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CHAPTER12
THERMALENERGYSTORAGETECHNOLOGIES
CliffordK.HoandAndreaAmbrosini,SandiaNationalLaboratories
Abstract
Thermalstoragetechnologieshavethepotentialtoprovidelargecapacity,long-durationstoragetoenablehighpenetrationsofintermittentrenewableenergy,flexibleenergygenerationforconventionalbaseloadsources,andseasonalenergyneeds.Thermalstorageoptionsincludesensible,latent,andthermochemicaltechnologies.Sensiblethermalstorageincludesstoringheatinliquidssuchasmoltensaltsandinsolidssuchasconcreteblocks,rocks,orsand-likeparticles.Latentheatstorageinvolvesstoringheatinaphase-changematerialthatutilizesthelargelatentheatofphasechangeduringmeltingofasolidtoaliquid.Thermochemicalstorageconvertsheatintochemicalbonds,whichisreversibleandbeneficialforlong-termstorageapplications.Currentresearchineachofthethermalstoragetechnologiesisdescribed,alongwithremainingchallengesandfutureopportunities.
KeyTerms
Thermalstorage,sensiblestorage,latentstorage,thermochemicalstorage,long-durationstorage
Introduction
Increasingpenetrationsofintermittentrenewableenergysources(e.g.,photovoltaics[PV]andwindenergy)haveincreasedtheneedforenergystoragetechnologiestoaccommodatedailyperiodsofovergenerationandpeakloads.Thesediurnalenergy-storagerequirementsarecategorizedinthischapterasshort-durationandspanperiodsfromsecondstohourswithcapacitiesrangingfromkilowattstogigawatts.Previousstudieshavesuggestedthatthedecreasingcostsofbatteriesandassociatedtechnologiesmayenablebatterysystemstomeettheshort-durationneedsofthegridwithhighpenetrationsofintermittentrenewableenergysystems[1,2].However,recentstudieshaveshownthatlong-durationenergystorage(daystomonths)willbeneededtoaccommodate100%renewable(orcarbon-free)energygeneration[3].Inaddition,long-durationenergystoragewillbeneededtoincreasethesecurityandresilienceoftheelectricalgridinthefaceofincreasingnaturaldisastersandintentionalthreats.
ThermalStorageApplications
Figure1
showsachartofcurrentenergystoragetechnologiesasafunctionofdischargetimesandpowercapacityforshort-durationenergystorage[4].Withintherangeofshort-durationenergystoragecapacities,applicationsincludereserveandresponseservices(1–100kW),transmissionanddistributionsupportgrid(100kW–10MW),andbulkpowermanagement(10MW–1GW).Althoughthermalstoragetechnologyisincludedinthechartascryogenicenergystorage,hotthermalstorageusingsensible,latent,orthermochemicalmethods[5,6]isnotshown.Commercialconcentratingsolarpower(CSP)usingsensibleheatstoragehasdemonstratedtheabilitytoprovideontheorderof100MWofpowercapacityover10hours(~1GWh)forbothgridsupportandbulkpowermanagement.
Thermalstoragetechnologiesarealsobeingconsideredfornuclearpowerplantstoincreasetheflexibilityofthesetraditionallybaseloadsystems[6].Attimesoflowornegativeelectricityprices,
Chapter12ThermalEnergyStorage
heat(orelectricity)generatedbythenuclearreactorwouldbesenttothermalstorage.Attimesofhighelectricityprices,theheatfromthereactorandthermalstoragewouldbeusedtoproducemaximumelectricityoutput(
Figure2
).NewGenerationIVnuclearreactorsdeliverhighertemperaturestothepowercyclerelativetowater-cooledreactors,whichisbeneficialforthermalstoragebecauseathighertemperatures,lessstoragematerialisrequiredtodeliveradesiredamountofthermalpower.Inaddition,thehighertemperaturesenablemoreefficientthermal-to-electricpowerconversion.Addingthermalenergystoragetogeothermalpowerplantstoincreaseflexibilityanddispatchabilityhasalsobeenconsidered[7].
Figure1.Dischargetimeandcapacityofvariousenergystoragetechnologies[4].Hotthermalstoragetechnologiesarenotshownbutcanprovidehundredsofmegawattsformanyhours
Chapter12ThermalEnergyStorage
Figure2.Diagramillustratinghowthermalstoragecanincreasetheflexibilityoftraditionalbaseloadpowerplantsthatrelyonthermalenergy[6].
