4.1.1. Fins
Fins represent a common method for enhancing the thermal conductivity heat transfer coefficient and achieving a faster solidification process in heat exchangers [
78,
79]. Their popularity stems from their simplicity, ease of manufacture, and cost-effectiveness [
80]. Fins are typically extended on the PCM rather than the HTF side to enhance efficiency [
42]. Fins facilitate heat transfer within these systems, and increasing their number and size can significantly enhance system performance [
43,
81,
82]. This assertion is supported by studies such as Hosseine et al. [
83], which propose that fin length is a critical parameter capable of augmenting absorbed energy and reducing melting temperatures. Additionally, Kalbasi and Salimbur [
84] observe that a greater number of fins can lead to a more uniform temperature distribution, optimizing the time required to reach peak temperature. Khan et al. [
85] corroborate these findings. Conversely, Al-Abidi et al. [
49] suggest that fin thickness, length, number, and the geometry of PCM units in Triplex Tube Heat Exchangers (TTHX), as well as TTHX material and Stefan number, are pivotal parameters for hastening PCM fusion. Tavakoli et al. [
86] and Mao et al. [
87] indicate that various geometric parameters can influence the PCM melting time, along with the TES model in which the fins are situated. However, Dinker et al. [
10] note that reducing the fusion time may inversely impact the overall system efficiency. Therefore, it is imperative to consider various parameters such as inlet temperature, shape, and HTF flow rate during the charging period to mitigate PCM melting time [
88,
89].
Fins can be manufactured in various shapes, including flat rectangular fins, rod-shaped fins, and other irregular configurations, as illustrated in
Figure 7. Research conducted by Zhang et al. [
71] indicates that longitudinal and annular fins have acquired the most attention in the past decade. However, helical and topologically optimized fins (depicted in
Figure 7d) demonstrate exceptional potential due to their superior performance compared to traditional fins. This observation suggests that fins can be further improved using various active and passive techniques for HTE.
Hosseini and Rahimi [
90] highlight in their research that the position and size of rectangular fins can significantly influence heat transfer distribution within energy storage systems. So, to have a shorter melting time of the PCM, one must consider these parameters in rectangular fins and possibly in other configurations. Amagour et al. [
91] present a three-dimensional numerical study of a fin-tube heat exchanger to assess HTE performance. The findings indicate that increasing the HTF (water) flow rate reduces both charging and discharging times. Conversely, elevating the HTF temperature accelerates the melting process by up to 30% when there is a 10 °C temperature difference between the HTF and the PCM; however, this also prolongs the solidification process.
Moreover, augmenting the number of fins decreases the heat transfer time and enhances the energy storage capacity. Nonetheless, the study suggests an upper limit to the number of fins for effective enhancement. Additionally, the authors recommend positioning the fins in the middle of the heat exchanger, increasing fin thickness, and using copper material, as these measures reduce the total melting time. In another study, Amagour et al. [
92] indicate that a minimum of 8 h of hot water is required for residential construction. Conversely, Chow and Lyu [
27] propose a minimum requirement of 18 h (from 7:00 am to 12:00 am) for residential applications.
Figure 7.
Different shapes of fins: (
a) branch-shaped fins [
78] (CC by 4.0); (
b) annular fins [
43] (CC by 4.0); (
c) rectangular fins [
93] (Copyright © 2013 Elsevier Ltd.); (
d) twisted fins [
94] (Copyright © 2013 Elsevier Ltd.); (
e) different fins of various researchers [
95] (CC by 4.0).
Figure 7.
Different shapes of fins: (
a) branch-shaped fins [
78] (CC by 4.0); (
b) annular fins [
43] (CC by 4.0); (
c) rectangular fins [
93] (Copyright © 2013 Elsevier Ltd.); (
d) twisted fins [
94] (Copyright © 2013 Elsevier Ltd.); (
e) different fins of various researchers [
95] (CC by 4.0).
Moreover, using copper strips shows promising potential for conduction HTE, thereby reducing melting time by 16% [
96]. Authors conducting numerical simulations employ various methods to analyze fins in heat storage systems, including the Finite Volume and Enthalpy-Porosity methods [
94].
Table 2 summarizes selected research studies employing fins as an HTE technique.
The literature review underscores the widespread utilization of rectangular fins for HTE across various applications. Their simplicity in design and low manufacturing complexity renders them highly favored. The findings of these studies highlight a significant potential for improving heat transfer in LHTESS. Notably, the methodology employed revealed a paucity of studies addressing the real-world application of hot water, with most being either numerical or laboratory-scale investigations. Consequently, a research gap exists regarding both simple and complex-shaped fins’ ability to enhance heat transfer in these systems. In addition to numerical analyses, experimental studies are imperative to validate the efficacy of this technique in HWGS. The outcomes of these studies underscore the pivotal role of the number of fins in LHTESS. While some studies suggest a progressive improvement in heat transfer efficiency with an increased number of fins, others indicate that this relationship has a finite range beyond which further enhancement ceases. Therefore, it is crucial to corroborate this information, as only numerical data are available on this aspect (see
Figure 8). Moreover, investigating the use of various fin shapes in LHTESS is essential, as it can explain which of the shapes studied in the literature yield superior results.
