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The Viability of ThermalEnergy StorageKamil KaygusuzPublished online: 29 Oct 2010.
To cite this article: Kamil Kaygusuz (1999): The Viability of Thermal EnergyStorage, Energy Sources, 21:8, 745-755
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The Viability of Therm al Energy Storage
ÇKAMIL KAYGUSUZ
Department of Chemistry
Karadeniz Technical Unive rsity
Trabzon, Turkey
With rising energy costs and an increasing dem and for renewable energy sources,( )therm al energy storage TES system s are becoming an interesting option . TES is a
key component of any successfu l therm al system and a good TES shou ld allow
m inimum therm al energy losses. In this study, various ways of therm al conservation
are outlined and discussed, both theoretical and experimental. In th is respect, the
TES systems and their practical applications and som e selection criteria have also
been given .
Keywords thermal energy storage , sensible he at storage , latent heat storage,phase change material, domestic heating, solar ene rgy
s .Thermal ene rgy storage TE S has always been one of the most critical components
in re sidential solar space he ating applications. Solar radiation is a time -dependent
energy source with an inte rmittent characte r. The heating demands of a re sidential
house are also time dependent. Howeve r, the ene rgy source and the demands of a
building, in ge neral, do not match e ach othe r, e specially in solar he ating applica-
tions. The pe ak solar radiation occurs near noon, but the pe ak he ating demand is
in the late eve ning when solar radiation is not available . Thermal energy storage
provides a re servoir of energy to adjust this mism atch and to mee t the energy
needs at all times. It is used as a bridge to cross the gap between the energy source,
the sun, the application, and the building. So, the rmal ene rgy storage is e ssential in
s .the solar heating system Huang e t al. 1986; KakacË e t al. 1989 .
Thermal energy storage is conside red advanced energy technology, and the re
has been an incre asing intere st in using this essential technique for the the rmal
applications such as he ating, hot wate r, air conditioning, and so on. The se le ction
sof the TES systems mainly depends on the storage pe riod required i.e ., diurnal or
.se asonal , e conomic viability, operating conditions, and the like . In practice , m any
research and deve lopment activitie s related to ene rgy have been concentrated on
e fficient ene rgy use and energy savings, le ading to ene rgy conservation. In this
regard, TES systems appe ar to be one of the most attractive the rmal applications
s .DincË e r e t al. 1996 .
This pre sent work give s both expe rimental and theore tical re sults about
thermal ene rgy storage for re sidential heating applications. In the experimental
study, the viability of the the rmal energy storage concept was tested experimentally
by using phase change materials as a storage medium. The obtained experimental
re sult was used to compare the technical and economical diffe rences between
latent he at storage and sensible energy storage systems.
Received 14 January 1998; accepted 23 February 1998.Address correspondence to K. Kaygusuz, Department of Chemistry, Keradeniz Techni-
cal University, 61080 Trabzon, Turkey. Fax: 0462 325 3195.
745
Energy Sources, 21:745 ] 755, 1999
Copyright Q 1999 Taylor & Francis
0090-8312 r 99 $12.00 q .00
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Types of Therm al Energy Storage
Thermal ene rgy storage basically can be classified according to the way he at is
stored: as sensible he at in hot liquids and solids, as latent he at in me lts and vapor,
as the rmochemical heat appe aring in chemical re actions, and as sorption heat in
adsorption processes. The following sections give de tailed explanations of the se
type s of storage .
Sensible Heat Storage
In the sensible he at storage technique , energy is stored by changing the tempera-
ture of the storage medium. The amount of energy stored by a sensible he at device
is proportional to the difference between the storage input and output tempera-
tures, the mass of the storage medium, and the medium’s he at capacity. E ach
medium has its own advantage s and disadvantage s, but advantages of sensible -he at
storage in liquids include pumpability and high-volume utilization. Their pumpabil-
ity suits them for he at transport as well as storage , thereby facilitating he at
exchange , reducing constraints on system ge ometry, and m aking possible positive
s .methods of temperature separation such as diaphragms KakacË et al. 1989 .
W ate r usually is the pre ferred liquid for temperatures between 0 ] 100 8 C. It is
plentiful, e ssentially free , nontoxic, nonflammable, e asily pumped, has excellent
thermal properties, and is only mildly corrosive in the absence of oxygen. It is used
mainly in building applications where storage subsystem concepts and designs
divide conveniently into those most suitable for passive space he ating, domestic
water he ating, diurnal storage in active space heating and cooling systems, and
se asonal storage. Concepts for process he at storage in water tend to be similar to
those for large domestic hot wate r systems and large diurnal space-he ating installa-
tions. Table 1 give s propertie s of some sensible he at storage media.
s .Thermal storage for the short term le ss than one we ek is implemented most.