TechnologyOverview
Theremainderofthischapterprovidesasummaryofthermalstoragetechnologies,whichcanincludesensible,latent,andthermochemicalsystems.Sensiblestoragereliesonatemperaturedifferencewithinthestoragemediumtoenableusefulworktobeperformed,suchasusinghotmoltensalttoheatwaterandgeneratesteamtospinaturbineforelectricityproduction.Latentstorageinvolvesstoringheatinaphase-changematerialthatutilizesthelargelatentheatofphasechange,forexample,duringisothermalmeltingofasolidtoaliquid,whichrequiresheat,andsubsequentfreezingoftheliquidtoasolid,whichreleasesheat,isothermally.Thermochemicalenergystorage(TCES)reversiblyconvertsheatintochemicalbondsusingareactivestoragemedium.Whentheenergyisneeded,areversereactioncombinesthereactants,releasingenergy.
Table1
summarizesthedifferentthermalstoragetechnologiesandkeyattributes.
Table1.Summaryofthermalstoragetechnologies
SensibleHeatStorage
[5,8-12]
LatentHeatStorage
[5,9,10,12,13]
ThermochemicalStorage
[9,11,13]
Storagemechanism
Energystoredastemperaturedifferenceinsolid(e.g.,concrete,rock,sand)orliquidmedia
(moltensalt)
Energystoredusingphasechangematerials(e.g.,salts,metals,organics)
Energystoredinchemicalbonds
EnergyDensity
~200–500kJ/kg(for
~200–400°C
temperaturedifferential)
~100–200kJ/kgfornitratesalts;~200–500kJ/kgformetals;~1000
kJ/kgforfluoridesalts
~300–6,000kJ/kg
Chapter12ThermalEnergyStorage
SensibleHeatStorage
[5,8-12]
LatentHeatStorage
[5,9,10,12,13]
ThermochemicalStorage
[9,11,13]
Advantages
Demonstratedlargeenergycapacity(~GWh)
Inexpensivemedia
Solidmediadoesnotfreezeandcanachieve
>1000°C
GoodforisothermalorlowTapplications
Canprovidelargeenergydensitywithcombinedsensibleandlatentheatstorage
Largeenergydensities
Smallheatlosses
Potentialforlong-termstorage
Compactstoragesystem
OxideTCESStableathightemperatures(>
1000°C)
Challenges
Requiresinsulationtomitigateheatlosses
Lowerenergydensityrequireslargervolumes
Moltensaltsfreezeat
~200°C.
Potentialforcorrosion
ForlargerT,mayneedcascadedsystems(addscostsandcomplexity)
Lowmaturity
Highercomplexity
Lowmaturity
Highercapitalcosts
Mayrequirestorageofgaseousproducts
Maturity
High
Low
Low
Cost
~$1/kgformoltensaltsandceramicparticles
~$0.1/kgforrockandsands
~$1/MJ–$10/MJ(systemcapitalcost)
~$4/kg–$300/kg
~$10/MJ–$100/MJ(systemcapitalcost)
~$10/MJ–$100/MJ(systemcapitalcost)
StateofCurrentTechnology
Sensibleheatstorage
Sensibleheatstorageconsistsofheatingamaterialtoincreaseitsinternalenergy.Theresultingtemperaturedifference,togetherwiththermophysicalproperties(density,specificheat)andvolumeofstoragematerial,determineitsenergycapacity(JorkWh):
Esensible
=ρV
THc
∫
TC p
(T)dT
(1)
Desirablefeaturesofsensiblestoragematerialsincludelargedensities,ρ(kg/m3),largespecificheats,cp(J/kg-K),andlargetemperaturedifferencesbetweenthehotandcoldstates,TH–TC(K).Keyadvantagesincludealowcostofsensiblestoragematerials,highmaturitylevel,andlargeenergycapacities.
Table2
providesasummaryofthermophysicalpropertiesofvarioussensiblesolidandliquidstoragemedia.
Chapter12ThermalEnergyStorage
Table2.Thermophysicalpropertiesofsensiblestoragemedia(adaptedfrom[5]).Calculationofvolumetricandgravimetricstoragedensitiesassumeatemperaturedifferentialof350°C.
