Submitted:
06 June 2025
Posted:
09 June 2025
You are already at the latest version
Abstract
Keywords:
1. Introduction
2. Thermal Energy Storage Technology (TES)
3. Operational Processes of Phase Change Materials (PCMs)
3.1. Integration of Phase Change Materials
3.2. Fundamental properties of Phase Change Materials
3.3. Advanced Incorporation Techniques for Phase Change Materials
3.3.1. Direct Incorporation Methods of Phase Change Materials
3.3.2. Impregnation Technique for PCM
3.3.3. Encapsulation Technique for PCM
3.3.4. Stabilization Techniques for Phase Change Materials
3.4. Change Materials: A Sustainable Approach for Heating and Cooling in Buildings
4. Phase Change Materials: Addressing Drawbacks and Potential Enhancements
5. Commonly Adopted Fundamental Assumptions in Leading Research Studies
- Liquid PCM is considered an incompressible and Newtonian fluid.
- Natural convection of liquid PCM is neglected.
- PCM envelope layers are assumed thin and with high thermal conductivity to overlook its thermal resistance.
- Volume change during solid-liquid phase change, heat loss from the TES, and radiative heat transfer are neglected.
6. Ground-Breaking Insights and Practical Recommendations
- Improve thermal inertia of the wall, delay heat transfer, and stabilize indoor temperatures.
- Improve energy efficiency, thereby reducing heating and cooling requirements.
- Reduce greenhouse gas emissions by reducing reliance on mechanical HVAC systems.
- Promote waste recovery by incorporating organic by-products into building materials.
6.1. Spent Coffee Grounds as PCM
6.2. Hybrid Composite
7. Outlook and Emerging Trends for Future Research
- Temperature range suitability
- Appropriate PCM selection for each application
- Efficient heat transfer during charge and discharge cycles
- Managing leakage problems
- Stability and sustainability of PCMs
- Improved thermal conductivity
- Strategic location for optimal efficiency
8. Conclusions
Author Contributions
Funding
Data Availability Statement
Acknowledgments
Abbreviations
| Abbreviations | |
| DSC | Differential Scanning Calorimeter |
| DTG | Derivatives Thermogravimetric machine |
| EG | Expanded Graphite |
| EP | Expanded Pearlite |
| EV | Expanded Vermiculate |
| FSPCM | Foam stabilised PCM |
| FTIR | Fourier Transform Infrared Spectroscopy instrument |
| GDP | Gross Domestic Product |
| HVAC | heating, ventilation, and air conditioning |
| LHS | Latent heat storage systems |
| LTES | Latent Thermal Energy Storage |
| MUFA | Monounsaturated Fatty Acids |
| PCM | Phase Change Materials |
| PUFA | Polyunsaturated fatty acids |
| PVT | Photovoltaic-thermal system |
| SCG | Spent Coffee Grounds |
| SDG | Sustainable development goals |
| SFA | Saturated Fatty Acids |
| SHS | Sensible heat storage |
| SSPCM | Shape stabilized PCM |
| TES | Thermal Energy Storage |
| TG | Thermogravimetric machine |
| ZEB | Net Zero Emissions in Building |
| Nomenclature | |
| Cp | Specific heat capacity (kJ/kg.K) |
| K | Thermal conductivity (W/m.K) |
| Tm | Melting temperature(ºC) |
| W0 | Weight of extracted oil (g) |
| Wd | Weight of the dried SCGs (g) |
| α | Thermal expansion coefficient |
