Identification of best available thermal energy storage compounds for low-to-moderate temperature storage applications in buildings

J. Lizanaa,*, R. Chacarteguib, A. Barrios-Paduraa, J. M. Valverdec, C. Ortizc

a. Escuela Técnica Superior de Arquitectura, Universidad de Sevilla (Seville, Spain)

b. Escuela Técnica Superior de Ingeniería, Universidad de Sevilla, (Seville, Spain)

c. Facultad de Física, Universidad de Sevilla, (Seville, Spain)

*flizana@us.es

 

ABSTRACT

Over the last 40 years different thermal energy storage materials have been investigated with the aim of enhancing energy efficiency in buildings, improving systems performance, and increasing the share of renewable energies. However, the main requirements for their efficient implementation are not fully met by most of them. This paper develops a comparative review of thermophysical properties of materials reported in the literature. The results show that the highest volumetric storage capacities for the best available sensible, latent and thermochemical storage materials are 250 MJ/m3, 514 MJ/m3 and 2000 MJ/m3, respectively, corresponding to water, barium hydroxide octahydrate, and magnesium chloride hexahydrate. A group of salt hydrates and inorganic eutectics have been identified as the most promising for the development of competitive thermal storage materials for cooling, heating and comfort applications in the short-term. In the long-term, thermochemical storage materials seem promising. However, additional research efforts are required.

 

RESUMEN

Identificación de los mejores compuestos disponibles de almacenamiento de energía térmica para aplicaciones de baja a moderada temperatura en edificación. En los últimos 40 años se han investigado diferentes materiales de almacenamiento térmico con el objetivo de mejorar la eficiencia energética en los edificios, mejorar el rendimiento de sistemas y aumentar el uso de renovables. Sin embargo, la mayoría no cumple los principales requisitos para su eficiente implementación. Este artículo desarrolla una revisión de las propiedades termofísicas de los materiales existentes en la literatura. Los resultados muestran que las mayores capacidades de almacenamiento volumétrico para los mejores materiales de almacenamiento sensible, latente y termoquímico son 250 MJ/m3, 514 MJ/m3 y 2000 MJ/m3, respectivamente, correspondientes a agua, hidróxido de bario octahidratado y cloruro de magnesio hexahidratado. Un conjunto de sales hidratadas y eutécticos han sido identificados como los más prometedores para el desarrollo de materiales competitivos para aplicaciones de enfriamiento, calefacción y confort a corto plazo. A largo plazo, el almacenamiento termoquímico parece prometedor. Sin embargo, investigación adicional es requerida.

 

Received 16 October 2017; Accepted 12 April 2018; On line first 27 June 2018

Citation/Citar como: Lizana, J.; Chacartegui, R.; Barrios-Padura, A.; Valverde, J.M.; Ortiz, C (2018) Identification of best available thermal energy storage compounds for low-to-moderate temperature storage applications in buildings. Mater. Construcc. 68 [331], e160 https://doi.org/10.3989/mc.2018.10517

KEYWORDS: Thermal energy; Characterization; Thermal energy storage materials; Phase change materials; Thermophysical properties.

Palabras clave: Energía térmica; Caracterización; Materiales de almacenamiento de energía térmica; Materiales de cambio de fase; Propiedades termofísicas.

ORCID ID: J. Lizana (http://orcid.org/0000-0002-1802-5017); R. Chacartegui (http://orcid.org/0000-0001-7285-8661); A. Barrios-Padura (http://orcid.org/0000-0003-1054-010X); J. M. Valverde (http://orcid.org/0000-0002-2345-8888); C.Ortiz (http://orcid.org/0000-0002-7795-676X)

Award-winning paper at III International Congress and V National on Sustainable Construction and Eco-Efficient Solutions (CICSE) March 2017

Copyright: © 2018 CSIC. This is an open-access article distributed under the terms of the Creative Commons Attribution 4.0 International (CC BY 4.0) License.


 

CONTENT

NomenclatureTOP

cp specific heat (KJ/kg K)
CSMP composite salt in porous matrix
DH district heating
h latent heat of fusion per unit mass (kJ/kg)
HVAC&R heating, ventilation, air conditioning and refrigeration
LHSM latent heat storage materials
m mass of heat storage medium (kg)
PCM phase change material
PEG polyethylene glycol
Q quantity of heat stored (MJ)
SHSM sensible heat storage material
T temperature (°C)
TABS thermally Activated Building system
TCA thermo-chemical accumulator
TCES thermochemical energy storage
TES thermal energy storage
TSM thermochemical energy storage material
UTES underground thermal energy storage
Greek letters
α thermal diffusivity (mm2/s)
λ thermal conductivity (W/m K)
ρ density (kg/m3)
Subscript
l liquid
s solid

1. INTRODUCTIONTOP

Over the last 40 years, a number of thermal energy storage and management technologies have been explored for a low-carbon energy transition in domestic and industrial sectors given their great potential to reduce energy demand, increase the use of renewable energy and improve the operating conditions of heating and cooling systems. Probably, thousands of pure materials and mixtures have been investigated for their use in thermal energy storage (TES) applications (1, 2). From the early publications of Abhat (3, 4), Lane (5), Telkes (6, 7), Schröder and Gawron (8) and Naumman and Emons (9) in the 1980s, until most recent works of Sharma et al. (10, 11), Cabeza et al. (12), Tyagi et al. (13, 14), Zhou et al. (15), N’Tsoukpoe et al. (16), Tatsidjodoung et al, Yu et al. (17), De Gracia and Cabeza (18), Kenisarin and Mahkamov (19, 20) and Alva et al. (21, 22), different types of thermal storage compounds have been considered, tested and listed as promising for low-to-moderate temperature applications. This includes liquid and solid materials for sensible storage, organic and inorganic materials, and their eutectic mixtures, for latent heat storage and thermochemical storage forms. For an efficient implementation of these systems, they should possess a high volumetric TES density with high thermal stability and reliability under cycling, as well as being widely present readily available at low cost (1). However, these requirements are not fully met by most existing materials.

The aim of this paper is to identify the best available TES compounds developed for low-to-moderate temperature storage applications. The work considers all existing and tested to our knowledge sensible, latent and thermochemical TES materials in the temperature range between 0 and 100 °C. The paper is structured as follows. First, heat storage methods and their main building applications are introduced. Afterwards, definition of characterization parameters and requirements of each storage method are provided. Most of the TES materials tested and reported in the literature are categorized, with special emphasis on their thermophysical properties. Finally, all the collected materials are compared, according to volumetric TES capacity and temperature applications, and the compounds with highest potential are identified.

2. CLASSIFICATION OF THERMAL ENERGY STORAGE MATERIALS AND THEIR BUILDING APPLICATIONSTOP

Thermal energy storage methods can be broadly classified as sensible, latent (phase change) and thermochemical. Figure 1 shows the main available material groups for each storage method in building applications.

Figure 1. Classification of thermal energy storage materials.

 

Sensible heat storage is just based on increasing or decreasing the temperature of a given material with high heat capacity. Sensible storage compounds are usually classified into liquids (such as water or oil) and solids (such as rocks, concrete, bricks, sand or gravel). Latent heat storage relies on the heat absorbed or released when a material undergoes a phase change from a physical state to another (15, 23). Phase change materials (PCMs) are classified into organics (paraffins, fatty acids, esters, sugar alcohols, polyethylene glycols and other), inorganics (salt hydrates and metals) and eutectics mixtures (mixtures of inorganics and/or organics) (4, 15). Thermochemical energy storage (TCES) is based on the use of a source of energy to induce a reversible chemical reaction and/or sorption process (17). Thermochemical storage materials (TSM) can be classified into solid adsorption materials, liquid absorption materials, chemically reactive solid materials and composite materials (CSMP).

TES materials can be integrated in buildings to improve their energy performance by means of different passive or active applications.

•  Passive solutions are characterized by a heat exchange without mechanical action via natural convection between the indoor environment and storage material (24).
•  Active applications are based on a heat exchange assisted by a mechanical component (fan, blower or pump) (25).

Figure 2 illustrates the relationships existing between available TES materials and their possible applications. Main building applications can be classified into: TES in building materials or elements, thermally activated building systems (TABSs), TES components, small-scale TES units and large-scale TES systems (26).

Figure 2. Applications of thermal energy storage materials in buildings.

 

TES in building materials or elements consists of passive applications based on high thermal inertia. They allow improving the thermal performance of buildings by the attenuation of thermal oscillations (24). TABSs consist of active applications which use the building structure as a TES system. A thermal energy source is connected to a construction element which exchanges heat with the indoor space, such as an underfloor heating system (27). TES components consist of latent heat storage modules usually applied to ventilation systems in free cooling applications (28), and PV panels for increasing the electrical yield thanks to a reduction of temperature rise of their surface (2931). Small-scale TES units refers to compact storage tanks, which allow increasing the use of renewable energy and improving the energy performance of heating, ventilation, air conditioning and refrigeration (HVAC&R) systems (32, 33). Large-scale TES systems refer to above-ground large-scale tanks or underground thermal energy storage (UTES) systems (34). Their main applications consist of solar storage in district heating (DH) networks or large-scale buildings. Following this classification, most advanced TES solutions assessed and tested in literature was further assessed by Lizana et al. (35).

Each application group has different temperature ranges according to final implementation and thermal energy use. Also, the performance of these TES applications depends on the thermophysical properties of the TES materials chosen.

3. CHARACTERIZATION PARAMETERS OF TES MATERIALSTOP

3.1. Sensible and latent heat storage materialsTOP

Sensible heat storage is yet the most widely used technique for TES in buildings while applications based on latent heat storage are gradually growing as they allow storing high thermal energy amounts within a narrower temperature range. Characterization parameters of sensible and latent heat storage materials (SHSMs and LHSMs), and their influences in storage solutions are showed in Table 1 (2, 23, 36).

Table 1. Characterization parameters of SHSMs and LHSMs
Property Measure Influences
Density (r) kg/m3  
Specific heat (cp) kJ/kg K Thermal storage capacity
Latent heat of phase change (h) kJ/kg  
Phase change temperature °C Thermal application
Thermal conductivity (l) W/m K Charging/ discharging time Stratification ability
Thermal diffusivity (α) mm2/s  
Thermal effusivity Ability to exchange thermal energy with its surroundings (36)
Thermal expansion coefficient % Change of volume (Requirements for container)
Thermal reliabilitya (Efficiency after thermal cycles) % Performance over several thermal cycles
Chemical stabilitya (after thermal cycles) Changes in spectrum No chemical decomposition of material after thermal cycles
Thermal stabilityb (Degradation at high temperature) Weight loss % No degradation of material with the increase of temperature
a5000 cycles are required for approximately 13–14 years (37).
bCommonly not important for building applications due to low-temperature of applications.

The amounts of energy stored in a given mass of material (m) by sensible heat storage (Qsensible) and by latent heat storage (Qlatent) are given by Eq. [1] and Eq. [2] (23), respectively.

The most important physical properties to take into consideration are: i) high specific heat capacity and density, good thermal conductivity and low cost for sensible heat storage; ii) suitable phase change temperature for the corresponding application, high volumetric latent heat capacity, good thermal conductivity and low cost for latent heat storage. As a reference value, sensible heat storage capacity of water, for a temperature difference (ΔT) of 60 °C (25–85 °C), is 250 MJ/m3. This value should be considered as maximum reference value, which could be reduced according to final building application.

Other requirements and constraints for selecting SHSMs and LHSMs are specified in Table 2 (2, 38). They are based on safety conditions, environmental impact and compatibility with other materials.