StorageMedium
SpecificHeat(kJ/kg-K)
Density(kg/m3)
TemperatureRange(°C)Cold Hot
GravimetricStorageDensity
(kJ/kg)
VolumetricStorageDensity(MJ/m3)
Solids
Concrete
0.9
2200
200
400
315
693
Sinteredbauxiteparticles
1.1
2000
400
1000
385
770
NaCI
0.9
2160
200
500
315
680
Castiron
0.6
7200
200
400
210
1512
Caststeel
0.6
7800
200
700
210
1638
Silicafirebricks
1
1820
200
700
350
637
Magnesiafirebricks
1.2
3000
200
1200
420
1260
Graphite
1.9
1700
500
850
665
1131
Aluminumoxide
1.3
4000
200
700
455
1820
Slag
0.84
2700
200
700
294
794
Liquids
Nitratesalts
(ex.KNO3-0.46NaNO3)
1.6
1815
300
600
560
1016
TherminolVP-1®
2.5
750
300
400
875
656
Siliconeoil
2.1
900
300
400
735
662
Carbonatesalts
1.8
2100
450
850
630
1323
CaloriaHT-43®
2.8
690
150
316
980
676
Sodiumliquidmetal
1.3
960
316
700
455
437
Na-0.79Kmetaleutectic
1.1
900
300
700
385
347
Hydroxidesalts(ex.NaOH)
2.1
1700
350
1100
735
1250
Silicon
0.71
2300
1900
2400
250
575
CommercialCSPplantsthatemploysensiblethermalstoragewithover1GWhofstoragehavebeendeployedworldwide.Forcomparison,Figure3showsthetotalnumberoflarge-scalebatterydemonstrationfacilitiesintheUnitedStatesattheendof2017alongwithtwoCSPplants.EachCSPplantprovidesmoreenergystoragecapacitythanall~100PVdemonstrationfacilitiescombined.
Chapter12ThermalEnergyStorage
1800
1600
EnergyStorageCapacity(MWh)
1400
1200
1000
800
600
400
200
0
Large-ScaleBatteryStorage(~100plantsinU.S.atendof2017)
CrescentDunesCSPPlant(molten-saltstorage)
1680
1100
742
SolanaCSPPlant(molten-saltstorage)
Figure3.ComparisonofenergystoragecapacityforbatteryandCSPplants.Batterydatafrom
U.S.EnergyInformationAdministration[14].
CurrentImplementation
Currentimplementationofhigh-temperaturesensibleheatstorageforelectricityproductionusesliquids(e.g.,moltensalts)andsolids(concrete,rocks).
Liquid
Moltennitratesalt(60%NaNO3,40%KNO3)isbeingusedincommercialCSPplantsaroundtheworldtoprovidegigawatt-hoursofthermalenergystorage.Ithasalowvaporpressure,soitisnotpressurizedattypicalstoragetemperaturesupto~600°C,anditcanbepumpedfromonelocationtoanother.
Figure4showsaphotographandschematicofthe110MWCrescentDunesCSPplantwith1.1GWhofthermalstorageusingmoltennitratesalt.Moltensaltisheatedinareceiverontopofatowerbyconcentratedsunlightfromafieldofheliostats.Thehotmoltensalt(~565°C)flowstoahotstoragetank(righttankinFigure4).Whenneeded,moltensaltispumpedfromthehotstoragetanktoaheatexchangerwhereitheatswaterandgeneratessteamtospinaturbine/generatorforelectricity.Thecooledmoltensalt(~300°C)ispumpedtoacoldstoragetank(lefttankinFigure4)andbacktothereceivertobeheatedwhenthesunisshining.CSPplantscanoperatewithlargecapacityfactors(70–80%)andprovidedispatchableenergy.
Chapter12ThermalEnergyStorage
SolartoThermalConversion ThermalStorage ElectricityGeneration
SolarThermal
Receiver
HotStorage
HeatExchanger
PowerBlock
HeliostatField ColdStorage
Figure4.Top:110MWCrescentDunesCSPplantwith1.1GWhofthermalstorageusingmoltennitratesalt[15].Bottom:Schematicofsensibletwo-tankthermalstoragesysteminaCSPplant.
Solid
Solidthermalstoragehasbeenusedinseveralcommercialanddemonstrationfacilities.In2011,GraphiteEnergydevelopeda3MWeCSPplantinLakeCargelligoinNewSouthWales,Australia,thatusedgraphiteblocksinthereceiversontopofmultipletowers.Thegraphiteblocksinthereceiver,irradiatedbyconcentratedsunlight,servedasboththestoragesystemandboilertogeneratesteamforpowerproduction.