| ΔH | Latent Heat for fusion (kJ/kg) |
| ρ | Density (kg/m³) |
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| Types of TES | Functional | Phases |
|---|---|---|
| Sensible heat | *Associated with the temperature rise, until the initialization of PC. *Classified to storage in medium media. |
L/S |
| Latent heat | *Higher energy storage density associated with PC. *Sustains a small difference in temperature between the release and storage of heat. |
L – S S – S L–G |
| Thermochemical heat | *Due to the shifting of equilibrium by P and T changing, a large amount of chemical energy is absorbed and released. | L– G S – G G – G |
| PCM | Advantage | Weaknesses |
|---|---|---|
| Organic |
|
|
| Inorganic |
|
|
| PCM | Melting point (ºC) | Heat of fusion (kJ/kg) |
Thermal conductivity (W/m.K) |
Density (kg/m³) | Specific heat (kJ/kg.K) |
|---|---|---|---|---|---|
| (L/S) | (L/S) | (L/S) | |||
| Paraffin | 27-29 | 245 | 0.2 (L) | 770/880 | 2 (L) |
| Bio-PCM | 28.85 | 219 | 0.2/0.2 | 860/860 | 1.97/1.97 |
| OM32 | 31.85 | 200 | 0.145/0.219 | 870/928 | 2.3/1.95 |
| Pure-Temp 23 | 22.23–24.17 | 170.71 | 0.15/0.25 | 830/910 | 2.06/1.56 |
| OM35 | 35 | 160 | 0.16/0.2 | 870/900 | 2.71/2.31 |
| Eicosane | 36–38 | 202 | 0.15/0.39 | 780/815 | 2.46/1.92 |
| Paraffin wax | 44 | 174.12 | 0.13 (L) | 783/830 | 2.53/2.44 |
| Paraffin PT 27 | 28 | 147 | 0.2 (L) | 750/870 | - |
| OM37 | 26–29 | 218 | o.13 (L) | 860 | - |
| HS29 | 26–29 | 190 | 0.55/1.05 | 1530/1681 | 2.62 (L) |
| GR27 | 28 | 72 | 0.15 | 710 | 1.125 |
| Water | 0 | 334 | 0.6 | 1000 | 4.179 |
| PCM | Melting temperature(ºC) | Heat of fusion(kJ/kg) | Thermal conductivity(W/m.K) | Density (kg/m³) |
| Paraffin L/S | ||||
| n-Heptadecane | 19 | 240 | 0.21 | 777 |
| Paraffin C17 | 21.7 | 213 | 0.2 | 817/754 |
| ParaffinC13-C24 | 22-24 | 189 | 0.21 (L) | 760/900 |
| Paraffin RT-27 | 28 | 179 | 0.2 | 800 |
| Paraffin RT-18 | 15-19 | 134 | 0.2 | 756 |
| Paraffin C18 | 28 | 244 | 0.148 (L) | - |
| n-octadecane | 28 | 179 | 0.2 | 750/870 |
| Fatty acids | ||||
| Capric Acid- Palmitic Acid | 26.2 | 177 | 2.2 | 784 |
| Capric Acid | 30 | 142.7 | 0.2 (L) | 815 (L) |
| Capric Acidand1 - dodecanol | 26.5 | 126.9 | 0.12(S) | 752 (S) |
| MeP + MeS | 23 -26.5 | 180 | 0.2 (L) | 817 (L) |
| Butyl Stearate - Palmitate | 17 - 20 | 137.8 | 0.12 (S) | 754 (S) |
| Eutectic Capric Acid – Myristic Acid | 21.7 | 155 | ||
| Eutectic Capric Acid – Stearic Acid | 24.7 | 179 | ||
| Capric Acid – Lauric Acid | 19.2- 20.3 | 144- 150 | - | 550 |
| Glycerin | 17.9 | 198.7 | - | - |
| Lauric Acid – Myristic Acid – Stearic Acid / Expanded Graphite | 29.05 | 137.1 | - | - |
| Capric Acid -Palmitic Acid – Stearic Acid | 19.93 | 129.4 | ||
| Myristic Acid – Palmitic Acid Stearic Acid/Expanded Graphite | 41.64 | 153.5 | ||
| Constructive localization |
Method of PCM integration |
Constructive solution |
Temperature transition of PCM (°C) | Most Relevant Conclusions |
|---|---|---|---|---|
| Walls | Immersion | Gypsum Boards | 50 | Cost reduction of the energy consumed by HVAC systems, aiming to minimize peak electricity demand. |
| 20 | The system assisted in decreasing the temperature to its maximum level and rise it to the minimum level. |