Examples are warm-wate r boilers in homes, and ice storage for air-conditioning
plants in office s. Short-te rm storage systems lower the maximum demand capacity
on the supply side . As a consequence, power companies can, for example, lowe r the
maximum capacity se tting and operate their power stations more efficiently. They
s .stimulate the application of storage via rate s tariffs .
Table 1
Propertie s of some sensible he at storage media
Density Specific he at Cost3s . s .Material kg rm J rkg.K $ r1000 kg
W ate r 1000 4190 0.5 ] 1.0
Rock 2500 ] 3500 880 4.0 ] 6.0
Iron 7860 500 50 ] 70
Concre te 2250 650 20 ] 30
Engine oil 888 1880 250 ] 400
Therminol T-66 750 2100 700 ] 750
s .Note: Costs are liberal marketing costs in Trabzon 1996 .
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The Viability of Therm al Energy Storage 747
s .The application of seasonal the rmal energy storage more than three months
is currently much le ss common. This is not due to a smalle r technical potential. On
the contrary, the re is a large amount of surplus heat in summer and surplus cold in
the winter. Further application is mainly de layed by economic factors, and to a
lesse r extent by technical ones.
In the past fifte en ye ars various applications of underground the rmal energy
storage have been studied. Much attention has been given to the deve lopment of
storage technique s. It appears that the deve lopment of a given type of storage
technique gre atly depends on local ge ological conditions. There fore , for example ,
in are as without natural storage structure s, small-scale storage systems in particu-
lar have been studied. The analysis of supply and demand systems has rece ived
little attention. Many we ll-functioning systems have been deve loped in the past few
ye ars which, howe ver, have not been implemented to a gre at extent.
Furthe rmore , it is remarkable that attention in the initial ye ars was primarily
aimed at he at storage . The drop in price s of prime energy and hydrotherm al
problems in storage have caused the number of applications of he at storage to be
re latively small. Attention to the application of cold storage has gre atly incre ased
in the past few ye ars, partly due to the increasing dem and for cooling in buildings
and the increased attention to environmental impacts caused by using chillers
s .UTES 1994 .
Latent Heat Storage
When a mate rial me lts or vaporizes, it absorbs heat; when it changes to a solid
s . s .crystallize s or to a liquid condenses , or m aybe to a gas, it gives back this he at.
This process of change of state , or phase change, can be used for storing he at.
s .Materials used for this purpose are called phase change mate rials PCMs . Typical
materials are water r ice , salt hydrate s, paraffin wax, and certain polymers. Energy
densities for latent heat storage are greate r than those for sensible heat storage,
s .re sulting in smaller and lighte r storage devices and lower storage losse s figure 1 .
The re lative ly constant temperature of storage can maximize colle ctor e fficiency
and minimize storage he at loss. Especially in a solar-assisted heat pump system for
domestic heating, the PCM stores energy from the solar colle ctors as a latent he at
s .at a ne arly constant transition temperature during me lting and solidification . It
can be used more preferably as a he at source than the wate r and rock storage for
a he at pump because the energy storage temperature of the PCM is around 25 ]s35 8 C for both calcium chloride hexahydrate and sodium sulfate decahydrate the se
.salt hydrates are the most commonly used . These temperature intervals are
suitable for solar-assisted he at pump applications in moderate climatic regions
s .Gultekin e t al. 1991; Kaygusuz 1988; Kaygusuz 1995 .ÈMany phase change mate rials have been investigated. While many studie s on
phase change he at the rmal ene rgy storage systems have been performed at
s .re latively low temperature s below 100 8 C for heat storage in home heating and
s .cooling units, studie s are sparse for higher temperature heat about 200 8 C used
for solar ene rgy systems and also for inte rmediate-temperature phase change
thermal energy storage. An ideal PCM must have the following feature s: appropri-
ate phase change temperature, high latent heat, low cost, ready availabil ity,
snontoxicity and nonflamm ability, uniform phase change characte ristics no subcool-
.ing or separation , and long life under repeated phase change .
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sFigure 1. Performance comparison of PCM, water, and rock storage systems Huang et al.