4.1.2. Turbulators
Turbulators represent passive methods characterized by spiral inserts elevating fluid velocity within tubes. Turbulators use discs, twisted tapes, wire coils, and others. Turbulators look like fins but differ in their twisted geometry [
104]. Typically composed of carbon steel, stainless steel, or copper, turbulators promote HTE and increase flow turbulence [
105,
106]. Research indicates that this method of heat enhancement surpasses the efficacy of using simple-shaped tubes in SWHS [
107]. The subsequent section outlines selected studies from the literature pertaining to this topic.
Twisted tapes and turbulators can potentially increase heat transfer and performance, contingent upon the type of solar collector employed. Nevertheless, this passive technique exhibits somewhat restricted applicability in hot water generation or solar collectors [
108,
109]. Jaisankar et al. [
110] undertook a study to investigate the impact of heat transfer from a collector enhanced with a helically twisted tape. Their findings revealed that using a helically twisted tape can elevate the heat transfer rate, pressure drop, and thermal efficiency by enhancing the tape’s solar radiation and twist ratio.
Li et al. [
94] conducted a similar study, only that they are called twisted fins or helical fins since these are located outside the tube through which the HTF (water) passes. In their numerical investigation, they examined the application of shell-and-tube-based heat storage with twisted fins to enhance the performance of this storage type. Their study encompassed various configurations of twisted fins, ranging from 0 to 4 fins positioned around the base tube, and was conducted in two orientations: vertical and horizontal. Their findings indicate that the configuration featuring three twisted fins enhances the melting time of the PCM in the vertical orientation, while in the horizontal orientation, the configuration with two twisted fins yielded the most favorable melting time. Consequently, the authors concluded that increasing the number of twisted fins does not necessarily correspond to a performance enhancement.
Not all researchers confirm the efficacy of turbulator-based enhancement methods. For instance, Hobbi et al. [
111] explored the influence of various passive devices (including twisted strips, coil-spring wires, and conical ridges) on a flat plate solar collector. Their findings suggest that these turbulence enhancement techniques fail to significantly increase heat transfer, as evidenced by the absence of discernible differences in the heat flow to the fluid.
The use of turbulators in LHTESS remains limited. Nevertheless, considering their association with fins, it represents an area warranting further investigation and expansion. The literature review reveals divergent viewpoints regarding the effectiveness of turbulators, which may stem from variations in methodology, collector size, or experimental setups adopted by researchers. The studies identified in this review primarily focused on systems employing tubes or solar collectors, as turbulators are commonly deployed to augment fluid velocity within the tubes. Notably, no explicit investigations were found about using coils in storage tanks. This presents a research opportunity to enhance HTF velocity within the coils, potentially improving the melting efficiency.
4.1.3. Porous Media (PM) or Foams
PCMs represent a promising avenue for enhancing energy efficiency and sustainability within systems. Researchers have explored various methodologies to augment thermal conductivity, among which the utilization of PM or metal foams stands out. These materials are favored for their robust, highly conductive, and permeable structures. The literature reveals a diversity of models, materials, pore densities, and porosities employed in fabricating foams or PM. However, the efficacy of this technique is compromised by the inherent natural convection of the material [
12,
44]. Moreover, numerous numerical methods are available for modeling this technique, with the Lattice Boltzmann method emerging as the most prevalent [
112,
113]. Alternatively, Habibishandiz et al. [
69] demonstrate several models capable of simulating velocity within the PM, including the Darcy model, Darcy–Forchheimer (DF) model, Darcy–Brinkman (DB) model, and Darcy–Brinkman–Forchheimer (DBF) model.
Majdi et al. [
114] indicate that incorporating PM within a tank can significantly extend the thermal storage duration compared to systems lacking such media. Furthermore, the thermal conductivity of PCMs can be substantially augmented through metallic foams, with copper foam exhibiting a 44-fold increase and aluminum foam exhibiting a remarkable 218-fold increase when configured with 89% and 71% porosities, respectively. Additionally, employing the impregnation method proves beneficial in minimizing empty pores within the PCM, thereby mitigating undesired thermal resistance [
76]. It is important to acknowledge that these enhancements may vary based on several factors inherent to the system; nonetheless, experimental investigations have demonstrated HTEs of up to 400% [
115,
116]. Conversely, Zhang et al. [
117] illustrate that the effectiveness of metallic foam in HTE is contingent upon factors such as porosity, pore density, and thermal conductivity.