|||
| Microencapsulation | Gypsum Boards | 22 | Relatively low changes in temperature. | |
| 18 | Enhanced performance of the PCM was obtained when placed close to the surface of the gypsum board, which resulted in an increase in the minimum temperature. | |||
| Concrete | 22 | Air temperature reduction and lagging latency. | ||
| 25 | Enhanced thermal inertia and heat efficiency. | |||
| Bags | 34 | The bags reduce the peak demand period of the heat. | ||
| Mortar | 24 | Increase of the minimum temperature and decrease of the maximum temperature along with reduction in the cooling and heating requirements and lag time delay. |
||
| Macroencapsulation | Brick | 35 | The system can reduce heat flux and inner temperature | |
| 25 | Reduction of the electricity utilization along with decrease in the highest temperature and daytime thermal gradients. | |||
| Panels | 30 | Enhanced energy storage capacity. | ||
| 21 | Decrease of the temperature intensity. | |||
| Microencapsulation (Hybrid solution) | 10, 24, 26 and 28 | Greater thermal amplitude attenuation. | ||
| Ceiling | Macroencapsulation | Metallic panel | 46 | Reduction of the cooling load and thermal flow. |
| 22 | Grater internal temperature control system. | |||
| Shape-stabilization |
Ceiling | 21 | Energy conservation during daylight hours. | |
| Concrete | 26 | Increase of the minimum temperature and decrease of the maximum temperature | ||
| Microencapsulation | Panels | 18 | Decrease in volume flows. | |
| Macroencapsulation (Hybrid solution) | Metallic panels | 26-28 | Reduction of the interior temperature fluctuation and improvement of the thermal comfort | |
| Floor | Macroencapsulation | Concrete | 20 | Extended periods at constant temperature. |
| 23 | Increase of the minimum temperature and decrease of the maximum temperature. | |||
| Shape-stabilization | Boards | 52 | Increase of the temperature inside without increasing the temperature gradient. | |
| Macroencapsulation (Hybrid solution) |
Panels | 14, 16, 18, 20, 22, 30, 34, 38, 42 and 46 | Decrease in surface temperatures variability as well heat flows. | |
| Glazed | Macroencapsulation | Shutter system | Maintaining the internal temperature at a consistent level. | |
| Macroencapsulation (Hybrid solution) | - | 18, 26 and 32 | Thermal efficiency enhancement of the glazed unit when incorporating PCM. |
| Thermo-physical properties | Kinetic properties | Chemical properties | Economic and environmental properties |
|---|---|---|---|
|
|
|
|
| Sample | Components | Absorbed PCM (wt%) | Thermal conductivity (W/m.K) | Melting temperature (°C) | Melting latent heat (J/g) |
|---|---|---|---|---|---|
| Base PCM | Hydrogenated palm kernel vegetable fat (HPKVF) | - | 0.2 | 26.53 | 74.35 |
| Composite PCM | HPKVF +cellulose fibers +natural clay +graphite | 53 | 0.86 | 27.33 | 40.27 |
| Base PCM | Coconut oil | – | 0.182 | 22.63 | 106.17 |
| Composite PCM | Coconut oil +50 % cellulose fibers +50 % natural clay +10 % graphite | 44 | 0.53 | 23.73 | 46.70 |
| Coconut oil +42 % cellulose fibers +33 % natural clay +25 % graphite | 46 | 0.71 | 23.66 | 48.39 | |