Table 2. Requirements or constraints for selecting of SHSMs and LHSMs
Requirements or constraints Measure Reasons
Small volume change % Less mechanical requirements of container
Non-toxic, non-flammable, non-explosive and non-reactive - Safety
Recyclability % Environmental impact
Non-polluting, low CO2-eq footprint CO2-eq/kg  
Non-corrosiveness - Compatibility with other materials
Availability and low price €/m3 or €/kg Competitiveness and effective cost
Congruent melting    
Not subcooling/supercoolinga ΔTª (°C) To assure that melting and solidification can proceed in a narrow temperature range.
Not phase segregation or separationb - Assure a long lifetime
aSubcooling refers to a liquid existing at a temperature below its normal melting temperature. If such temperature is not reached, PCM will not solidify at all and stored heat will not be released (2).
bPhase segregation or separation refers to the conversion of a single-phase system into a multi-phase system (separation of components of a solution).

Main drawbacks of SHSMs are related to their low energy density (owing to space limitation for building applications) and system’s self-discharge, which can be substantial due to heat losses (particularly for long-period storage) (38). Main drawbacks of LHSMs are related to their high cost, low thermal conductivity, relative large volume change, flammability, supercooling, corrosiveness, and thermal reliability and stability after undergoing a great number of thermal cycles (15).

3.2. Thermochemical storage materialsTOP

TCES can be classified into chemical reactions and/or sorption processes (17). A chemical reaction is characterized by a change in chemical bounds of the compounds involved during the reaction (dissociation and recombination). Energy can be stored through the endothermic reaction and released by the exothermic reverse reaction. Sorption storage can be defined as a phenomenon of fixation or capture of gas or vapour by a sorbent substance in the condensed state (solid or liquid) by means of less intense interactions. Also, sorption processes can involve thermophysical and thermochemical aspects (16). For the characterization of solid sorbents for thermal applications, in addition to energy density or process efficiency, other parameters should be considered: the possible temperature lift (defined as the difference between the air entering and exiting the solid bed), the drop in humidity ratio and the breakthrough curves (dynamic response of the system) (39). All these parameters can be known from the adsorption equilibrium of each adsorbent material.

Main advantages of TCES are high stored energy density, negligible heat losses, and long-term storage capacity. Characterization parameters of TSMs and their influences are showed in Table 3.

Table 3. Characterization parameters of TSMs
Property Measure Influences
Density (r) kg/m3  
Heat input Wh/kg - MJ/m3  
Heat output (storage density) Wh/kg - MJ/m3 Thermal storage capacity
Storage efficiency (Qreleased/Qstored) %  
Degree of sorbate loading in the adsorption/absorption equilibrium % (for physical sorption)  
Charging/desorption temperature °C  
Discharging/sorption temperature °C Thermal application
Temperature lift (Tair,inTair,out) °C  
Thermal conductivity (l) W/m K  
Kinetic of reaction or reaction rate m/s Charging/ discharging time
Evolution of output temperature close to the equilibrium point °C  
Operating pressure range Pa System design requirements
Thermal reliability (Efficiency after thermal cycles) % Performance over several cycles
Chemical stability (After thermal cycles) Changes in spectrum after thermal cycles No chemical decomposition of material after thermal cycles
Thermal stability Weight loss % No degradation of material with the increase of temperature

Thermal energy stored during a specific time period through thermochemical processes is given by Eq. [3] (23).

Other requirements for selecting TSMs are defined in Table 4. They are based on safety conditions, environmental impact, lifetime and compatibility with other materials.

Table 4. Requirements or constraints for selecting of TSMs
Requirements or constraints Measure Reasons
Non-toxic, non-flammable, non-explosive and non-reactive - Safety
Non-polluting, low CO2-eq footprint CO2-eq/kg Environmental impact
Non-corrosiveness - Compatibility with other materials
Availability and low price €/m3 Competitiveness and effective cost
Moderate operating pressure range Pa No excessive pressure conditions and especially no high vacuum. Less system requirements

Main drawbacks of TSMs are related to their high cost, inappropriate operation temperatures, non-effective discharge power for building applications due to slow reaction kinetics and low output temperature close to the equilibrium point, and low/moderate efficiency in storage process.

4. CHARACTERIZATION OF AVAILABLE THERMAL ENERGY STORAGE COMPOUNDS FOR BUILDING APPLICATIONTOP

4.1. Sensible heat storage materialsTOP

SHSMs can be classified into liquid and solid storage materials (23). Usual liquid storage materials for low-to-moderate temperature applications are water, oils and alcohol derivatives. Some common solid storage materials are rocks, bricks, concrete, dry and wet earth/soil, wood, plasterboard, and corkboard. Some of the most commonly used in buildings are listed in Tables 5 and 6.

Table 5. SHSMs. Liquids. Properties
Material Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Average volumetric specific heat capacity (kJ/m3 K) Reference
Mineral oil 770 0.12 1.96 1509 (21)
Engine Oil 888 0.14 1.88 1669 (38)
Water (80 °C) 970 0.67 4.19 4064 (40)
Water (40 °C) 990 0.63 4.19 4148 (40)
Water (10 °C) 1000 0.6 4.19 4190 (40)
Table 6. SHSMs. Solids. Properties
Material Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Average volumetric specific heat capacity (kJ/m3 K) Reference
Wood (low density) 450 0.12 1.6 720 (40)
Plywood boards (low density) 500 0.13 1.6 800 (40)
Gypsum (plasterboard) 900 0.25 1 900 (40)
Gypsum (coating) 1000 0.4 1 1000 (40)
Oriented strand board 600 0.14 1.7 1020 (40)
Wood (high density) 700 0.18 1.6 1120 (40)
Oriented strand board 900 0.18 1.7 1530 (40)
Ceramic tile 2000 1 0.8 1600 (40)
Lime mortar 1600 0.8 1 1600 (40)
Plywood boards (high density) 1000 0.24 1.6 1600 (40)
Ceramic brick 1800 0.73 0.92 1656 (41)
Cement bonded particleboard 1200 0.23 1.5 1800 (40)
Cement mortar 1800 1 1 1800 (40)
Concrete 2000 1.35 1 2000 (40)
Sand and gravel 1700–2200 2 0.910–1.180 2072 (40)
Limestone 1600–2600 0.85–2.3 1 2100 (40)
Rock 2800–1500 3.5–0.85 1 2150 (40)
Concrete (high density) 2400 2 1 2400 (40)
Reinforced concrete (2%) 2400 2.5 1 2400 (40)
Clay or silt 1200–1800 1, 5 1.670–2.500 3252 (40)
Asphalt sheet 2300 1.2 1.7 3910 (42)

4.1.1. LiquidsTOP

Liquid materials are widely used for cooling and heating purposes. Water is the best available liquid material for temperature applications lower than 100 °C due to its high specific heat capacity, availability and low cost (38). It is the most widely used medium for heating and cooling applications as it can be circulated easily to transport heat if required (21). For a temperature gradient of 60 °C (25-85 °C), water stores 250MJ/m3. This value is taken into account as a reference for comparison with other TES materials. Main drawbacks are related to the risk of leakages and high investment cost of storage infrastructures mainly for large-scale applications.

4.1.2. SolidsTOP

Solid materials are widely used for heating applications at low and high temperature. Rocks and concrete can operate in a temperature range from 40 to 75 °C without any leakage problem (23, 38). They have a reduced energy storage density for heating as compared to water (95-105 MJ/m3), however stratification can be maintained over considerable time periods due to the high thermal diffusivity (0.7-1 mm2/s), which helps heat release and charge (38). Solids are also characterized by some limitations such as, associated costs involved in operation and maintenance of the storage units, and risks of self-discharge in long-term storage.

Other solids materials widely used in buildings to improve TES capacity are brick, sand and gravel, cement, gypsum and bricks. They have been mainly applied to improve the thermal inertia of building structure, for attenuating indoor temperature oscillation. The properties of common sensible building materials are listed in Table 6.

4.2. Latent heat storage materialsTOP

Solid-liquid PCMs are the most common processes in building applications. This section reviews all different latent heat compounds, eutectics and mixtures that have been studied by different researchers for their potential use as PCMs with a special focus on their thermophysical properties.

4.2.1. OrganicsTOP

Organic materials have been successfully tested and implemented in many building applications (21). They present congruent melting without phase separation. Organic materials used as PCM are commonly classified into paraffins and non-paraffins. Paraffins or paraffin waxes refer to linear chain hydrocarbons composed of n-alkanes. Non-paraffins usually refer to a large category of organic materials for latent heat storage composed mainly by fatty acids, esters, sugar alcohols, glycols and other (10).

4.2.1.1. ParaffinsTOP

Paraffins or straight-chain alkanes are characterized by the chemical formula CnH2n+2 or CH3–(CH2)n–CH3 (10, 11). Pure paraffin waxes are very expensive, thus only technical grade paraffins are commonly used as PCMs due to cost considerations (10, 21). They are widely utilized as PCMs because of their favorable properties: moderate thermal storage density (approximately 200 kJ/kg and 150 MJ/m3), congruent melting and solidification with negligible subcooling (good nucleating properties), good chemical stability without phase segregation, little volume change, non-corrosive with metal containers, non-toxic and moderate cost (4, 10, 21, 38, 43, 44). They usually show stable properties and good thermal reliability even after 1000–2000 thermal cycles (21). However, they have low thermal conductivity (≈0.2 W/mK), which reduces their heat exchange rate during the melting and solidification processes (1, 38). In addition, they show moderate flammability and can interact with some plastic containers, particularly with polyolefins, leading to infiltrations and softening (1, 10).

Table 7 shows the straight-chain alkanes tested in literature and their performance according to the results obtained by different authors.

