New Perspectives in Gas–Liquid Reactors

A special issue of Fluids (ISSN 2311-5521). This special issue belongs to the section "Flow of Multi-Phase Fluids and Granular Materials".

Deadline for manuscript submissions: closed (25 December 2024) | Viewed by 1975

Special Issue Editors


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Guest Editor
Institute for Process Engineering, Johannes Kepler University, Altenberger Straße 69, 4040 Linz, Austria
Interests: multi-phase flows; coalescence; breakup; hydrodynamics; computational fluid dynamics; artificial intelligence; measurement techniques; circular economy
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Guest Editor
Institute of Chemical Engineering, Polish Academy of Sciences, 5 Baltycka St., 44-100 Gliwice, Poland
Interests: multiphase reactors; flow regime identification; sophisticated time series analysis; nonlinear chaos theory; information entropy; liquid mixing; gas-liquid mass transfer
Special Issues, Collections and Topics in MDPI journals

Special Issue Information

Dear Colleagues,

Gas–liquid reactors (bubble columns, agitators, airlift reactors, etc.) are the most frequently used units in the chemical industry (absorption, oxidation, chlorination, etc.). They are also used in wastewater treatment, flotation, methanol synthesis, Fischer–Tropsch synthesis, papermaking, etc. Over the past four decades, the classical topics of hydrodynamics, mixing, mass transfer (MT) and heat transfer in these reactors have been extensively studied. Many new empirical and theoretical correlations have been developed. The presence of catalytic particles has also been studied. However, new areas of research in these types of reactors have emerged. The most important new areas are the Computational Fluid Dynamics (CFD) simulations and the operation with various ionic liquids, as well as the new modifications (including vibrations) of these classical reactors. This Special Issue will be especially dedicated to these topics, but many other new applications will also be considered. The process of MT with a chemical reaction should also be investigated. It is of key importance to develop new and reliable measurement techniques for more accurate estimation of both the local bubble diameters and local gas holdups. New concepts for a better characterization of the liquid turbulence in gas–liquid reactors are also needed. It is especially important to have new visualization techniques in order to study the eddy lengths and bubble wakes. Their size and movement is important for MT enhancement. Contributions focused on these topics are welcome in this Special Issue.

Prof. Dr. Mark Hlawitschka
Prof. Dr. Stoyan Nedeltchev
Guest Editors

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Keywords

  • gas–liquid reactors
  • hydrodynamics, mixing, mass transfer (MT) and heat transfer
  • computational fluid dynamics
  • liquid turbulence in gas–liquid reactors
  • bubble wakes
  • visualization

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Published Papers (1 paper)

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Research

11 pages, 2165 KiB  
Article
Rim Driven Thruster as Innovative Propulsion Element for Dual Phase Flows in Plug Flow Reactors
by Maximilian Lackner, Alexander Löhr, Felix Schill and Martin Van Essche
Fluids 2024, 9(7), 168; https://doi.org/10.3390/fluids9070168 - 22 Jul 2024
Cited by 1 | Viewed by 1358
Abstract
The purpose of this work was to test a new setup to pump water with entrained air for application in gas fermentation. A mixed flow, where gas is contained in a liquid to be pumped, rapidly reduces the efficiency of a conventional pump, [...] Read more.
The purpose of this work was to test a new setup to pump water with entrained air for application in gas fermentation. A mixed flow, where gas is contained in a liquid to be pumped, rapidly reduces the efficiency of a conventional pump, due to the compressibility of the gas. It is not always possible to degas the fluid, for instance in gas fermentation, which is preferably carried out in tubular reactors (loop fermenters) to achieve a high conversion rate of the gaseous feedstocks. Method: In this work, a rim-driven thruster (RDT) was tested in a lab-scale, cold flow model of a loop reactor with 5–30% (by volume) of gas fraction (air) in the liquid (water) as alternative propulsion element (6 m total pipe length, ambient temperature and pressure). As a result, it was found that the RDT, in connection with a guiding vane providing swirling motion to the two-phase fluid, could pump a mixed flow with up to 25.7% of gas content (by volume) at atmospheric pressure and 25 °C and 0.5 to 2 m/s flow speed. In conclusion, an RDT is advantageous over a classic propulsion element like a centrifugal pump or axial flow pump for transporting liquids with entrained gases. This article describes the potential of rim-driven thrusters, as known from marine propulsion, in biotechnology, the chemical industry, and beyond, to handle multiphase flows. Full article
(This article belongs to the Special Issue New Perspectives in Gas–Liquid Reactors)
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