.1986
s .Abhat 1983 reviewe d low-temperature PCMs in the temperature range 0 ]120 8 C and inve stigated the ir me lting and freezing behavior. Short-te rm he at
storage systems, utilizing salt hydrates that melt in their crystallization wate r, have
sbeen proposed by many rese arche rs Morrison and Abde l-khalik 1978; Te lke s 1974;
.Jurinak and Abde l-khalik 1979; Huang e t al. 1986 . The most studied PCMs
include Glauber’ s salt, calcium chloride hexahydrate, sodium thiosulfate pentahy-
drate , sodium carbonate decahydrate , and disodium phosphate dodecahydrate . The
first two salt hydrates have especially rece ived conside rable attention because the se
are che ape r and have bette r thermal stability and resistance to corrosion than the
othe r salt hydrate s. The melting point, cost, and storage capacity of some salt
shydrates are given in table 2 Carlsson e t al. 1979; Parisini 1988; Brandste tte r 1988;
.Hahne 1996 .
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The Viability of Therm al Energy Storage 749
Table 2
Propertie s and cost of some salt-hydrates
6Melting Density Latent he at Cost Storage 10 kJ3s . s . s .Salt-Hydrate point 8 C kg rm kJ r kg $ r 100 kg of $ kg
CaCl .6H O 29 1710 176 6 250 41662 2
Na SO .10H O 32 1460 252 5 170 34002 4 2
Na CO .10H O 33 1440 248 9 230 25552 3 2
Na HPO .12H O 36 1520 273 19 510 26842 4 2
Na S O .5H O 47 1665 210 30 1010 33662 2 3 2
s .Source: Costs are from the Chemical Marketing and Drug Report 1996 .
Thermochemical Energy Storage
The chemical he at storage unit so far store s he at at high or low temperature by
using chemical reactions. Despite a number of proposals regarding chemical
storage systems in chemical engineering rese arch, to our knowledge , the re has
been no bre akthrough in this fie ld so far. Howeve r, the re have been deve loped five
different chemical he at storage technologies: three for high-temperature storage
and two for low-temperature storage . Metal hydrite s have been examined for use in
chemical he at pumps using hydroge n at pressure s substantially lower than the
saturation pressure. Metallic salts combined with ammonia have also been exam-
ined as a me ans of the rmochemical ene rgy storage. Temperatures can be lower
than those of comparable sensible he at systems so that he at losse s during long-te rm
cycles can be reduced. The reve rsible thermal decomposition of several inorganic
s s . .substances e .g., Ca O H , CaCO , ZnSO , and NH HSO has recently been2 3 4 4 4
s .studied JETRO 1989; Casarin and Ibanez 1993 .
Exp erim en tal Setup
The water-based system inve stigated in this experimental study is shown in figure 2,
and the system parameters are listed in table 3. As shown in figure 2, this system
consists of the solar colle ctors, ene rgy storage tank filled by PCM, wate r-to-air he at
Figure 2. Schematic diagram of the base solar energy system
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Table 3
W ater-based system parameters
Collector
Number of glass cove rs 1
Thickness of glass cove r 0.004 m
Refractive index 1.45
Collector plate absorptance 0.90
Colle ctor emittance 0.85
Collector e fficiency factor 0.852
Back and side losse s 1.20 kJ r h m K2
Mass flow rate 40 kg r h m2
Total colle ctor area 30 m
Number of colle ctors 18
System circu it pipe
Length 40 m
Diameter 0.04 m
Heat loss 20 kJ r h K3s .Fluid density water 1000 kg rm
Fluid specific heat 4.197 kJ rkg K
Ambient temperature 18 8 CEnergy storage tank
3V olume 3.65 m
2s .Therm al loss 0.210 W r m . 8 Cs .Shape L r D 2.46
Initial temperature 18 8 C
exchange r, wate r circulating pump, and other me asuring and control equipment. A
de tailed description of the expe rimental se tup was given in previous studie s
s .Kaygusuz e t al. 1993; Kaygusuz 1993 .
Configuration of the Storage Tank
Figure 3 shows the configuration chosen for the storage tank. It consists of a vesse l
packed in the horizontal dire ction with cylindrical tubes. The ene rgy storage
s . smaterial calcium chloride hexahydrate is inside the tubes the tubes or containers
. s .are m ade of PVC plastic , and the heat transfe r fluid wate r flows paralle l to them.
The storage tank contains cylindrical PV C containe rs filled with PCM. The void
s .fraction the ratio between the fluid volume and the storage tank volume is 0.3.
The inside volume and inside surface are a of the ene rgy storage tank are ,
re spective ly, given by V and A . The number of cylindrical PVC containers insidest st
the storage tank is N . The radius of the cylinde r containe rs is r , and the length ofc c
the cylindrical tube containers is given by L. Also, the radius and length of the
energy storage tank are given by R and L , re spective ly. The r rL is 0.01 and thisst st c
ratio is small enough to minimize radial heat conduction in the storage m aterial
s .Kaygusuz 1995 .