The utilization of metallic foams in various applications has acquired significant interest. In a study by Xiao et al. [
118], two types of metallic foams, copper and nickel, were compared for their effectiveness in creating a composite PCM. Their findings revealed that the copper metal foam exhibited a superior enhancement in thermal conductivity compared to its nickel counterpart. Similarly, Aramesh and Shabani [
75] conducted a comparative analysis involving different setups: (a) no PCM, (b) pure PCM, (c) PCM with fins, and (d) PCM with metal foam in an evacuated tube solar collector. While the absence of PCMs (setup a) resulted in a higher outlet temperature, it lacked the energy storage capability observed in setups involving PCM (b, c, d). Notably, setup (d) incorporating PCM with metal foam exhibited a reduced temperature drop, enhanced heat storage, improved heat transfer performance within the tubes, and higher overall efficiency. Further investigations exploring the application of this technique can be found in
Table 3.
The remarkable thermal conductivity of metallic foams facilitates the solidification and melting processes of PCMs. However, choosing an appropriate position when placing the PCM is necessary, as this will allow for a more efficient heat transfer. This observation was only made in LHTESS with tubes. Regarding the application of this technique, few current studies validate the results in hot water generation, whether using solar collectors or storage tanks. Nevertheless, the collective evidence from reviewed studies consistently highlights the exceptional performance of copper metallic foams. Therefore, it is recommended to prioritize investigations focusing on copper metallic foams as a foundational starting point for future research endeavors in this domain.
Table 3.
Research about porous media in the literature.
Table 3.
Research about porous media in the literature.
Author | PCM/HTF | Porous Media | Type Study 3 | Focus Study | Results |
---|
Zhu et al. [65] | Paraffin wax 2 | Copper metal foam | N/E | Melting process | Increasing the proportion of metal foam decreased the melting time of the material. Heat storage rate increased. Enhanced thermal conductivity. Weakening of natural convection heat transfer because the metal foam restricts the natural convection of the PCM.
|
Zhu et al. [119] | Paraffin wax 2 | Copper metal foam | E | Melting process | |
Alam et al. [120] | n-eicosane/H2O | Copper metal foam | N | Solidification process | Decreased porosity in the PM can favor solidification by decreasing it, thanks to the thermal conductivity of PM. Performance improvements are observed during the discharging phase when using PM, particularly when the PCM is in direct contact with the HTF. Using the M-11 configuration has a solidification time reduction of up to 91.1% compared to M-1 ( Figure 9), but the cost can be high.
|
Wang et al. [121] | Paraffin wax 2 | Copper metal foam (Porosity 95%, pore density 5PPI) | E | Melting process | Increasing the PM proportion decreases the discharging time and temperature gradient. Heat storage rate and integrated heat transfer coefficient increased. Heat conduction plays an important role in this HTE method.
|
Yang et al. [122] | Paraffin/H2O | Open-cell metal foam | E | Melting process | Under the use of different inlet velocities, the efficiency of TES increased. Melting time was reduced by 64%, and there was better temperature distribution due to foam conduction.
|
Baruah et al. [123] | PCM 1,2 | Capsules of metal foam | N | Melting process | The metal foam can increase heat transfer and thus enhance the melting process. By reducing the capsule’s size and the metal foam’s porosity, a higher cover thickness is achieved, and thus, better melting time results are achieved.
|
4.1.4. Encapsulation
Encapsulation involves enveloping a material with a protective coating, which is crucial in LHTESS. Various types of coatings, including metallic, inorganic, and plastic, necessitate careful selection for optimal performance [
21]. Encapsulation serves several key purposes, including isolating the PCM from the external environment, preventing direct contact with the HTF, mitigating external volume change reactions, enhancing system efficiency, and augmenting the heat transfer surface [
85]. Different integration methods for PCM encapsulation exist, such as macroencapsulation (approximately 1 mm), microencapsulation (0–1000 μm), nanoencapsulation (0–1000 nm), immersion, and direct incorporation [
44,
72,
124]. While various PCMs can be encapsulated, paraffin wax and sodium acetate trihydrate are commonly employed in this context. Among the available encapsulation materials, plastic, aluminum, and stainless steel are frequently used for macroencapsulation [
125]. In contrast, although more intricate in manufacturing, microencapsulation offers superior heat transfer capabilities [
126]. Encapsulation with metallic materials like copper, aluminum, and steel presents an attractive option for enhancing thermal conductivity. However, it poses manufacturing challenges [
85].
Figure 10 illustrates diverse ways of PCM encapsulation.