Table 7. Organic PCMs: straight-chain alkanes. Properties (solid/liquid)
Material Melting temp. (°C) Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Latent heat (kJ/kg) Reference
n-Tridecane (C13H28) CH3(CH2)11CH3 −5       160 (21)
n-Tetradecane (C14H30) CH3–(CH2)12–CH3 4.49–11.72       230.38 (45)
  4.5       165 (4, 46)
  5.5       228 (10)
  5.9 /762       (47)
  6 /760 0.21/   230 (48)
  6 810     229 (49)
n-Pentadecane (C15H32) CH3–(CH2)13–CH3 8.72–15.11       176.15 (45)
  9.6 776.1/727.2 0.182/0.15 3.08/3.53 168.0 (50)
  9.9 /768.3       (47)
  10 /770     212 (48)
  10       205 (10)
n-Hexadecane (C16H34) CH3–(CH2)14–CH3 16.7       237.1 (10)
  16.76–23.63       225.15 (45)
  18 780 0.17-0.26 1.65/2.1 236 (51)
  18 /776 0.21/   210.238 (48)
  18 830     229 (49)
  18.0–20.0 /773     216-236 (1, 52)
  18.2 /773.4       (47)
  20       185 (22, 43)
n-Heptadecane (C17H36) CH3–(CH2)15–CH3 19 /776     240 (48)
  21–27.36       172.21 (45)
  21.7       213 (10)
  21.98 777.9/       (47)
  22 780 0.17-0.26   214 (51)
  22 /778     214 (1, 52)
n-Octadecane (C18H38) CH3–(CH2)16–CH3 27.74   0.153   209.10 (22, 53)
  28.0       244 (10)
  28 780 0.17-0.26 1.75/2.1 244 (51)
  28 814/774 0.15/ /2.16 244 (4, 46, 54)
  28 814/774 0.358/0.148   200.245 (48)
  28 850     243 (49)
  28.0–28.4 /776     200–244 (1, 52)
  28.2 781.8/       (47)
  28.4       234 (22, 43)
n-Nonadecane (C19H40) (CH3(CH2)17CH3) 31.9 785.4/       (47)
  32.0       222 (10)
  32.0 /785     222 (1, 52)
  32       194.3 (22, 43)
n-Icosane (C20H42) CH3(CH2)18CH3 36.4 788/.6       (47)
  36.6 /788     247 (1, 52)
  36.7       246 (10)
  37.8       218.5 (55)
  38 779     283 (48)
n-Heneicosane (C21H44) CH3(CH2)19CH3 40.2       200 (10)
  40.2 /791     213 (1, 52)
n-Docosane (C22H46) CH3(CH2)20CH3 41.6 785 0.22 1.93/2.38 194.6 (56)
  44.0       249 (10)
  44.0 /794     249 (1, 52)
n-Tricosane (C23H48) CH3(CH2)21CH3 47.5       232 (10)
  47.5 /796     234 (1, 52)
n-Tetracosane (C24H50) CH3(CH2)22CH3 50.6       255 (10)
  50.6 /799     255 (1, 52)
n-Pentacosane (C25H52) CH3(CH2)23CH3 49.4       238 (10)
  53.5 /801     238 (1, 52)
n-Hexacosane (C26H54) CH3(CH2)24CH3 56.3       256 (10)
  56.3 /803     256 (1, 52)
n-Heptacosane (C27H56) CH3(CH2)25CH3 58.8       236 (10)
  58.8 /779     235 (1, 52)
n-Octacosane (C28H58) CH3(CH2)26CH3 41.2 /806     254 (1, 52)
  61.6       253 (10)
n-Nonacosane (C29H60) CH3(CH2)27CH3 63.4       240 (10)
  63.4 /808     239 (1, 52)
n-Triacontane (C30H62) CH3(CH2)28CH3 65.4 /775     252 (1, 52)
  65.4       251 (10)
  65.8 809.6/       (47)
  66 775       (48)
n-Hentriacontane (C31H64) CH3(CH2)29CH3 68.0       242 (10)
n-Dotriacontane (C32H66) CH3(CH2)30CH3 69.5       170 (10)
n-Tritriacontane (C33H68) CH3(CH2)31CH3 73.9       268 (10)
n-Tetratriacontane (C34H70) CH3(CH2)32CH3 75.9       269 (10)
n-Tetracontane (C40H82) CH3(CH2)38CH3 81.5 820.4/       (47)
  82         (48)
n-Pentacontane (C50H102) CH3(CH2)48CH3 95 779       (48)

The melting point of paraffins increases with the number of alkane chains within the molecule (10, 38), being n-Tetradecane the shortest n-alkane, which melts above 0 °C. Alkanes of different chain length are also prepared in different mixtures to get PCMs with different melting temperatures (48). Table 8 shows examples of mixtures of some alkanes.

Table 8. Organic PCMs: Mixture of straight-chain alkanes. Properties (solid/liquid)
Materiala Melting temp. (°C) Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Latent heat (kJ/kg) Reference
Paraffin C15–C16 8       153 (4, 46)
Paraffin C16–C18 19.5–22.2       152 (57)
Paraffin C13–C24 22–24 900/760 0.21/ /2.1 189 (4, 15, 46)
Paraffin C16–C28 42–44 910/765 0.21/ /2.1 189 (4, 46)
Paraffin C20–C33 48–50 912/769 0.21/ /2.1 189 (4, 46)
Paraffin C22–C45 58–60 920/795 0.21/ /2.1 189 (4)
Paraffin C23–C45 62–64 915/790 0.21/ /2.1 189 (4)
Paraffin C21–C50 66–68 930/830 0.21/ /2.1 189 (4, 46)
aParaffin nomenclature (Cn) refers to the number of n-alkanes (straight-chain alkanes) in each compound. For instance, Paraffin C15 consists of n-Pentadecane with the formula C15H32 or CH3–(CH2)13–CH3.

The undesirable low thermal conductivity of paraffins and other organic PCMs has been overcome through different solutions such us improved heat transfer by means of metal matrix structures or metallic fins (28, 58, 59), and the development of composite materials based on metal shavings or metal powder embedded in pure PCMs (37, 60).

4.2.1.2. Fatty acidsTOP

Along with parrafins, saturated and unsaturated fatty acids have been widely tested and used as PCMs. Saturated fatty acids are characterized by the general formula CH3(CH2)2nCOOH (48). Fatty acids show reproducible melting and freezing behaviour with little or no subcooling (4) and are stable upon cycling since they consist of only one component without the possibility of phase separation (48). Saturated fatty acids also exhibit low phase transition volume changes (21). On the other hand, they show some drawbacks such as low thermal conductivity, mild corrosiveness, and higher cost than technical grade paraffins (approximately 2-2.5 times greater) (10, 48).

Tables 9 and 10 show the tested properties of saturated and unsaturated fatty acids used as LHSMs.

Table 9. Organic PCMs: Saturated fatty acids. Properties (solid/liquid)
Material Melting temp. (°C) Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Latent heat (kJ/kg) Reference
Caprylic acid CH3(CH2)6COOH 16 981/901 /0.149     (5, 46, 61)
  16.5 1033/862 /0.148   149 (4)
Capric acid CH3(CH2)8COOH 28.8       147.4 (62)
  31.04       190.21 (63)
(22)
  31.3       163 (44)
  31.5 /886 /0.149   153 (4)
  32 1004/878 /0.153   152.7 (5, 46, 61)
  32.14       154.24 (64)
  35.6       169.9 (65)
Lauric acid CH3(CH2)10COOH 40–43       167–171 (44)
  42.0       123.9 (62)
  42–44 /870 /0.147 1.6 178 (4)
  42.6     1.7/2.3 211.6 (66)
  42.6       176.6 (67)
  43.97       200.18 (22, 63)
  44 1007/862     177.4 (5, 46)
  48.5       187.7 (65)
Myristic acid CH3(CH2)12COOH 50.4–53.6       189 (44)
  51.5     2.8/2.42 204.5 (68)
  52.2       182.6 (67)
  53.52       201.65 (22, 63)
  53.8     1.7/2.4 192.0 (66)
  54 /844   1.6/2.7 187 (4)
  58 990/861     186.6 (5, 46)
  61.0       201.0 (65)
Palmitic acid CH3(CH2)14COOH 57.8–61.8     2.20/1.70 201 (44)
  59.40       218.53 (64)
  59.9     1.9/2.8 197.9 (66)
  61 942/862 0.16 2.2/2.48 203.4 (69)
  62.6       208.5 (22, 70)
  63 /847 /0.165   187 (4)
  64 989/850 /0.162   185.4 (5, 46, 61)
  66.8       216.5 (65)
Stearic acid CH3(CH2)16COOH 53.6     1.6/2.2 174.6 (66)
  60–61 1080/1150 0.18 2.83/2.38 186.5 (71)
  65.2–68.5     2.07/1.90 210 (44)
  69 965/848     202.5 (5, 46, 61)
  70 941/ /0.172 /2.35 203 (4)
  72.5       220.4 (65)
Arachidic acid CH3(CH2)18COOH 74.0       227 (1)
Table 10. Organic PCMs: Unsaturated fatty acids. Properties (solid/liquid)
Material Melting temp. (°C) Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Latent heat (kJ/kg) Reference
Undecylenic acid CH2=CH(CH2)8COOH 24.6       141 (1, 72)
Eladic acid C8H7C9H16COOH 47       218 (10)

Their melting temperature generally increases with the length of the molecule (1, 48). Different fatty acids can also be mixed to design PCMs with melting temperatures differing from those of the pure fatty acids (48).

Sari and Kaygusuz (66) studied the thermal reliability under 910 thermal cycles of stearic acid, palmitic acid, myristic acid and lauric acid. The percentage of latent heat losses after cycling was 31.9%, 17.8%, 17.1% and 37.2%, respectively, indicating that palmitic acid and myristic acid are more suitable for latent heat storage.

4.2.1.3. Fatty acid estersTOP

Fatty acid esters are derived from acids in which one hydroxyl (-OH) group is replaced by one alkyl (-O) group (21). They show a narrow temperature range of phase transition and their mixtures can form eutectics with negligible subcooling (1). They are widely available due to their commercial use in other industries (polymer, cosmetics, clothes, etc.) (21). Table 11 shows the tested properties of fatty acid esters used as LHSMs.

Table 11. Organic PCMs: Fatty acid esters. Properties (solid/liquid)
Material Melting temp. (°C) Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Latent heat (kJ/kg) Reference
Isopropyl palmitate (C19H38O2) CH3(CH2)14COOCH(CH3)2 11       100 (46, 73, 74)
Isopropyl stearate (C21H42O2) CH3(CH2)16COOCH(CH3)2 14       142 (46, 73, 74)
Propyl palmitate (C17H34O2) CH3(CH2)12COOC3H7 16–19       186 (1, 75)
  19       186 (46, 76)
Butyl stearate (C22H44O2) CH3(CH2)16COO(CH2)3CH3 18–23       140 (75)
  19       200 (46, 73, 74)
  19       140 (76)
  23       140 (22)
Allyl palmitate (C19H36O2) 22.6       173 (1, 77)
Dimethyl sebacate (C12H22O4) (CH2)8(COOCH3)2 21       135 (46, 73, 74)
Methyl palmitate (C17H34O2) CH3(CH2)14CO2CH3 28.8       163.2 (1, 62)
Vinyl stearate (C20H38O2) CH3(CH2)16COOCH=CH2 27-29       122 (46, 73, 74)
Methyl stearate (C19H38O2) CH3(CH2)16CO2CH3 37.0       160.7 (1, 62)
Methyl-12 hydroxy-stearate (C19H38O3) CH3(CH2)10CH(CH2)5COOCH3OH 43       126 (46, 73, 74)
Ethylene glycol distearate (C38H74O4) 65.5 972.9     215.8 (1, 78)

4.2.1.4. Sugar alcoholsTOP

Different sugar alcohols and polyalcohols have been tested as potential PCMs. They are characterized by the general formula HOCH2(CHOH)nCH2OH. Sugar alcohols have much higher latent heat of fusion than other organic materials (approximately 300 kJ/kg and 375 MJ/m3). However, they have a high melting temperature (>90 °C) and may be combustive, which limits their application in buildings.

Table 12 shows the tested properties of sugar alcohols used as LHSMs.

Table 12. Organic PCMs: Sugar alcohols. Properties (solid/liquid)
Material Melting temp. (°C) Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Latent heat (kJ/kg) Reference
Xylitol (C5H7(OH)5) HOCH2[CH(OH)]3CH2OH 93       248.7 (79)
(22)
  93       280 (80)
  94 1500/     263 (48)
D-Sorbitol (C6H8(OH)6) HOCH2[CH(OH)]4CH2OH 97 1520/     185 (48)
  97       110 (80)
Erythritol (C4H6(OH)4) HOCH2[CH(OH)]2CH2OH 117       344 (80)
  118.0 1480/1300 0.733/0.326   339.8 (46, 81)
  120 1480/1300 0.733/0.326   340 (48)
Mannitol (C6H14O6) HOCH2[CH(OH)]4CH2OH 165       341 (80)

4.2.1.5. Polyethylene glycols (PEGs)TOP

Polyethylene glycols (PEGs) are composed of dimethyl ether chains having the hydroxyl group at the end, being characterized by the chemical formula HO–CH2–(CH2–O–CH2–)n–CH2–OH or C2nH4n+2On+1 (21). They are chemically and thermally stable under cycling, non-flammable, non–toxic, non–corrosive and have moderate cost. However, they present low thermal conductivity as other organic materials. Table 13 shows the tested properties of PEGs used as LHSMs. The melting point and latent heat of fusion of PEGs increase with increasing molecular weight (1).