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The Viability of Therm al Energy Storage 751
Figure 3. Schematic configuration of the ene rgy storage tank
Results an d Discu ss ion
Figure 4 shows the temperature variation with time for Na SO .10H O as a PCM2 4 2
for an energy storage application. This figure was obtained during the he ating
pe riod of 1.0 kg of PCM in the sm all cylindrical stainless ste el container. A detailed
s .description of this container is given in a previous study Kaygusuz 1988 .
Figure 4. Temperature variation with time for sodium sulfate decahydrate 1: water inle t
temperature 2: water outle t temperature 3: temperature of PCM
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Figure 5 also shows the temperature variation with time for calcium chloride
hexahydrate as a PCM for an ene rgy storage application. This figure shows the
s .he ating pe riod of the PCM 1.0 kg in the same cylindrical containe r. Figures 4 and
5 show the the rm al behavior during the melting period for pure PCMs obtained
from Merck Chemical Company.
Figure 6 shows the temperatures of the indoor and outdoor air and outlet
water of the storage and total solar insolation with time of day for TES applica-
tion. As shown in figure 6, the total solar insolation was at a maximum value of
900 W rm2
at a local time of 12:00.
Figure 7 also shows the temperature variation of calcium chloride hexahydrate
with time of day in the storage tank shown in figure 3. As shown in figure 7, the re
Figure 5. Temperature variation with time for calcium chloride hexahydrate
Figure 6. Temperature and insolation variations with time of day 1: insolation 2: outle t
water temperature of storage 3: indoor air temperature 4: outdoor air temperature
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The Viability of Therm al Energy Storage 753
Figure 7. Temperature variation of calcium chloride hexahydrate with time of day in
storage tank
T1: upper temperature
T2: middle temperature
T3: bottom temperature
is a temperature stratification in the tank, but differences between the three points
are small, so we say there is semistratification in the tank.
Figure 8 shows the variation of Ta, Tind, Tmean, Tcol2, Tcol1, and Tout with
time of day for the same TES system. Around solar noon, the temperatures of
storage outle t and collector inlet routlet are roughly at m aximum value because the
solar insolation is at maximum at solar noon. This re sult shows that the expe rimen-
tal re sults agree with theoretical re sults.
Con clus ions
Energy is a commodity for which we shall continue to pay an increasing price .
Furthe rmore, the inve stment and capital costs of powe r plants are high. In
addition, the environmental damage due to thermal power gene ration is an
important consideration for Turkey and all othe r countrie s. There fore , TES is a
key component for any the rmal system, and a well-designed TES system should
allow minimal the rmal energy losse s, le ading to energy savings, while permitting
the highe st possible extraction efficiency of the stored thermal energy.
From the experimental and theore tical inve stigations, we conclude that the r-
mal ene rgy storage is an important component in cold and moderate climatic
conditions such as Erzurum and Trabzon in Turkey, re spectively. In Erzurum, the
winter se ason is ve ry cold but has more sunny days. Therefore, using solar energy
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Figure 8. Temperature variation with time of day
Ta: ambient air temperature
Tind: indoor air temperature
Tm: mean temperature of storage
Tc2: collector outlet water temperature
Tc1: collector inle t water temperature
Tout: storage outlet temperature
with the TES system will give more ene rgy for domestic he ating. O n the other
hand, in the case of Trabzon, the winter se ason is mild but has more cloudy days.
There fore , a solar assisted he at pump system should be used with ene rgy storage
for residential he ating.
The following concluding remarks can be given from this study:
v Phase-change energy storage technology is still in the re search and deve lop-
ment stage and should not be ove rlooked because of its pre sent high cost
compared with water and rocks.v This technology could also be used to leve l the peak output of the utility
powe r ge neration and off-peak storage for residential heating applications
with air and water he at pumps.v The se lection of the thermal energy storage systems mainly depends on the
s .storage period required e.g., daily or se asonal , e conomic viability, and
operating conditions.v From the viewpoint of the rm al stability, corrosion e ffe ct, and economy,
sodium sulfate decahydrate and calcium chloride hexahydrate have more
advantage s compared with othe r phase change mate rials.v Substantial energy savings can be re alized by taking advantage of TES when
implementing techniques such as using waste ene rgy and surplus he at,
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The Viability of Therm al Energy Storage 755
avoiding he ating and air conditioning equipment purchase s, and reducing
e le ctrical demand charge s.v Thermal energy storage can reduce the time or rate mismatch between
energy supply and energy dem and, the reby playing a vital role in energy
savings. Also, TES can play a vital role in mee ting socie ty’s needs for more
e fficient, environmentally benign energy use in various sectors.
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system } CaCl .6H O } made congruent through modification of the chemical compo-2 2
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