Different parameters must be considered when encapsulating a PCM, as they can affect or enhance heat transfer. These parameters are the shell material, geometry, and core-to-coating ratio (decides the encapsulated PCM’s mechanical strength and thermal stability). Additionally, factors such as the Stefan number, the temperature range of the PCM, and the volumetric concentration of the microcapsule can exert a significant influence on heat transfer [
126]. One of the significant challenges associated with encapsulating materials is the risk of leakage. Therefore, conducting leakage analysis on the PCM during encapsulation is essential to ensure its reliability before deploying it in practical applications. Leakage analysis involves subjecting the encapsulated PCM to thermal cycling and thorough cleaning procedures to assess its integrity and performance [
127].
Microencapsulation presents an opportunity to improve the energy storage efficiency and enhance various thermal properties in direct absorption solar collectors [
128]. This is because there is no change in the velocity of water and microencapsulated PCM product of microencapsulation; a diameter of 5 μm is recommended to enhance the performance [
129]. Nanoencapsulation of PCM offers benefits such as improved thermal conductivity, leakage prevention, reduced overcooling, and increased suspension capacity at the melting temperature [
124,
130].
Certain investigations into cylindrical macroencapsulation have demonstrated its potential to increase energy storage density and prolong the storage duration. However, simply increasing the PCM amount does not necessarily improve the system’s thermal performance, as a critical threshold exists for PCM quantity [
131,
132]. In a study by Sun et al. [
133], an experimental–numerical analysis was conducted to evaluate the impact of integrating encapsulated PCMs into a water storage tank linked to four unglazed monocrystalline photovoltaic–thermal (PVT) modules. Their findings indicated a slight increase in average and overall electrical efficiency; however, the authors caution that alterations may influence these values in the flow rate.
Other studies have explored spherical encapsulation, such as the investigation by Nallusamy et al. [
15], who employed spherically encapsulated paraffin with high-density polyethylene in a hybrid storage system combining sensible and latent heat. Their findings indicated a faster discharge period, suggesting this hybrid system is well-suited for intermittent hot water discharge systems. In a separate study, Shin et al. [
77] compared elliptical and spherical capsules with the elliptical capsule, composed of polyethylene, aimed at enhancing heat transfer. The results demonstrated that the elliptical geometry could increase the Nusselt number by fivefold, reducing the charging and discharging times by 50% and 35%, respectively. Moreover, this experiment, conducted on a large scale, exhibited favorable charge and discharge times, suggesting its potential as a thermal battery.
PCM encapsulation is common in storage tanks, particularly for prolonged hot water generation. Macroencapsulation, owing to its affordability, has garnered significant attention, especially in mixed heat storage systems like LHTS-SHTS. However, real-world applications of encapsulation in solar collectors remain largely unexplored, predominantly confined to laboratory-scale investigations, thus presenting a promising avenue for future research. Additionally, exploring diverse macroencapsulation geometries can enhance heat transfer efficiency by augmenting the surface area for heat transfer. Nonetheless, while microencapsulation demonstrates promising outcomes, its high manufacturing cost poses a significant limitation, rendering it less accessible for LHTESS applications.
Furthermore, a techno-economic analysis was conducted to investigate the casing cost and encapsulation methods [
47]. Findings revealed that PCM encapsulated with aluminum alloy, titanium, and carbonate tubes offer a cost-effective solution for their deployment. Moreover, the overall cost of encapsulation is contingent upon the casing material and encapsulation technique employed, with due consideration to the minimal cost associated with PCM itself.
4.1.5. Geometry and Orientation Variation
The geometry and orientation of TES systems play a crucial role in determining their performance. Therefore, it is essential to select a geometry that ensures uniform temperature distribution within the TES system and to consider the container orientation, which can influence heat transfer [
85]. Various LHTS geometries are available, including circular, cylindrical shell and tube, rectangular, and triplex tube configurations (which consist of a cylinder with two tubes of different sizes inside, facilitating the exchange of HTF and PCM) [
6]. This method offers long-term viability compared to alternative techniques like nanoparticles and fins. Notably, the container’s inclination angle can impact melting and solidification rates [
134]. Additionally, the TES system can be enhanced by modifying the container geometry or the tubes through which the HTF flows.
Yan et al. [
135] conducted a numerical study investigating the impact of altering the shape of a cylindrical latent heat storage unit (CLHSU) on both the charging and discharging times.
Figure 11 illustrates the CLHSU before and after the geometry modification. The study focused on varying the wavelength (Lw) and wavelength amplitude (aw) to assess their effects on the charging and discharging times. Results indicated significant changes in the heat transfer coefficient and the velocity of PCM during these processes. During discharging, the heat transfer coefficient experienced a slight 2% decrease due to the corrugated wall but remained higher than that of the CLHU-S model.