Table 13. Organic PCMs: Polyethylene glycols (PEG). Properties (solid/liquid)
Material Melting temp. (°C) Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Latent heat (kJ/kg) Reference
Diethylene glycol C4H10O3 −10 to −7 /1120       (48)
Triethylene glycol C6H14O4 −7 /1120       (48)
PEG 400 4.2       117.6 (1)
  8 1228/1125 /0.187 - 99.6 (5, 46, 61)
PEG 600 12.5       129.1 (1, 49)
  22 1232/1126 /0.189 - 127.2 (5, 46, 61)
PEG 1000 35–40         (48)
  40.0       168.6 (1, 82)
PEG 3000 52–56         (48)
PEG 3400 63.4       166.8 (1, 65)
PEG 6000 66 1212/1085 - - 190.0 (5, 46, 61)
PEG 10000 55–60         (48)
  65.9       171.6 (1, 65)
PEG 20000 67.7       160.2 (1, 65)
PEG 35000 68.7       166.9 (1, 65)
PEG 100000 67.0       175.8 (1)
PEG 1000000 70.0       174.0 (1)

4.2.1.6. Other compoundsTOP

Other organic compounds tested as PCMs are aromatic hydrocarbons, monohydroxy alcohols, ketones, ethers, halogen derivatives, sulphur compounds, amides, dienes, oleochemical carbonates (Table 14). They show a relatively moderate thermal storage density (approximately 100–200 kJ/kg and 100–200 MJ/m3). Most of them have not been studied in detail regarding their applicability as PCMs but could be a valuable alternative to paraffins and salt hydrates, which currently dominate the PCM market.

Table 14. Organic PCMs: Other compounds. Properties (solid/liquid)
Class of compounds Material Melting temp. (°C) Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Latent heat (kJ/kg) Reference
Aromatic hydrocarbons Biphenyl (C12H10)2 71 1166/991     119.2 (5, 46, 61)
  Naphthalene C10H8 80 1145/976 0.310/0.132 2.8/ 147.7 (5, 46, 61)
Monohydroxy alcohols 1-dodecanol (C12H26O) CH3(CH2)11OH 17.5–23.3       188.8 (75)
    23.8       184 (77)
    26       200 (46, 76)
  1-Tetradecanol (C14H30O) CH3(CH2)12OH 38       205 (46, 76)
    39.3       221.23 (83)
Ketones Trimethylcyclohexene-1, 4-dione (C9H12O2) 24.1       47 (72)
  Phorone (C9H14O) (CH3)2C=CHCOCH=C(CH3)2 25.8       124 (72)
Ethers Diphenyl ether (C6H5)2O 27.2       97 (1, 72)
Halogen derivative Chlorobenzothiazole C7H4ClNS 18.6       65 (1, 72)
  1-Iodehexadecane 22.2       131 (1, 72)
  3-Iodoaniline IC6H4NH2 22.5       64 (1, 72)
Sulphur compounds Dimethyl sulfoxide (CH3)2SO 16.5 1009/1009   1.45/1.88 85.7 (46, 84)
  Octadecyl 3-mercaptopropionate HS-CH2CH2COO(C18H37) 21       141 (73, 74)
  Octadecyl thioglycolate HS-CH2COO(C18H37) 26       91 (73, 74)
  Dilauryl thiodipropionate S(CH2CH2COO(C12H25))2 39       159 (73, 74)
Amides Propionamide (C3H7NO) CH3CH2CONH2 79       168.2 (46)
  Acetamide CH3CONH2 81       241 (1, 10)
Dienes Dicyclopentadiene (C10H12) 28.7       11.7 (1, 49)
Oleochemical carbonates Decyl carbonate (C21H42O3) −2.2       144 (1, 85)
  Dodecyl carbonate (C25H50O3) 19.3       200 (1, 85)
  Tetradecyl carbonate (C29H58O3) 33.7       227 (1, 85)
  Hexadecyl carbonate (C33H66O3) 44.9       219 (1, 85)
  Octadecyl carbonate (C37H74O3) 51.6       223 (1, 85)

4.2.2. InorganicsTOP

Inorganic materials have been widely tested and implemented in building applications as PCMs. They usually have similar latent heat of fusion per mass than organic materials, but higher ones per volume due to their high density (48). Main inorganic materials used as PCMs are salt hydrates and metals.

4.2.2.1. Salt hydratesTOP

Salt hydrates are characterized by the general formula: AB·xH2O, being inorganic salts containing water of crystallization (21). Salt hydrates have higher LHSC and thermal conductivity than organic materials for low-to-moderate temperature applications, approximately 350MJ/m3 and 0.5 W/m K, respectively (15, 38). Also, they are non-flammable and cheaper than paraffins. However, they often present some disadvantages which limit their applicability, such us low thermal reliability for long-operation periods, phase segregation, subcooling and corrosiveness (2, 10, 38, 44). Table 15 shows the properties of the main salt hydrates tested.

Table 15. Inorganic PCMs for building applications: Salt hydrates. General formula: AB·xH2O. Properties (solid/liquid)
Material Melting temp. (°C) Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Latent heat (kJ/kg) Reference
H2O 0 900/1000 2.2/0.6 2/4.19 334 (40)
Lithium chlorate trihydrate LiClO3·3H2O 8 1720/1530     155 (48)
  8.1 1720/1530     253 (8, 20)
  8.1         (9)
Zinc chloride tetrahydrate ZnCl2·3H2O 10         (46, 86)
Potassium phosphate hexahydrate K2HPO4·6H2O 13         (46, 86)
Sodium hydroxide NaOH·3 ½;H2O 15         (46, 86)
  15.4         (9)
Sodium chromate decahydrate Na2CrO4·10H2O 18         (46, 86)
Potassium fluoride tetrahydrate KF·4H2O 18.5         (9)
  18.5 1455/1447   1.84/2.39 231 (4, 13, 15)
Calcium chloride hexahydrate CaCl2·6H2O 24 /1470 1.09/0.54 1.4/2.1 140 (87)
  28 1710/1500 1.09/0.54 1.43/2.31 188.34 (88)
  28 1680/1500 0.624/0.454 1.25/2.13 200 (1, 89)
  29 1630/1500     160 (44)
  29.2         (9)
  29.30 1710/1562 1.088/0.540   171.19 (48)
  29.5 1680/   1.42/2.3 170 (7, 20)
  29.6 1802/1562 1.088/0.540 1.42/2.1 190.8 (5, 20, 46, 90)
  29.7 1710/1496   1.45/ 171 (4)
Manganese nitrate hexahydrate Mn(NO3)2·6H2O 25.8 1795/1738 2.34/   125.9 (46, 49)
  26       140 (7, 20)
Lithium nitrate trihydrate LiNO3·3H2O 29.9       296 (5, 20)
  30       125 (7, 20)
  30       296 (13, 46, 91)
  30 1460     256 (49)
Sodium sulphate decahydrate (Glauber’s salt) Na2SO4·10H2O 21–23 1480     198 (92)
  31–32 1534/     251 (44)
  32.4       251 (9)
  32.4 1460/1330 0.7/0.544 1.76/3.3 241 (93)
  32.4 1485/ 0.544 1.93/ 254 (4, 46)
  32.4       251 (7, 20)
  32.5       251 (74)
  34 1550     176 (49)
Sodium carbonate decahydrate Na2CO3·10H2O 32–36 1442     247 (44)
  33         (9)
  33 1460/     247 (5, 20, 91)
  34 1440/   1.88/3.35 251 (7, 20)
Calcium bromide hexahydrate CaBr2·6H2O 34 2194/1956     115.5 (46, 61)
  34         (9)
  34.3 2194/1956     115.5 (5, 20, 46)
Disodium hydrophosphate dodecahydrate Na2HPO4·12H2O 35 1520/1442 0.514/0.476 1.70/1.95 281 (4)
  35.2         (9)
  35.2–44.6 1520/1442 0.514/0.476 1.70/1.95 280 (5, 20)
  36.5 1520   1.55/3.18 264 (7, 20)
  38–41.5 1522/1442     269.7 (44)
Zinc nitrate hexahydrate Zn(NO3)2·6H2O 36         (9)
  36 1937/1828 /0.464   146.9 (5, 46)
  36.4 2065/   1.34/2.26 147 (4)
  36.4 2070   1.34/2.26 130 (7, 20)
Potassium fluoride dihydrate KF·2H20 41.4         (9)
Potassium acetate monohydrate K(CH3COO)·1 ½;H2O 42         (46, 86)
Calcium nitrate tetrahydrate Ca(NO3)2·4H2O 42.6 1820/   1.46/ 140 (7, 20)
  42.7       142 (20, 94)
  42.7         (9)
Potassium phosphate heptahydrate K3PO4·7H2O 45         (46, 86)
Zinc nitrate tetrahydrate Zn(NO3)2 ·4H2O 45.5         (46, 86)
Sodium phosphate heptahydrate Na2HPO4·7H2O 48         (9)
Sodium thiosulfate pentahydrate Na2S2O3·5H2O 48.0 1730/1670   1.46/2.39 201 (4)
  48.0       200 (20, 94)
  48     /3.83 206 (95)
  48         (9)
  48.5–55.2 1750/1670     201 (5, 20)
  49.0 1690/1660   1.46/2.38   (7, 20)
  49.8–51.3 1730/1660     217.2 (44)
Zinc nitrate dihydrate Zn(NO3)2·2H2O 54         (46, 86)
Sodium acetate trihydrate NaCH3COO·3H2O 55.6–56.5       237-243 (1, 96)
  58.0 1450/   1.97/3.35 180 (7, 20)
  58.0       289 (20, 94)
  58.0     2.26/3.33 248 (95)
  58 1450/     226 (46, 91)
  58 1450/ 0.6   240 (97, 98)
  58 1450/1280     226.264 (48)
  58.4         (9)
  58.5       260 (74)
Sodium hydroxide monohydrate NaOH·H2O 58.0     2.18/ - (9)
  64       259 (74)
  64       272 (7, 20)
Cadmium nitrate tetrahydrate Cd(NO3)2·4H2O 59.5         (9)
  59.5 2450/   1.09/ 106 (7, 20)
Iron nitrate hexahydrate Fe(NO3)2·6H2O 60         (46, 86)
Sodium tetraborane decahydrate Na2B4O7·10H2O 68.1         (9)
Sodium phosphate dodecahydrate Na3PO4·12H2O 69.0         (9)
Sodium pyrophosphate decahydrate Na4P2O7·10H2O 70       184 (46, 91)
Aluminium nitrate nonahydrate AI(NO3)2·9H20 70         (9)
Barium hydroxide octahydrate Ba(OH)2·8H2O 78.0 2180/   1.17/ 267 (4)
  78.0 2180/   1.17/ 301 (7, 20)
  78.0 2070/1937 1.225/0.653   265.7 (5, 20, 90)
  78.0       295 (20, 94)
  78 2070/     280 (46, 91)
  78         (9)
  78       301 (74)
Potassium alum dodecahydrate KAl(SO4)2·12H2O 80         (46, 86)
  85.8         (9)
Aluminium sulphate octadecahydrate Al2(SO4)3·18H2O 88         (9)
Aluminium nitrate octahydrate Al(NO3)3·8H2O 89         (46, 86)
Magnesium nitrate hexahydrate Mg(NO3)2·6H2O 89 1636/1550 0.669/0.490 1810/2480 162.8 (5, 20, 46)
  90.0 1460/   2260/3680 160 (7, 20)
  90       150.3 (9)
Ammonium aluminium sulphate hexahydrate (NH4)Al(SO4)·6H2O 95       269 (46, 86, 91)
Ammonium aluminium sulphate dodecahydrate (NH4)Al(SO4)2·12H2O 94.0 1650/   1.71/3.05 269 (5, 20)
  94         (9)
Sodium sulphide pentahydrate Na2S·5H2O 96       320.8 (9)
Sodium sulphide pentahydrate Na2S·5 ½;H2O 97.5         (46, 86)
Bischofite (main component MgCl2 ·6H2O) 98.8 1686/1481   1.6/3.0 120.2 (99)
Calcium bromide tetrahydrate CaBr2·4H2O 110         (46, 86)
Aluminium sulfate hexadecahydrate Al2(SO4)16H2O 112         (46, 86)
Magnesium chloride hexahydrate MgCl2 ·6H2O 114.6 1517/1422   2.1/1.95 126.6 (99)
  116 1570/1442   1.72/2.82 165 (4)
  117.0 1560/   1.59/2.85 172 (7, 20)
  117 1569/1450 0.694/0.570 2.25/2.61 168.6 (5, 20, 46)
  117       259.0 (9)

