals from Finite Sources in Neutral and Stable Environments, with Application to Thermal Plumes from Submarines</b></p>
	<p>Fluids <a href="https://www.mdpi.com/2311-5521/11/3/62">doi: 10.3390/fluids11030062</a></p>
	<p>Authors:
		Jason H. Middleton
		</p>
	<p>The first application of theory of the rise of line thermals was to understand the rise of turbulent smoke plumes emitted from smoke stacks into a cross-wind. Initial solutions required numerical calculations. In this article analytical solutions are found, and these are used here to explore solutions for the rise of buoyant line wakes from submarine vehicles. Solutions cater for wakes in both neutral and stable environments, and for sources which have either negative or positive initial buoyancy. Account is also taken of sources with differing size and initial momentum. Practical examples of submarine thermal wake flows are given using neutral and typical stably stratified upper ocean conditions and a range of source conditions. A key result is that small-diameter submarine wakes with high temperatures produced in weakly stratified ocean waters will have a large height of rise, and may easily reach the surface. By contrast, large-source-diameter wakes, with temperatures close to ambient and emitted into strongly stratified oceans, will have very small heights of rise.</p>
	]]></content:encoded>

	<dc:title>Line Thermals from Finite Sources in Neutral and Stable Environments, with Application to Thermal Plumes from Submarines</dc:title>
			<dc:creator>Jason H. Middleton</dc:creator>
		<dc:identifier>doi: 10.3390/fluids11030062</dc:identifier>
	<dc:source>Fluids</dc:source>
	<dc:date>2026-02-26</dc:date>

	<prism:publicationName>Fluids</prism:publicationName>
	<prism:publicationDate>2026-02-26</prism:publicationDate>
	<prism:volume>11</prism:volume>
	<prism:number>3</prism:number>
	<prism:section>Article</prism:section>
	<prism:startingPage>62</prism:startingPage>
		<prism:doi>10.3390/fluids11030062</prism:doi>
	<prism:url>https://www.mdpi.com/2311-5521/11/3/62</prism:url>
	
	<cc:license rdf:resource="CC BY 4.0"/>
</item>
    
<cc:License rdf:about="https://creativecommons.org/licenses/by/4.0/">
	<cc:permits rdf:resource="https://creativecommons.org/ns#Reproduction" />
	<cc:permits rdf:resource="https://creativecommons.org/ns#Distribution" />
	<cc:permits rdf:resource="https://creativecommons.org/ns#DerivativeWorks" />
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