Moreover, it was noted that the parameters Lw and aw played a minor role in the discharging process but had a more pronounced impact during charging. Additionally, Aggarwal et al. [
17] highlighted in their research the significance of the tilt angle of evacuated tube solar collectors (ETSCs) in enhancing effectiveness and cost efficiency across different geographical regions. Thus, it is imperative to consider this factor when planning the installation of a HWGS based on the specific location of the study.
Although the numerical investigation conducted by Quitiaquez et al. [
136] focuses on enhancing heat transfer within a solar collector/evaporator primarily used in heating systems, it reveals a notable improvement in heat generation when modifying the cross-section of the tubes, as illustrated in
Figure 12. As a result, alternative geometries are being considered for HWGS. However, an economic analysis is imperative to determine whether this enhancement is economically viable for enhancing system performance. Additionally, experimental validation is essential to ascertain whether altering tube or storage tank geometry can enhance efficiency and reduce the charging and discharging times of LHTESS.
4.1.6. Composite Phase Change Materials (CPCMs)
CPCMs are favored for energy storage due to their exceptional thermal conductivity, low cost, enhanced productivity, chemical stability, corrosion resistance, and thermal diffusivity [
81]. Certain CPCMs incorporate nanofillers like graphite, graphene oxide (GO), and hexagonal boron nitride (HBN), which significantly augment the thermal properties of the PCM, thereby benefiting solar energy storage systems [
137]. Additionally, CPCMs with additives or nanoparticles such as expanded graphite (EG) and carbon fiber (CF) exhibit favorable thermochemical properties, high thermal conductivity, and remarkable heat storage capacity [
44].
Nanoparticles, characterized by their dimensions smaller than 100 nm, exhibit thermal conductivity influenced by several factors such as concentration, temperature, particle size, pH, shape, material composition, and potentially the manufacturing process [
1]. The literature highlights diverse methods for synthesizing nanoparticles from disposable materials, as delineated in
Table 4. However, exploring the feasibility of producing nanoparticles from waste materials remains relatively unexplored. Conversely, limited research delves into the cost-effectiveness of incorporating nanoparticles in PCM preparation, particularly regarding implementation expenses for specific applications. While some studies demonstrate the enhancement of PCM thermal conductivity by adding expanded graphite or graphite nanoparticles, it is noteworthy that this augmentation affects thermal conductivity, melting time, and overall thermal performance positively [
138,
139,
140].
D’Oliveira et al. [
141] demonstrated the capacity of highly conductive nanoparticles to augment the thermal conductivity of PCM with low melting temperatures (ranging from 20 to 70 °C). The literature underscores the potential of carbon-based nanoparticles to supplant conventional metallic nanoparticles due to their commendable stability and ability to enhance PCM thermal conductivity [
45,
147,
148]. In comparison, H.M Teamah and M. Teamah [
149] agree on carbon-based nanoparticles but indicate that metallic foams are also strong candidates. In a study by Cabeza et al. [
150], a CPCM comprising 10% volume of graphite and 90% volume of sodium acetate was investigated for hot water generation. Their findings revealed that employing this CPCM could extend the duration of hot water availability, contingent upon the number of bottles used. Although their study assessed 2, 4, and 6 bottles, it clarified that the energy storage density surged to 40%, 57.2%, and 66.7%, respectively.
In contrast, Xie et al. [
151] present a study demonstrating the feasibility of utilizing environmentally sustainable materials in creating CPCMs. They employed coconut shell charcoal (CSC) as the primary material in their investigation. Focused on optimizing the PCM charging process, they augmented the PCM with CSC, modified the supporting material (H
2O
2), and evaluated its thermal characteristics in domestic solar energy applications. Their findings revealed that the CPCM exhibited a nearly threefold increase in thermal conductivity compared to non-CSC variants. Moreover, the CPCM displayed altered phase change temperatures, reduced latent heat, and improved efficiency. Furthermore, they evaluated the material’s performance in a tankless solar water heater, demonstrating its ability to store energy for subsequent use after sunset effectively. Additional significant studies are cataloged in
Table 5.
This approach can be combined with other methodologies like microencapsulation, thereby augmenting the thermal characteristics of the PCM and promoting uniform temperature dispersion [
157]. The utilization of CPCMs is highly prevalent in hot water generation. Consequently, there is a proposition to fabricate CPCMs incorporating nanoparticles sourced from both organic and inorganic waste materials. Despite the extensive literature review, only limited instances of CPCMs formulated from organic waste have been identified. Moreover, no numerical or experimental studies have been encountered that validate their application in LHTESS.