Some of the barriers for using salt hydrates can be eliminated or significantly reduced to obtain a long-term thermal cycling material by different techniques. One of the main methods used for preventing segregation and sedimentation is adding thickening agents. The decomposition along the melting process into water and salt with less content of water is mainly due to density difference between salt and water, which leads the lower hydrate (or anhydrous salt) to settle down at the bottom of the container (10). Thus, by adding polymeric or cellulosic gelling materials, such as wooden fibres or attapulgite clays, the lifetime of salt hydrates can be increased up to 1000 cycles without significantly impairing their properties (21, 74). Other methods are based on the addition of water to a hydrate, in the quantity which slightly exceeds the stoichiometric ratio, and mechanical stirring of the mixture (10, 74). Supercooling, which refers to a liquid existing at a temperature lower the melting temperature, can be reduced or eliminated by using nucleating agents, which accelerate the crystallization of supersaturated solutions, such as borax or carbon (90). However, they often reduce the thermal conductivity (21). A list of nucleating agents used in salt hydrates has been reported by Kenisarin (74).

Regarding the corrosion properties of salt hydrates, according to Kenisarin (74), stainless steel is compatible with all salts and mild steels would react only weakly. However, aluminium, copper and brass are not recommended in applications because of their limited resistance.

4.2.2.2. Metals and metal alloysTOP

Some metal compounds have been tested as PCMs for low-to-moderate temperature applications. Most of fusible alloys are based on the combination of bismuth with other metals, such as lead, tin, indium, and cadmium (38). They have high volumetric fusion heat because of their high density (10) and present high thermal conductivity, good thermal stability and reliability, and a negligible volume change during phase change (1, 22, 38). However, their usage in buildings is constrained by their moderate-high melting temperature, scarce availability and very high cost. Table 16 shows the properties of main metals and metal alloys reported.

Table 16. Inorganic PCMs for building applications: Metals and metal alloys. Properties (solid/liquid)
Material Composition (wt.%) Melting temp. (°C) Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Latent heat (kJ/kg) Reference
Gallium - 29.8 5904 33/41 0.33 80.1 (100)
  - 30.0 2910 40.6/ 0.83 80.3 (38)
Bolton 117 (Cerrolow 117) Bismuth (44.7) + Lead (22.6) +
Tin (8.3) + Cadmium (5.3) + Indium (19.1)
47.2 8858   0.15/0.15 14.0 (101, 102)
Bolton 136 (Cerrolow 136) Bismuth (49) + Lead (18) + Tin (12) + Indium (21) 57.8 8581   0.13/0.13 18.6 (101, 102)
Bolton 140 (Cerrolow 140) Bismuth (47.5) + Lead (25.4) + Tin (12.6) + Cadmium (9.5) + Indium (5) 60.0         (101)
Fields Metal Bismuth (32.5) + Tin (16.5) + Indium (51) 62.2         (101)
Bolton 147 (Cerrolow 147) Bismuth (48) + Lead (25.63) Tin (12.77) + Cadmium (9.6) + Indium (4) 61.1–65 9467     16.3 (101, 102)
Bolton 158 (Cerrobend) Bismuth (50) + Lead (26.7)
Tin (13.3) + Cadmium (10)
70.0 9383   0.17/0.17 32.6 (101)
Woods Metal Bismuth (50) + Lead (25)
Tin (12.5) + Cadmium (12.5)
70.0         (101)
Bolton 160–190 (Cerrosafe) Bismuth (42.5) + Lead (37.7)
Tin (11.3) + Cadmium (8.5)
71.1–87.8 9439   0.17/0.17 23.3 (101)
Bolton 174 (Cerrolow 174) Bismuth (57) + Tin (17) + Indium (26) 78.9     0.16/0.17   (101)
Bolton 203 (Cerroshield) Bismuth (52.5) + Lead (32) + Tin (15.5) 95.0 9850       (101)
Bolton 255 (Cerrobase) Bismuth (55.5) + Lead (44.5) 124 10518   0.13/1.76 16.7 (101)
Bolton 281 (Cerrotru) Bismuth (58) + Tin (42) 138 8719   0.19/0.19 46.5 (101)
Bolton 281/338 (Cerrocast) Bismuth (40) + Tin (60) 138–170 8193   0.20/0.20 51.2 (101)

4.2.3. EutecticsTOP

Eutectics are mixtures of two or more components. Theses mixtures can be developed from organic–organic, organic–inorganic and inorganic–inorganic compounds. One of the most important characteristics of eutectics is their capability to change of phase congruently without phase segregation, with a single melting/freezing point (21). Furthermore, the melting temperature of eutectics is usually lower than that of their single compounds (38). A list of eutectic mixtures with a wide temperature range is presented in the following sub-sections.

4.2.3.1. Organic-organic eutecticsTOP

Different organic-organic eutectics and compositions are found in literature and listed in Table 17. Main tested organic eutectics are based on fatty acid mixtures, such as capric acid + lauric acid (CA + LA), capric acid + palmitic acid (CA + PA), lauric acid–palmitic acid (LA–PA), lauric acid–myristic acid (LA–MA) or myristic acid–stearic acid (MA–SA) (50, 64, 103, 104). Thermo-physical properties of theses mixtures have been tested at different weight combinations by DSC analysis with the aim of identifying the eutectic mixture concentration. It has been shown that the melting temperature and the latent heat in the mixture of these materials follow a downtrend process through different concentrations until the eutectic proportion is achieved (64, 67, 105107).

Table 17. Eutectics and compositions for latent heat storage. Organic-Organic. Properties (solid/liquid)
Material Composition (wt.%) Melting temp. (°C) Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Latent heat (kJ/kg) References
Capric-lauric acid + Pentadecane 50+50 10.2 850.4/827.8   2.44/2.89 157.8 (50)
  70+30 11.3 872.7/858.0   2.27/2.57 149.2 (50)
  90+10 13.3 891.3/883.2   2.08/2.42 142.2 (46, 50)
Triethylolethane + H2O + CO(NH2)2 38.5+31.5+30 13.4 - -   160 (10)
Capric acid + lauric acid 45+55 17-21       143 (75)
  65+35 18 900.0/894.9 0.143/0.139 1.97/2.24 140.8 (50, 103)
    18       120 (44)
  45+55 21 - - - 143 (46, 76)
Capric acid + palmitic acid 76.5+23.5 21.8       171.2 (1, 64)
  75.2+24.8 22.5 870/790 0.14/0.14 2/2.3 173 (29)
Mystiric acid + Capric acid 34+66 24 1018/888 /0.164 - 147.7 (5, 46)
Mystiric acid + Decanoic acid 34+66 24 - -   147.7 (10)
Capric acid + stearic acid 86+14 26.04       176.68 (22, 108)
Acetamide + Urea CH3CONH2 + CO(NH2)2 50+50 27 - -   163 (10)
Triethylolethane + CO(NH2)2 62.5+37.5 29.8 - -   218 (10)
Lauric acid + Palmitic acid   33       145 (44)
  69.0+31.0 35.2       166.3 (1, 104)
Lauric acid + Stearic acid   34       150 (44)
  75.5+24.5 37       182.7 (1, 107)
Lauric acid + Myristic acid 66.0+34.0 34.2       166.8 (1, 67, 104)
Myristic acid + Palmitic acid 58.0+42.0 42.6       169.7 (1, 106)
Myristic acid + Stearic acid 64.0+36.0 44.1       182.4 (1, 104, 109)
  65.7+34.3 50.2       162.0 (1, 110)
Propionamide + Palmitic acid 25.1+74.9 50     1.96/2.40 192 (4)
Palmitic acid + Stearic acid   51       160 (44)
  64.2+35.8 52.3       181.7 (1, 105)
Acetamide + Stearic acid CH3CONH2 + C17H35COOH 50+50 65 - -   218 (10)
Naphthalene + benzoic acid C10H8 + C6H5COOH 67.1+32.9 67   0.282/0.136   123.4 (5, 46)
Naphthalene + benzoic acid C10H8 + C6H5COOH 67.1+32.9 67 - -   123.4 (10)

4.2.3.2. Organic-inorganic eutecticsTOP

Organic-inorganic eutectics and compositions tested are listed in Table 18. They are mainly based on the mixture of urea and salt.

Table 18. Eutectics and compositions for latent heat storage. Organic-Inorganic. Properties (solid/liquid)
Material Composition (wt.%) Melting temp. (°C) Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Latent heat (kJ/kg) Reference
Sodium acetate + Urea Na(CH3COO)·3H2O + CO(NH2)2 60+40 30       200.5 (46, 111)
  40+60 30       200.5 (1, 10)
  60+40 31.5       226 (74)
Urea + Ammonium nitrate CO(NH2)2 + NH4NO3 53+47 46 - -   95 (10)
Urea + Ammonium bromide CO(NH2)2 + NH4Br 66.6+33.4 76 1548/1440 0.682/0.331   161.0 (1, 5, 46)
  66.6+33.4 76 - -   151 (10)

4.2.3.3. Inorganic-inorganic eutecticsTOP

Different inorganic-inorganic eutectics and compositions are listed in Table 19. Main inorganic eutectics are based on alloys of salt hydrates.