| Coconut oil +0.38 % cellulose fibers +31 % natural clay +31 % graphite | 55 | 0.81 | 23.57 | 58.03 | |
| Coconut oil +29 % cellulose fibers +29 % natural clay +42 % graphite | 56 | 1.06 | 23.79 | 59.10 | |
| Base PCM | Non-cocoa vegetable fat | – | 0.2 | 34.94 | 108.83 |
| Composite PCM | Non-cocoa vegetable fat +cellulose fibers +natural clay +graphite | 56 | 0.83 | 34.83 | 62.39 |
| Composite PCM | Core (palmitic acid) +shell (polylactic acid) micro encapsulated PCM | 24.3 core content | - | 61.9 | 40.7 |
| 35.8 core content | - | 62.3 | 59.9 | ||
| 41.9 core content | - | 62.1 | 70.1 | ||
| Base PCM | Beeswax | - | - | 62.28 | 141.49 |
| Composite PCM | Beeswax +3 % graphene | - | 2.8 | 62.42 | 186.74 |
| Base PCM | Stearic acid | - | 0.16 | 69.23 | 208.16 |
| Composite PCM | Stearic acid +carbonized maize straw | 77.22 | 0.3 | 67.62 | 160.74 |
| Base PCM | Capric-stearic acid | - | 0.19 | 24.65 | 175 |
| Composite PCM | Capric-stearic acid +sugar beet pulp | 70 | 0.34 | 24.4 | 117 |
| Base PCM | Lauric-stearic acid | – | 0.228 | 37.5 | 199.6 |
| Composite PCM | Lauric-stearic acid +carbonized biomass waste corn cob | 77.9 | 0.441 | 35.1 | 148.3 |
| Acid | Tm (°C) | Hf (kJ/kg) | Cp(kJ/kg.K) | k (W/m.K) | ρ (kg/m3) |
|---|---|---|---|---|---|
| Enanthic | -7.4 | 107 | - | - | - |
| Butyric | - 5.6 | 126 | - | - | - |
| Caproic | -3 | 131 | - | - | - |
| Propyl palmiate | 10 | 186 | - | - | - |
| Pelargonic | 12.3 | 127 | - | - | - |
| Isopropyl stearate | 14-18 | 140-142 | - | - | - |
| Caprylic | 16 | 148.5 | - | 0.149 (l) | 862 (l) |
| 16.5 | 149 | 0.148 (l) | 1033 (s) | ||
| 981 (s) | |||||
| Butyl stearate | 19 | 140 | - | - | - |
| 123-200 | |||||
| Dimethyl sabacate | 21 | 120-135 | - | - | - |
| Undecylenic | 24.6 | 141 | - | - | - |
| Vinyl stearate | 27-29 | 122 | - | - | - |
| Undecylic | 28.4 | 139 | - | - | - |
| Capric | 31.5 | 153 | - | 0.149 (l) | 886 (l) |
| 32 | 152.7 | 0.153 (l) | 878 (l) | ||
| Tridecylic | 41.8 | 157 | - | - | - |
| Methyl-12 hydroxy-stearate | 42-43 | 120-126 | - | - | - |
| Lauric acid | 42-44 | 178 | 1.6 | 0.147 (l) | 870 (l) |
| 44 | 177.4 | 862 (l) -1007 (s) | |||
| Elaidic | 47 | 218 | - | - | 851 (l) |
| Myristic | 54 | 187 | 1.6 (s) | - | 844 (l) |
| 58 | 186.6 | 2.7 (l) | 990 (s) | ||
| 49-51 | 204.5 | ||||
| Pentadecanoic | 52-53 | 178 | - | - | - |
| Margaric | 60 | 172.2 | |||
| Palmitic | 63 | 187 | - | 0.165 (l) | 874 (l) |
| 61 | 203.4 | - | 0.159 (l) | 874 (l) | |
| 64 | 185.4 | - | 0.162 (l) | 850 (l) | |
| Stearic | 70 | 203 | 2.35 (l) | 0.172 (l) | 941 (l) |
| 69 | 202.5 | 848 (l) | |||
| 60-61 | 186.5 | ||||
| 69.4 | 199 | ||||
| Nonadecylic | 67 | 192 | |||
| Arachidic | 74 | 227 | - | - | - |
| Heneicosylic | 73-74 | 193 | |||
| Phenylacetic | 16.7 | 102 | |||
| Acetamid | 81 | 241 | - | - | - |
| PP-MAPP/Hemp/Wood Weight ratio |
Melting process |
Crystallization process |
||
|---|---|---|---|---|
| (wt.%) | Tm (°C) | ΔHm (kJ/kg) | Tc (°C) | ΔHc (kJ/kg) |
| 100:0:0 | 165 | 81 | 111 | 84 |
| 80:20:0 | 164 | 66 | 119 | 64 |
| 60:30:10 | 164 | 53 | 121 | 47 |
| 80:10:10 | 163 | 75 | 120 | 66 |
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