It is important to acknowledge that this observation might stem from the relatively low conductivity of these materials, unlike the case with metallic nanoparticles. However, this inference remains speculative due to the absence of supporting studies. A thorough examination of the literature reveals that most authors have primarily combined nanoparticles with paraffin waxes. This highlights a potential way for further investigation to explore the utilization of nanoparticles with alternative PCMs. Such exploration could yield significant advancements in properties and heat transfer mechanisms.
4.1.7. Multiple PCMs (M-PCMs) or Cascade LHTES System
TES systems employing M-PCMs offer a promising solution to mitigate thermal distortion during the charging and discharging phases. Numerous studies suggest that these systems can significantly improve efficiency and expedite charging processes, contingent upon the specific thermal properties of the PCMs used, such as the phase change temperature, latent heat, thermal conductivity, and mass ratio [
158,
159]. Therefore, carefully selecting materials is imperative to realize performance enhancements [
160]. This advancement can potentially optimize heat transfer during latent heat storage periods, offering superior efficiency and flexibility in energy storage and delivery [
160,
161,
162]. The position of PCMs within the system is dictated by their respective melting temperatures, as illustrated in
Figure 13. As depicted in
Figure 13a, for heat storage, PCMs should be positioned in decreasing order along the flow direction of the HTF, while during discharge, the HTF flows in the opposite direction [
158].
Figure 13b showcases various shapes applicable to U-tube TES systems, demonstrating potential up to 30% enhancements in the charging process [
163].
Paraffin waxes (such as paraffin wax, RT60, and others) and fatty acids (including myristic acid, stearic acid, lauric acid, and others) are commonly used for energy storage. Moreover, several studies have carried out investigations using two to five PCMs to achieve expedited charging and discharging cycles and heightened thermal storage efficiency [
48]. However, it is worth noting that a study suggests a limit of three stages, as stages after this threshold produce negligible performance improvements [
164].
One notable study employing this technique is conducted by Wang et al. [
165], wherein an experimental investigation involving a cylindrical capsule with three distinct PCMs (stearic acid, paraffin, and lauric acid) demonstrates that employing a cascade system can augment both the charging period and velocity. Similarly, Mazman et al. [
166] explore the utilization of three CPCMs (paraffin–palmitic acid, paraffin–stearic acid, and stearic acid–myristic acid) and report favorable outcomes regarding the average water temperature throughout the full charging cycle of a storage tank. They note that during the tank’s complete discharging phase, the average water temperature remains below the PCM’s flow temperature, with the stearic acid–paraffin CPCM exhibiting superior thermal performance. Conversely, Lim et al. [
167] show findings from their experimental study, highlighting a 28% increase in thermal performance when employing two distinct PCMs within a storage unit compared to just using one.
Khor et al. [
168] investigated the charging process of three different PCMs configurations, revealing a reduction in charging time with this setup. Their findings underscore an effective arrangement for positioning various PCMs within a LHTESS. Conversely, Pu et al. [
169] conducted a numerical study, corroborated by experimental validation, to assess whether employing M-PCMs could augment heat transfer efficiency and expedite PCM melting. Their investigation employed a shell-and-tube TES unit featuring three PCMs arranged radially alongside copper foam. A comparison was drawn with the utilization of a single PCM. Contrary to expectations, the results indicated that employing M-PCMs did not yield significantly higher HTE compared to using a single PCM. Additionally, the authors suggested optimizing thermal performance by adjusting the porosity distribution within the copper foam.
In this technique, careful PCM selection is imperative, as the integration of cascading PCMs that do not contribute to smooth heat transfer may adversely impact the system’s HTE. Hence, consideration of the thermal properties of the PCM is vital in this regard. It is noteworthy that, for the effective implementation of this method, PCMs with phase change temperatures not surpassing 60 °C are recommended. However, this recommendation depends on the prevailing climatic conditions in the desired hot water generation setting, as it necessitates a progressive phase change within the system. Numerous experimental studies validating HTE were identified for this technique, involving blending various PCMs such as fatty acids and paraffin waxes or using only paraffin waxes. Furthermore, it was observed that while this technique is commonly employed in TES tanks, it is less prevalent in solar collectors or shell-and-tube TES units. Determination of the optimal quantity of PCM modules for this technique is crucial, as divergent opinions exist regarding the maximum amount of PCMs to be employed.
4.1.8. Coils
Based on previous observations, researchers tend to prioritize the augmentation of surface area in storage systems. Hence, one viable approach is adopting coil or spiral/helical tube configurations. Such arrangements can potentially improve system performance, elevate energy efficiency, and decrease the PCM’s melting duration [
170].
Based on the investigation conducted by Rogowski and Andrzejczyk [
95], various research studies are delving into the coil geometry to augment the solidification and melting characteristics of PCMs. Primarily experimental, these studies predominantly focus on low-temperature PCMs, commonly employed in hot water generation.