Table 19. Eutectics and compositions for latent heat storage. Inorganic-Inorganic. Properties (solid/liquid)
Material Composition (wt.%) Melting temp. (°C) Density (kg/m3) Thermal conductivity (W/m K) Specific heat (kJ/kg K) Latent heat (kJ/kg) Reference
NaNO3 + H2O 36.9+63.1 −18.5       212 (74)
(NH4)2SO4 + H2O 39.7+60.3 −18.5       1.59 (74)
NH4Cl + H2O 19.5+80.5 −16 1020/1060   /3.2 286 (74)
KCl + H2O 19.5+80.5 −10.7 1050/1130   /3.24 283 (74)
ZnSO4 + H2O 27.2+72.8 −6.5 /1340     150 (74)
NH4H2PO4 + H2O 16.5+83.5 −4.0 1040/1090   /3.64 164 (74)
MgSO4 + H2O 19+81 −3.9 990/1040   /3.81 286 (74)
NaF + H2O 3.9+96.1 −3.5 960/1040   /3.85 323 (74)
Ca(NO3)2 + H2O 9.7+90.3 −2.8 990/   /3.61 281 (74)
Na2SO4 + NaCl + KCl + H2O 31+13+16+40 4     - 234 (4)
Na2SO4 + H2O + NaCl + NH4Cl 32.5+41.4+6.66+6.16 13       146 (44)
CaBr2·6H2O + CaCl2·6H2O 55+45 14       140 (44)
  55+45 14.7       140 (10, 74)
Cu(NO3)3·6H2O + LiNO3H2O 55+45 16.5       250 (74)
LiNO3H2O + Zn(NO3)2·6H2O 45+55 17.2       220 (74)
Na2SO4·10H2O + NaCl 50+50 18         (49)
Co(NO3)2·6H2O + H2O + LiNO3H2O 47+7.75+45.25 22.3       265 (74)
LiNO3·3H2O + Ni(NO3)6H2O 60+40 24.2       230 (74)
Ca(NO3)6H2O + Zn(NO3)2·6H2O 45+55 25 1930/     130 (74)
CaCl2·6H2O + MgCl2·6H2O 66.6+33.3 25       127 (46, 91)
CaCl2 + NaCl + KCl + H2O 48+4.3+0.4+47.3 26.8         (4)
  48+4.3+0.4+47.3 26.8 1640     188.0 (46, 91)
Cd(NO3)2·6H2O + Zn(NO3)2·6H2O 60+40 27.4       126 (74)
Ca(NO3)2 4H2O + Zn(NO3)2·6H2O 50+50 29.2       130 (74)
Ca(NO3)2·4H2O + Mg(NO3)2·6H2O 67+33 30       136 (4)
  67+33 30 1670/     135 (74)
  47+53 30       136 (1, 10)
Zn(NO3)2·6H2O + Zn(NO3)2·6H2O 82+18 32 1910/     136 (74)
Ca(NO3)2·4H2O + Al(NO3)3·9H2O 72+28 35 1720/     139 (74)
Ni(NO3)2·6H2O + Cd(NO3)2·6H2O 50+50 37.5       - (74)
MgCl·6H2O + Mg(NO3)2·6H2O 49.3+50.7 58       132.3 (44)
Mg(NO3)·6H2O + NH4NO3 61.5+38.5 51       131.3 (44)
  53+47 52       125 (74)
  61.5+38.5 52 1596/1515 0.552/0.494   125.5 (5, 46)
Mg(NO3)·6H2O + MgCl2·6H2O 58.3+41.7 58       106 (44)
    58       132 (46, 91)
Mg(NO3)2·6H2O + MgCl2·6H2O 58.7+41.3 59 1630/1550 0.678/0.51   132.2 (5, 46)
  53+47 59.1     1.34/3.16 144 (4)
  61.5+38.5 59.1 1680/     144 (74)
  58.7+41.3 59.1       132.2 (9)
Mg(NO3)2·6H2O + Al(NO3)2·9H2O 53+47 61       148 (4)
  53+47 61 1850/     148 (74)
Mg(NO3)2·6H2O+MgBr2·6H2O 59+41 66       168 (10)
LiNO3 + Mg(NO3)2·6H2O 14+86 72 1610/1590     180 (1, 46, 91)
LiNO3+NH4NO3+NaNO3 25+65+10 80.5       113 (10)
LiNO3+NH4NO3+KNO3 26.4+58.7+14.9 81.5       116 (10)
LiNO3 + NH4NO3 + NH4Cl 27+68+5 81.6     1.07/2.20 111 (4, 74)
  27+68+5 81.6       108 (10)

4.3. Thermochemical storage materialsTOP

Thermochemical energy storage is a promising technology mainly due to the high energy density potentially achievable and the possibility of storing energy for long-term periods with negligible heat losses. Nevertheless, research in this field is yet at an early stage (38) and TSMs are not currently available as commercial solutions for TES in buildings. The higher complexity of these storage systems in comparison with currently used sensible heat materials, the higher cost of some of these compounds as well as the need to increase heat and mass transfer capacity to release the stored energy are main challenges for their commercial deployment (16). An evidence of the interest aroused by TCES is the number of international programmes and projects focused on the study of the most promising TSMs, such as the European projects HYDES, MODESTORE (2003-2012), MERITS (2007-20013), COMTES (2012-2016) or E-HUB (2010-2014), or the projects related to Task 32 (2003-2007) (112, 113), and Task 42 (2009-2015) (98) in the framework of the Solar Heating and Cooling Programme of the International Energy Agency (SHC-ECES).

Tested TSMs in the literature are classified into solid adsorption materials (zeolite and silica gel), liquid absorption materials, and chemical reactions through solid chemical reaction materials or composite materials (CSMP) (16, 17). This section reviews all different TSMs studied by different researchers for their potential use in low-to-moderate temperature applications.

4.3.1. Sorption materialsTOP

4.3.1.1. Physical adsorption materialsTOP

Adsorption is based on the binding of a gas or liquid on the surface of a porous media (39). Adsorbents are highly porous solids. Since different molecules interact differently with the adsorbent, it is eventually possible to separate them (114). During the energy charging step (desorption process), heat added to the system is used to remove the gas or liquid molecules, for instance water, from the solid surface. When energy is needed the reverse reaction (adsorption) is promoted by adding water to the surface and the stored heat is released. An advantage of the sorption materials in comparison with PCMs is that, in the former, the energy release process can be designed to provide a cooling effect from the evaporator in summer or heating from the reactor in winter, whereas in the case of PCMs the fixed discharging temperature imposes a restriction on their application (17).

The desorption-adsorption storage process can be carried out in both open and closed configurations. Closed configurations mainly consist of two vessels, a reactor and a condenser-evaporator where water is stored. Higher temperatures for heating applications as well as lower temperatures for cooling can be reached in closed systems as compared to open systems. On the other hand, the pressure in the adsorption and desorption processes play a critical role. Thus, closed sorption systems present several benefits form a design point of view. Moreover, the energy density is lower compared to open systems since the adsorptive must be also stored. In open configurations, only water can be used as sorbate. Abedin et al. (115) developed a comparison between both types of thermochemical systems and concluded that the overall energy efficiency was 50 and 69% for closed and open systems, respectively.

Since the adsorption equilibrium is given by specific operating conditions (composition, temperature and pressure), by changing one of these parameters it is possible to regenerate the adsorbent. Thus, information about the adsorption equilibrium of the distinct species is vital to design and model adsorption processes (116). Most studied materials for energy storage by means of adsorption are zeolites and silica gel. New materials such as aluminophosphates (AlPOs) or metal-organic frameworks (MOFs) have been proposed (17, 117). Differences between zeolites and silica gel are related to their structure; while zeolites present a narrow pore size distribution determined by their crystalline structure, silica gel (which is composed of 99% of SiO2) has a larger range of pore sizes (39).

Silica gel is a desiccant widely used which allows working at a changing temperature bellow 100 °C. One of the main drawbacks for silica gel is that water adsorption occurs at high relative pressures, leading to a low water exchange (17). In the case of zeolites, the main commercial types are Zeolite 4A, 5A, 10X and 13X, which present a desorption temperature usually close to 150 °C (112, 118) that limits their application to low temperature solar systems.

Adsorption of water vapour in both silica gel and zeolite compounds has been investigated experimentally in several works (39, 112). Experiments have shown an almost linear relation between air temperature and humidity at system exit when fixed adsorption conditions are considered (39). Thus, by increasing the humidity ratio (kg H2O/kg material), air temperature is reduced in the energy releasing step. Regarding to the breakthrough curve, zeolite reaches its maximum outlet temperature which is kept almost constant until adsorption is over whereas in the case of silica gel the outlet temperature falls just after reaching its maximum (39).

Silica gel and zeolites have been tested in several research projects such as the HYDES and MODESTORE projects (2003–2012) (112, 119), which aim at the application of seasonal storage of solar thermal energy for space heating. For the material combination of silica gel and water, test results showed that the temperature lift is sufficient up to a water content in silica gel of about 13%. On the other hand, water contents of less than 3% are not realistically achievable given the temperature attainable from flat plate solar collectors and the temperature of an available heat sink. Therefore, the material has to operate between these limits of water content (3-13%). That means that the storage density of the material is significantly lower than initially expected. Lim et al. (120) built a lab scale closed loop system based on silica gel-water, in which the water uptake is approximately 29.8–56.7% the theoretical value. Sapienza et al. (121) studied the equilibrium and dynamics of the silica gel-water system by using Siogel, a commercial adsorbent. A water uptake of 12% was achieved. Deshmukh et al. (122) carried out thermal analysis of a closed silica gel-water system with the aim to develop a 18kWh storage system at an average temperature lift of 25 °C. Results showed that for these conditions 350 kg of adsorbent are necessary, with an energy storage density of 151 MJ/m3. Fernandes et al. (123) carried out simulations to evaluate a silica gel-water adsorption system which serves as TCES for a conventional solar system. Results indicated that annual energy savings up to 16% can be achieved in comparison with a conventional (water) storage system.

Results achieved with zeolites have shown a better performance due to its high water uptake compared to silica gel, which provides a high energy storage density. According to (112), Zeolite 13 X has a higher water vapour uptake rate than Silica gel 490 (up to 32% of its dry weight). Thus, Zeolite 13X, which was identified as one of the best adsorbents, has been also tested within international projects, such as E-Hub project (2010-2014) or COMTES project (2012-2016). Hauer et al. (124) developed and tested an open adsorption system based on zeolite 13X which provides heat to a district heating facility. Reported results showed an energy storage density of 446 MJ/m3. A domestic hot water system with storage based on zeolite 13X-water vapour was developed and tested by Köll et al. (125). Results demonstrated that an energy density of 640 MJ/m3 can be achieved, which allows achieving a solar fraction of 83.5% for both hot water and space heating. Tatsidjodoung et al. (126) also constructed a prototype using Zeolite 13X/H2O as the reactive pair, which was validated by means of a 1D mathematical model. Results on discharging process showed that, with a 40 kg zeolite system, an average temperature lift of 38 °C at the exit of zoolite vessel was attained during a period of 8 hours. As in similar prototypes, temperatures up to 180 °C were necessary to carry out the charging process. Analysis on the kinetics of the adsorption process for zeolite 13X/H2O showed that slow reaction rates reduce the efficiency significantly albeit only below a threshold value for the kinetics coefficient, which for the selected conditions was 0.001 [1/s] (127).

Table 20 shows the main solid adsorbents tested as TSMs. As shown, most of them present a discharge temperature below 70 °C and therefore an efficient low-temperature terminal heating system, such as underfloor heating, is fundamental. Regarding the charging step, thermal energy sources at temperatures of up to 180 °C for Zeolite and 95 °C for Silica gel are needed. Energy density of these TSMs varies between 151 and 648 MJ/m3, which is quite high in comparison with water-based sensible heat systems, although an optimized infrastructure must be designed to reduce the volume of external equipment, such as tanks, pumps, blowers or heat exchangers.

Table 20. TSMs. Solid physical adsorption. Properties
Material Charge temp. (°C) Discharge temp. (°C) Storage density (kJ/kg) Volumetric storage of material (MJ/m3) Volumetric storage of prototype (MJ/m3) Reference
Silica gel 127B/H2O 88 70–40   180 120 (112, 119)
Silica gel/H2O 95 25   151   (122)
Zeolite 13X/ H2O 180 65–55   648 208 (112)
  20–120 50–25   640.8   (125)
Zeolite 5A/ H2O 103 53–36 226.5 170 45 (128130)
Zeolite 13XBF/ H2O 150 75–47 399.6 277 - (131, 132)
Zeolite 4A/Air 180 35–10   576 432 (112)
  180 60–35 474.8 346 215 (118)
  230 60–35 529.9 421 243 (118)
Zeolite NaX/Air 180 57 787.5   8 (133)
  120 57 535.5   5 (133)
Zeolite 13X/Air 120–160 70–45 336   225 (129, 130)
  130–180 65   446 - (124)

4.3.1.2. Liquid absorption materialsTOP

The sorption process in absorption materials is based on liquids, which absorb the gas (usually water vapour) releasing the previously stored energy. In general, liquid materials present higher energy density than solid adsorption materials. However, the energy storage of the prototype decreases significantly in absorption systems since the storage in tanks of liquid must be considered. An advantage of liquid absorption materials is that they can be pumped and used directly as heat transfer fluid, which helps reduce the heat losses. The main components of an absorption process for energy storage are: a desorber and an absorber, a condenser and an evaporator, two solution storage tanks (diluted and concentrated solution) and an absorbate storage tank (134). The operating principle of a stored renewable energy based on liquid absorption materials for heating is: when energy is available (solar in most of cases) an aqueous solution is pumped from the tank to the desorber, where energy input is used to increase the vapour pressure to reach equilibrium. After that, if energy input continues, the solution becomes concentrated as water vapour is released, which is condensed and stored in a water tank. When energy is needed, the concentrated solution is sent to the absorber while water is pumped from the storage tank to the evaporator producing water vapour, which is absorbed by the solution, being the released heat used for air-conditioning proposes.