Figure 14 illustrates some examples of used coils, while
Table 6 presents a compilation of research efforts concerning coil utilization in LHTESS.
This approach circumvents health concerns by averting direct contact between the PCM or any fluid and the HTF within LHTESS. Its applicability extends to SHTS systems, ensuring the storage material remains isolated from the HTF. Multiple experimental investigations in this methodology corroborate its efficacy in enhancing heat transfer, albeit most of these studies are conducted at the laboratory scale. Therefore, validating this technique for hot water generation in real-world scenarios is advisable to ascertain its potential for efficiently improving heat transfer in such systems.
4.1.9. Nanofluids
Nanofluids offer distinct advantages in solar systems or collectors compared to traditional fluids. They can augment heat transfer rates and find utility across various applications [
171,
172]. Nanofluids are derived from nanoparticles (Al, Au, Ag, Cu) with sizes below 100 nm dispersed in water or other fluids [
173]. Hybrid nanofluids are also prevalent, containing two types of nanoparticles within a fluid. Employing stable hybrid nanofluids with reduced viscosity and heightened thermal conductivity can elevate the efficacy of solar collectors [
1]. These fluids serve as a potential alternative to enhance heat transfer efficiency in PCMs, alter thermal conductivity, boost the effectiveness of heat storage systems, or serve as substitutes for HTF [
106,
174]. Nanofluids can be integrated with other methodologies like encapsulations or used independently to amplify the thermal performance of solar collectors [
1,
108,
175,
176,
177].
Table 6.
Use of coil in latent heat storage systems according to the literature.
Table 6.
Use of coil in latent heat storage systems according to the literature.
Author | Type of Study 1 | Overview |
---|
Kabbara et al. [42] | E | The system’s performance was analyzed by incorporating a helical coil into a storage tank with lauric acid PCM. Temperature variations were notable during charging and discharging. However, the authors emphasize the need to explore different coil geometries and flow rates to fully grasp the system’s dynamics. |
Anish et al. [178] | E | Using a double helix coil consisting of a tube, a significant difference in the temperatures of the top and bottom of the tank was obtained in the melting process. Moreover, the solidification process occurred uniformly in the tank. |
Korti and Tlemsani [179] | E | Using a copper helical coil with various PCM types, charging temperatures and flow rates revealed a higher efficiency during the charging process compared to discharging. This discrepancy is due to convection dominance during melting. Additionally, charging temperatures notably impacted the results. |
Dinker et al. [180] | E | A study was conducted in a rectangular storage tank with PCM (beeswax) and HTF (water) flowing in a helical coil with different temperatures and flow rates. Their results show that temperature can significantly influence the efficiency of the solidification and melting processes. |
Saydam et al. [181] | E | A study investigated the solidification and melting processes of a PCM (Paraffin wax) in a storage tank with a helical coil. Findings revealed faster melting of the PCM on the tank’s periphery and slower near the axis during both processes. However, the authors suggest adding more coils at the tank’s bottom for improved discharge efficiency. It was found that the flow direction of the HTF (ethylene glycol (EG)–water mixture) had a negligible impact on the charging and discharging period but did influence the temperature fluctuations of the PCM within the energy storage unit. |
Rahimi et al. [182] | E | The impact of charging temperature on the coil storage tank’s performance was assessed alongside the introduction of a dimensionless parameter known as the Stefan number. The findings indicate that a specific Stefan number can decrease the PCM’s melting time. |
Using nanofluids in solar systems offers several advantages, including reducing the required heat transfer area, high density, conductivity, and thermal properties, along with favorable optical characteristics and stability [
183]. When combined with PCMs possessing good HTE and thermal stability, nanofluids can extend operational time and decrease energy consumption [
184]. However, their main disadvantages include high costs, thermal instability, chemical compatibility issues, and complexities in the manufacturing process [
183]. Over the years, nanofluid technology has advanced, as depicted in
Figure 15 and
Figure 16, showcasing the diverse fluids and nanoparticles used in preparing nanofluids or hybrid nanofluids. Commonly employed nanoparticles in solar collectors encompass CeO
2, SiO
2, Al
2O
3, CuO, graphene, and TiO
2 [
4,
17,
108,
185]. Additionally, carbon-based nanomaterials exhibit superior thermal conductivity for such applications [
141,
176]. Nonetheless, a primary challenge lies in selecting appropriate nanoparticles and fluids for specific applications [
52]. Aggarwal et al. [
17] have demonstrated that PCMs and nanofluids can synergize to enhance heat transfer in solar water heaters, including evacuated tube solar collectors (ETSCs) and flat plate solar collectors (FPSCs), leveraging the manifold advantages offered by nanofluids.