Several materials have been tested in closed absorption cycles for TCES, such as LiCl, NaOH, CaCl2 and LiBr. Main properties of these liquid absorption materials are shown in Table 21.

Table 21. TSMs. Liquid absorption materials. Properties
Material Charge temp. (°C) Discharge temp. (°C) Storage density (kJ/kg) Volumetric storage of material (MJ/m3) Volumetric storage of prototype (MJ/m3) Reference
LiCl salt/H2O 46–87 30–25 736.8 911 306 (112)
NaOH/H2O 95–150 70   900 18 (112, 135)
  95 32.8 / 56       (132, 136139)
        1566   (140)
CaCl2/H2O 117–138     382–1372   (98, 141, 142)
  130 165   777.6   (143)
LiBr/H2O 75–90 40–30   921.6   (134, 144)
  ≈40–110       368 (145)
  ≈40–110 35     263-331 (146)

Based on LiCl salt absorption process, a thermo-chemical accumulator (TCA) was patented by Olsson et al. (147), which is currently at the commercial level for cooling applications. TCA consists of a three-phase absorption process (solid, solution and vapour). The system works in batch mode. Water is desorbed from the solution in the charging mode and causes the solution saturation followed by the formation of solid crystals that fall under gravity into the vessel. In discharging mode, the saturated solution is pumped to a heat exchanger where it absorbs vapour coming from the evaporator, whose energy input is taken either from the environment (heating application) or from the building (cooling) (148). After that, the unsaturated solution passes though the crystals zone to reach saturation again before being stored. The condensation heat and released binding energy is transferred to the environment (cooling mode) or to the building (heating mode) (148). Laboratory test results showed an energy density for the material, LiCl salt, of 911 MJ/m3, although considering the entire TCES prototype the energy density results around 306 MJ/m3 (112). Hui et al. (149) evaluated seven absorption systems from an energy storage point of view. Results showed that the LiCl/H2O couple has an excellent storage capacity and efficiency, with the disadvantage of a high cost compared to other liquid absorbents (more than 14 times higher than CaCl2). Nevertheless, the high energy density of the LiCl-based system makes it an attractive choice from a storage capacity cost perspective resulting in one of the materials with lower cost per kWh stored (~6€/kWh) (150).

In the case of the NaOH system, a prototype for heating has been tested (112). The system works as a heat pump in which the driving force is the difference of the vapour pressures above water and NaOH solution (soda lye). In this system configuration, contrary to the TCA described above, the tanks are separated and works as a continuous process. Test results showed a good kinetics at desorption temperatures of 120 °C. The energy density of the system and prototype are 900 and 18 MJ/m3 respectively, but this prototype can be highly improved with an optimized system design (112). Another test carried out by Weber et al. (135) showed that, including tanks and heat exchangers, the total energy density could be three times higher compared to traditional hot water storage at 70 °C, and about six times higher for a tap temperature of 40 °C for low-temperature space heating. Fumey et al. (140) tested at lab-scale a conventional spiral fined tube heat exchanger where the absorbent (NaOH) flows along the fin from top to bottom. A temperature lift of 35 °C between the maximum absorbent temperature and the absorbate was measured, with a dilution from 50wt% to 27wt%. During desorption a concentration lift from 25wt% to 53wt% is achieved, which translates into a theoretically energy density of 1566 MJ/m3.

CaCl2-based system behaviour was analysed by Davidson et al. (98) for its use as liquid desiccant in an atmospheric-pressure chiller. Solar energy is stored in a liquid CaCl2 volume by heating the solution and vaporizing H2O. Energy is extracted as water is reabsorbed and/or the solution is cooled (142). The energy density of the material, which is dependent on how the tank is discharged, is 106 kWh/m3, similar to that of LiCl for the same operating parameters (98). Computational results showed that buoyancy driven flow induced by the presence of an immersed heat ex-changer is sufficient to heat and thermally stratify the storage fluid (142). Transport of mass across the density gradient between regions is limited by diffusion. Richter et al. (143) developed an experimental analysis on the absorption system based on CaCl2. In this work, storage is charged at 130 °C while the reverse reaction allows an energy discharge at 165 °C, which means a thermal upgrade of 35 °C and a thermochemical storage density of approximately 777.6 MJ/m3. Esaki et al. (151) assessed experimentally the use of a chemical heat pump for upgrading waste heat during the hydration of CaCl2, which occurs within a packed bed reactor. A waste heat temperature upgrading from 100 °C up to 155 °C was achieved with a performance coefficient of 0.48.

Liquid absorbent LiBr was also tested by N’Tsoukpoe et al. (134, 144) as a promising candidate for long-term energy storage in buildings. An 8 kWh energy storage prototype was built based on two storage tanks (water and solution: 88.5 kg) and two falling films heat exchangers (desorber/absorber, condenser/evaporator) assembled to the reactor, which produces a heating power of 1 kW. Several tests were carried out, focused in the charging process under practical conditions (25 °C-95 °C in the desorber and 10–30 °C in the condenser). It was demonstrated that a storage of 13 kWh is possible when charging the prototype with a thermal power of 2-5 kW. Discharging tests indicate absorption temperatures of about 30-40 °C, which can be low for space heating. Xu et al. (145) proposed an absorption solar energy storage system which uses a LiBr solution. A stored energy density of 368 MJ/m3 was achieved. Perier-Muzet and Le Pierres (146) assessed the efficiency of a LiBr/H2O absorption heat storage system integrated with a solar thermal facility for space heating. They analysed the impact of using a solution heat exchanger (SHX), which could improve both the energy efficiency and storage density up to 75% and 331 MJ/m3, respectively.

Another possibility is using liquid absorption materials for TCES in open systems. During absorption (discharging step) the concentrated solution is sent to an exchange surface where it gets in contact with an air stream. Humidity is removed from air and the solution becomes diluted by the absorption of vapour. During regeneration (reverse process) the solution is again concentrated by the mass and heat transfer with a hot air stream. In open absorption cycles the desiccants are regenerated against the ambient water vapour pressure (dew point of the ambient air) whereas the reference temperature is well above the ambient wet bulb temperature, thus open cycle regeneration requires lower regeneration temperatures and therefore higher collector efficiency (39). An open system based on CaCl2/H2O was tested by Bouché et al. (152), which, according to test results, could allow a thermal upgrade of approximately 65 K.

4.3.2. Chemical reactionsTOP

4.3.2.1. Solid chemical reaction materialsTOP

Energy storage by means of chemical reaction materials is based on using the heat obtained from an external source (e.g. solar) to drive an endothermic reaction. The products of the reaction are stored and, when energy is needed, brought together to induce the reversible reaction (exothermic). This group of energy storage materials present a higher energy storage density than previous materials. Main disadvantages could be a low chemical stability after cycling (loss on sorbent capacity) (129), slow kinetics associated to insufficient temperature rise in the reactor (153), and poor heat and mass transfer in gas-solid reactions (154). A number of salt hydrates have been analysed as potential candidates for TCES in buildings such as MgSO4·7H2O, MgCl2·6H2O and CaCl2·6H2O. Table 22 shows the properties of main chemical reaction materials.

Table 22. TSMs. Chemical reaction materials. Properties
Material Charge temp. (°C) Discharge temp. (°C) Storage density (kJ/kg) Volumetric storage of material (MJ/m3) Volumetric storage of prototype (MJ/m3) Reference
MgSO4·7H2O 150     1512 - (112)
  275–60 300–25   1800a - (155)
MgCl6H2O 130 64–50   ~2000 500 (129, 130, 156)
CaCl2·6H2O 165–190 50.1   1470   (157)
aThis value is considering the hydration process at 25 °C. Energy supplied along the dehydration process is 2000 MJ/m3. This energy is approximately 88% of the energy density of the corresponding dehydration reaction (155).

MgSO4·7H2O is a promising energy storage material with a high energy density (155). A characterization of MgSO4·7H2O as TSM was carried out by Bales et al. (112). The results obtained from TGA tests showed that the dehydration of MgSO4·7H2O occurs in three steps, namely, formation of MgSO4·6H2O, MgSO4·0.2H2O and finally MgSO4.

By analysing the DSC curve (112), it is seen that the third step of dehydration (production of MgSO4) is exothermic, which is contrary to expectations in dehydration reactions (first and second step are endothermic). According to Ruiz-Agudo et al. (158), the reason for the endothermicity of the final reaction is the recrystallization of an amorphous precursor. During hydration, MgSO4 takes up water to form MgSO4.6H2O. If the releasing energy system works at atmospheric pressure, the MgSO4 could provide energy for heating applications at 25 °C while in a closed system at low pressure a small amount of energy could be released at 50 °C (159). At 50 °C the material is unable to take up water and deliver heat (159). These values are a limitation to the system application for heating purposes. Okhrimenko et al. (160) analysed dehydration of magnesium sulphate at low water vapour pressure and the reaction mechanism. Experimental results showed that the water content in the solid phase after dehydration depends on water vapour pressure and temperature. The equilibrium constant K was found to follow Van’tHoff equation with ΔH=54.3 k/mol H2O (160). According to Ferchaud et al. (161), the reaction kinetics for the dehydration reactions of MgSO4·7H2O could reach a maximum for a water pressure of 50m bar.

Zondag et al. (156) carried out several dynamic tests to analyse the dehydration kinetics of MgSO4·7H2O, Al2(SO4)3·18H2O, CaCl2·6H2O and MgCl2·6H2O. To simulate the charging process, the first three materials were heated to 150 °C to provoke their dehydration while the CaCl2·6H2O was dried at 130 °C to avoid side reactions. After that, to release the energy stored, the materials were hydrated with vapour. The authors observed that sulphates had a much lower temperature rise in the reactor than CaCl2·6H2O and MgCl2·6H2O, which reached a temperature of around 50–68 °C depending on the reactor and vapour temperatures. In view of the results, MgCl2·6H2O was selected as the most promising material for energy storage due to its relatively low charging temperature (≥130 °C) and a discharging temperature sufficiently high to yield water heating (≤60 °C), as well as its high energy density (~2GJ/m3) and low price (<1€/kg) (129). MgCl2·6H2O was tested in a lab-scale prototype generating 150 W of thermal power (17 l of material and a steam volume flow of 510 l/min), with an effective energy density of 0.5GJ/m3 (129, 156). According to Barreneche et al. (157) the energy involved in the CaCl2 dehydration process is 1470MJ/m3.

4.3.2.2. Composite materialsTOP

Composite materials, also called composite “salt porous matrix” (CSPM), have been proposed to enhance the reaction kinetics and the poor heat and mass transfer in chemical reaction materials for energy storage. Composite materials usually consist of salt hydrates and an additive with a porous structure that works as host matrix with high thermal conductivity to improve the reaction rate and the heat release. Most studied materials to be used as additive are zeolites (98, 153, 162), metal foam (154, 163), expanded graphite (164166) and activated carbon (167). Table 23 shows the main properties of several composite materials for energy storage.

Table 23. TSMs. CSPM. Properties
Material Charge temp. (°C) Discharge temp. (°C) Storage density (kJ/kg) Volumetric storage of material (MJ/m3) Volumetric storage of prototype (MJ/m3) Reference
Na2S-graphite/H2O 95–80   8064     (164)
Na2S-cellulose/H2O >83 45–35 3960     (168)
SrBr2-ENG/H2O 80 35 1155.6 216   (166)
Zeolite 4A-CaCl2/H2O 130 25 3600 900   (98, 153, 162)
CaCl2 (30%wt)-silica gel 90 60 1020 822   (169)
CaCl2 (43%wt)-silica gel 80 30   760   (170)
CaCl2 (15%wt)-silica gel     746     (171)

A composite material consisting of a reactive mixture of sodium sulphide/water and graphite additives was analysed by Lammak et al. (164), which was filled in a tube-in-tube heat exchanger and operated between high temperature source and a sink temperature of 30-40 °C. The average heating and cooling power were about 3.79 kW and 0.23 kW, respectively. They found that the amount of adsorbed water could be increased drastically by using the graphite-based composite materials. In another work, Mauran et al. (166) analysed a system composed by SrBr2 implemented with an expanded natural graphite as reactant and H2O as refrigerant fluid. The prototype reactor, with a total volume of 1m3, was able to store 60kWh and 40kWh in heating and cooling modes respectively. Power released was 2.5kW for heating and 4kW for cooling applications, which was limited by a poor heat and mass transfer. Even though composite materials were expected to improve this issue, the transfer of heat at the inter-face between the consolidated composite and the wall of the exchanger posed a very strong limitation.

Mette et al. (153) proposed a new regeneration strategy for a thermochemical system based on a composite material composed by zeolite (matrix) and CaCl2, with the aim of reducing the regeneration temperature without affecting energy density. Simulation results showed that it is possible to reduce the regeneration temperature from 180 °C to 130 °C and therefore the process can be driven by solar thermal collectors. This implies a fractional energy saving higher than in the basic process without the proposed regeneration strategy. Wu et al. (169, 170) studied a CaCL2-silica gel composite material for energy storage. The results indicated that a 30wt% CaCl2 solution was the most stable and had the highest energy storage capacity: 822MJ/m3 at a charging temperature of 90 °C. In another work, Jabbari-Hichri et al. (171) studied by means of TG/DCS analysis three supporting materials, silica-gel, alumina and bentonite, mixed with a 15%wt of CaCl2. Results showed that the CaCl2-silica gel composite material had the highest energy storage density, with a value of 746 kJ/kg.

5. DISCUSSION OF RESULTSTOP

With the aim of comparing all reported TES materials for low-to-moderate temperature storage applications, Figure 3 illustrates the ranges of volumetric storage capacity of sensible, latent and thermochemical material groups.

Figure 3. Comparison of TES ranges of reported materials for low-to-moderate temperature applications

 

Sensible storage capacity ranges depend on temperature ranges in which materials operate. For building applications, water shows the higher storage density due to its high volumetric specific heat, being able to storage 250MJ/m3 for a temperature gradient of 60 °C (25–85 °C) in heating applications, and 42MJ/m3 for a temperature gradient of 10 °C (17–7 °C) in cooling applications. These values should be considered as maximum reference values, which could be reduced according to final building application.

Latent heat storage ranges are based on heat of fusion of reported materials for the specific melting temperature. Also, ranges of all commercially available organic and inorganic materials are reported according to data published in Lizana et al. (172). Metal alloys, sugar alcohols and salt hydrates present the highest volumetric storage capacity of all studied PCMs, being situated between 124–419 MJ/m3, 281–442 MJ/m3 and 218-514 MJ/m3, respectively.

Thermochemical heat storage ranges are drawn based on the energy storage density of materials without taking into account the whole systems’ components (tanks and heat exchangers), which can significantly reduce the effective material storage density by more than a 50% (16). Liquid absorption and chemical reaction processes show the highest energy storage capacity, being in the range of 900–1566 MJ/m3 and 1470-2000 MJ/m3, respectively.

Figure 4 illustrates volumetric latent heat capacity and melting temperature of all reported pure compounds and mixtures of PCMs tested in the literature by different authors: organics such as paraffins, fatty acids, esters, sugar alcohols, polyethylene glycols; inorganics such as salt hydrates and metals; and eutectics. Sensible TES processes in water for heating and cooling applications are also illustrated as a reference maximum value (yellow line).

Figure 4. Volumetric storage capacity of latent heat storage materials compared with sensible storage in water.

 

This figure allows identifying the PCMs with the highest volumetric storage capacity and with an appropriate melting temperature for heating, cooling and comfort applications. For cooling applications, those with the highest potential are lithium chlorate trihydrate [LiCiO3·3H2O] and the eutectic mixture of lithium nitrate trihydrate and zinc nitrate hexahydrate [LiNO3H2O and Zn(NO3)2·6H2O]. For comfort applications, lithium nitrate trihydrate [LiNO3·3H2O] and the eutectic mixture of [CaCl2 + NaCl + KCl + H2O] seem promising to reduce overheating; and for heating and solar applications, sodium sulphide pentahydrate [Na2S·5H2O], ammonium aluminium sulphate dodecahydrate [(NH4)Al(SO4)2·12H2O], barium hydroxide octahydrate [Ba(OH)2·8H2O] and sodium hydroxide monohydrate [NaOH·H2O] stand out as the best available compounds, with a storage density between 450 and 514 MJ/m3. On the other hand, despite the high volumetric storage capacity of some metal alloys and sugar alcohols, their melting temperatures are high, which reduces their applicability for building solutions.

Figure 5 shows the volumetric storage capacity and melting temperature of all reported TSMs tested in the literature by different authors: solid physical adsorption, liquid absorption, chemical reaction and composite materials. Sensible TES processes in water for heating and cooling applications are also illustrated as a reference maximum value (yellow line).

Figure 5. Volumetric storage capacity of thermochemical storage materials compared with sensible storage in water.

 

TSMs have the highest energy storage density considering all sensible and latent tested compounds. However, these values do not account for the volume required of other components for their implementation, such as tanks and heat exchangers. In the case of gas-solid thermochemical systems, the internal porosity of solids and the particle packing fraction (173) should be taken into account for the total infrastructure volume estimation. Furthermore, they often do not satisfy all requirements for building applications. Low discharge capacities as a consequence of a slow kinetics, variable thermal power over time, high cost and long thermal stability under cycling are common issues to be overcome. Among all tested materials for small-scale applications in buildings, Zeolite 13X (solid physical adsorption), LiCl salt/H2O (liquid absorption), LiBr/H2O (liquid absorption) and MgCl2·6H2O (chemical reaction) have the highest potential for building applications according to the results obtained by different authors (112, 125, 129, 130, 145, 146, 156). Considering all reported properties, MgCl2·6H2O is the most promising material for energy storage due to its high energy density (~2GJ/m3), relatively low charging temperature (≥130 °C), a discharging temperature sufficiently high to produce water heating (≤60 °C) and low price (<1€/kg). The tested prototype based on MgCl2·6H2O in the E-HUB (2010–2014) achieved an effective energy density of 0.5GJ/m3 (129, 130). However, additional research efforts are required to improve its chemical stability under conditions for seasonal storage (129).

6. CONCLUSIONSTOP

This paper reviews an extensive number of thermal energy storage (TES) materials technically developed for low-to-moderate temperature storage applications in buildings with the aim of identifying best available solutions. The results show that:

•  Up to 21 °C, for cooling applications, salt hydrates and their eutectics show the highest volumetric storage capacity, being placed in an energy density range of 300–387 MJ/m3, with melting points between 21 °C and 5 °C. Lithium chlorate trihydrate [LiCiO3·3H2O] and the eutectic mixture of lithium nitrate trihydrate and zinc nitrate hexahydrate [LiNO3H2O and Zn(NO3)2·6H2O] are the best available compounds, with a storage density of 387 and 366 MJ/m3, respectively. Also, latent heat storage in ice has a high potential due to the high availability, low cost and high storage capacity of 301 MJ/m3. However, its melting temperature could be lower for some domestic applications. In addition, sensible water storage remains currently as the most widely-used storage method for cooling purposes, with a volumetric storage capacity of 42MJ/m3 for a temperature gradient of 10 °C (17-7 °C).
•  Between 22 °C and 28 °C, for comfort conditions, salt hydrates and their eutectics show the highest volumetric storage capacity, with a range between 250 and 373 MJ/m3. Lithium nitrate trihydrate [LiNO3·3H2O] and the eutectic mixture of [CaCl2 + NaCl + KCl + H2O] are the greatest potential compounds for comfort purposes. They seem good suited to reduce overheating due to their very high storage density of 373 and 308 MJ/m3, and their melting points of 30 °C and 26.8 °C, respectively. However, most of salt hydrates are characterized by low thermal reliability for long-operation periods, phase segregation and subcooling, which limit their effective application.
•  Over 30 °C, for hot water, space heating and solar applications, a group of salt hydrates are identified as the best available compounds, with a storage density between 450 and 514 MJ/m3. They consist of sodium sulphide pentahydrate [Na2S·5H2O], ammonium aluminium sulphate dodecahydrate [(NH4)Al(SO4)2·12H2O], barium hydroxide octahydrate [Ba(OH)2·8H2O] and sodium hydroxide monohydrate [NaOH·H2O], with a melting temperatures of 96 °C, 95 °C, 78 °C and 64 °C, respectively. However, as for other salt hydrates, they present important drawbacks for their efficient implementation. This is why water and underground materials remain as the most widely-used storage mediums due to their high sensible storage capacity and moderate thermal diffusivity. Water is able to store 250MJ/m3 for a temperature gradient of 60 °C (25–85 °C). Besides, underground solutions show the benefit of using the ground as insulation, thus they store thermal energy more efficiently than above-ground solutions. Regarding thermochemical storage materials, despite their high energy densities and high storage ability for long-term storage periods due to their negligible heat losses, there is no available material that currently satisfies all requirements for commercial deployment. Among all tested materials, the most promising are Zeolite 13X (solid physical adsorption), LiCl salt/H2O (liquid absorption), LiBr/H2O (liquid absorption), and, above all, MgCl2·6H2O (chemical reaction) due to its high volumetric storage density (2GJ/m3 for the material and 0.5 GJ/m3 for the final prototype), relatively low charging temperature (≥130 °C), high discharging temperature (≤60 °C) and low price (<1€/kg). However, it suffers from a progressive decay of reactivity under cycling. Thermochemical energy storage is not mature enough for building applications. Additional research efforts are needed to optimize operation conditions, multi-cycling efficiency, material cost and systems design. In addition, thermochemical solutions require different tanks and heat exchangers, which reduce significantly the effective storage density and increase final costs.

Future research activities should be focused on experimental campaigns to validate and improve the performance of those materials with the highest potential with the aim of achieving practical solutions with high storage capacity, high thermal reliability and stability for long-operation periods, and competitive cost.

ACKNOWLEDGMENTSTOP

This work was supported as part of the ClimACT project (SOE1/P3/P0429EU) within the Interreg Sudoe Programme, funded by European Regional Development Funds. The authors gratefully acknowledge the financial support via two pre-doctoral contracts granted to Francisco Jesús Lizana Moral (FPU14/06583) from the Spanish Ministry of Education, Culture and Sport; and to Carlos Ortiz Dominguez (BES-2015-0703149) from the Spanish Ministry of Economy and Competitiveness (contracts CTQ2014-52763-C2-2-R and CTQ2017-83602-C2-2R, FEDER funds).

 

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