Figure 17 displays various models for simulating nanofluids, with the mixture model being the most prevalent due to its ability to simulate different velocities across phases and its applicability in interpenetrating phases [
186]. Solar collectors are commonly used for low-temperature systems, particularly in hot water generation [
187].
Figure 18 showcases examples of solar collectors in the literature, providing insight into where nanofluids have been employed for enhancement. Subsequently, this paper will outline research conducted with nanofluids in solar collectors, structured into three sections to facilitate comprehension.
Using PCMs in FPSCs can extend hot water availability and enhance system efficiency. However, outcomes are contingent on factors such as the degree of inclination, PCM–collector contact, solar radiation, and thermal stratification in the storage tank [
191]. FPSCs are frequently employed in research due to their accessibility and affordability, leading to numerous studies aimed at improving heat transfer (via nanofluids), maintaining stable temperatures (with PCMs), or enhancing system thermal capacity (through nanofluid–PCM integration) [
177,
184].
Table 7 presents a selection of studies conducted with FPSCs.
- 2
Evacuated tube solar collectors (ETSCs)
ETSCs feature parallel tubes designed to withstand reflection and absorb high solar radiation with specialized glass coatings, enhancing efficiency, thermal conductivity, and energy storage [
177,
195]. Hence, they are extensively employed in domestic applications [
196]. As of 2020, thermosyphon-type ETSCs are the most commonly utilized [
183].
Table 8 showcases notable studies conducted with ETSCs.
- 3
Photovoltaic–thermal collectors
Kezemian et al. [
197] conducted a 3D numerical study to enhance solar collector performance using various hybrid nanofluids: MWCNT–aluminum oxide, MWCNT–silicon carbide, graphene–aluminum oxide, and graphene–silicon carbide. Their findings reveal that the MWCNT–silicon carbide hybrid nanofluid exhibits superior electrical and thermal energy efficiency compared to others. Similarly, Khodadadi and Sheikholeslami [
198] demonstrated that incorporating nanoparticles such as MWCNT, SiC, Cu, Ag, Al
2O
3, and ZnO in water and PCM boosts the charging rate while marginally reducing unit and coolant temperatures. Additionally, they observed changes in the PCM’s liquid fraction with alterations in the system’s flow rate.
Table 8.
Studies on the use of nanofluids in evacuated tube solar collectors.
Table 8.
Studies on the use of nanofluids in evacuated tube solar collectors.
Author | Nanofluid Based on | Type of Study 1 | Results |
---|
Tabarhoseini et al. [199] | Nanoparticles of CuO/pure H2O | N | - ▪
Irreversibility of heat transfer caused sudden increases in fluid viscosity and pressure change. - ▪
Nano-sized powders within the fluid are suspended. - ▪
Entropy generation decreased by 6.3% with the use of nanofluids.
|
Ghaderian et al. [200] | Nanoparticles of CuO/H2O | E | - ▪
At a volume concentration of 0.05% of nanoparticles and a flow rate of 60 l/h, efficiency increased by 51.4%. This boost stemmed from heightened thermal conductivity attributable to the nanoparticles’ high density.
|
Al-Mashat and Hasan et al. [201] | Al2O3/water | N/E | - ▪
If the volume fraction of Al2O3 increases, the efficiency can increase proportionally. - ▪
The recommended angle of inclination of the evacuated tube is 41° annually.
|
Eltaweel et al. [196] | MWCNT/water | E | - ▪
Increased flow rate and nanofluid concentrations can increase efficiencies.
|
Mahbubul et al. [202] | Single-walled carbon nanotubes (SWCNT)/water | E | - ▪
Efficiency increased by almost 10%.
|
Daghigh and Zandi [203] | water/TiO2, water/CuO and water/MWCNT | T/E | - ▪
A nanofluid composite with MWCNT nanoparticles obtained a higher performance increase.
|
Kumar and Kaushal [204] | Nanoparticles of graphene- ethylene glycol/water | E | - ▪
Variations in graphene concentrations revealed a proportional increase in thermal conductivity and efficiency, particularly evident when fluid inlet temperature aligns with ambient conditions.
|
Ghaderian and Sidik [205] | Al2O3/distilled water | E | - ▪
The collector’s efficiency rises with nanofluid use, further increasing with higher volume fractions of nanoparticles.
|
In conclusion, passive methods, including nanofluids, encapsulation, fins, M-PCMs, and porous media, are deemed most effective for hot water generation applications. Among these, fins are considered practical, especially with simple configurations during system installation. Additionally, M-PCMs are seen as advantageous when proper PCM selection is used. These techniques are commonly employed due to their low costs, except for nanofluids, which incur higher manufacturing costs. However, it is essential to note that the literature does not have data on the construction, creation, or operational costs of these methods in energy storage systems; thus, our perspective is solely based on selected document readings.