EnergyNest,basedinNorway,developedaconcrete-basedthermalenergystoragesystemthatconsistsofanarrayofmodularpipesfilledwithconcreteandsteeltubes.Thetubescarryheat-transferfluidthatcanheattheconcretewhenchargingandextractheatfromtheconcretewhendischargingtopoweraturbine/generatororprovideprocessheating.Thesystemcancharge/dischargein~30minutesandthestoredenergycanlastforseveraldayswithlessthan2%heatlossper24hoursforlarge-scalesystems.
Chapter12ThermalEnergyStorage
SiemensGamesainGermanyhasdevelopeda130MWhtElectricThermalEnergyStorage(ETES)systemcomprisesrocksstoredinabuilding.Airisresistivelyheatedusingelectricity(whenpriceislow)andpasseddirectlythroughthebedofrocks.Therocksareheatedto~600°C,and,whenneeded,airispassedthroughthehotrockstoheatsteamforaRankinepowercycle.The130MWhtdemonstrationplantbecameoperationalin2019,andthecompanyisplanningadesignfora30MWcommercialpilotplant.
Challenges
Therelativelylowenergydensityofsensible-heatstoragematerialsrequireslargevolumesofmaterialforlarge-capacityenergystorage,whichincreasestheoverallstoragecost.Inaddition,somepowercyclesthatemployrecuperationtoincreasethethermal-to-electricefficiencyrequirerelativelylowtemperaturedifferentialsbetweenthehotandcoldstatesofthestoragematerial.Forexample,thesupercriticalCO2recompressionBraytoncyclerequiresatemperatureincreaseofonly~200°Cintheprimaryheatexchanger[16].Asaresult,therequiredmassinventoryofstoragematerialmustincreasetodeliverthesameamountofenergyforalowertemperaturedifferential,whichincreasescosts.ThetargetcapitalcostfortheU.S.DepartmentofEnergy(DOE)CSPprogramis$15/kWhfortheentirethermalstoragesystem.
Moltensaltsfreezeat>200°C,whichrequiresexpensivetraceheatingtomaintainallcomponentsattemperatureswellabovethefreezingpoint.Ifthesaltfreezes,flowcanbeblocked,andthawingmustoccurbeforeoperationcanbegin.StresswithinthelargestoragetankshasalsocausedissuesatCSPplants.Thermalgradientsatthebaseofthetankcancreatethermomechanicalstressesthatdamagethetankstructure.Appropriateconsiderationofthermomechanicalstressesiscriticaltothedesignoflarge-scalethermalstoragetanks.
Opportunities
Anumberofinstitutionshavebeenpursuingsmall,sand-likeparticle-basedthermalstorageforCSPplantsandstand-alonethermalenergystoragesystems.Unliketheprevioussolid-basedthermalstoragesystems,ratherthanpassingairoraheat-transferfluidthroughthestoragemedia,theparticlesareheateddirectlyandconveyedthroughaheatexchangertoheattheworkingfluid[8].Theparticlesareliftedtothetopofthereceiverwheretheyareirradiatedandheatedbyconcentratedsunlight.Thehotparticlesflowintoaninsulatedstoragetankwheretheycanbeheldforhoursordays.Whenneeded,theparticlesarereleasedthroughaparticleheatexchangertoheataworkingfluidthatspinsaturbine/generatorforelectricityproduction(
Figure5
).
Chapter12ThermalEnergyStorage
Particleelevator
Particlehot
storagetank
Particle-to-working-fluidheat
exchanger
Particlecold
storagetank
Particlecurtain
Particlecurtain
Apertur
Aperture
Fallingparticlereceiver
Figure5.Illustrationofahigh-temperaturefallingparticlereceiverwithtower-integratedstorageandheat-exchangerfordispatchableelectricityproduction[17]
Liketheothersolid-basedthermalstoragetechnologies,inexpensiveparticlestoragecanaccommodateincreasingpenetrationsofrenewablesbyallowingheattobestoredwhenelectricitydemandislow,andthenusingthatstoredheattoproduceelectricitywhendemandandpricesarehigher.Thistime-shiftingofenergyproductionandusecanincreasetheflexibilityoftraditionalbaseloadpowerplants,includingnuclearandgeothermal.
Solidstoragemediahastheadvantageofbeinginert,inexpensive,non-corrosive,andeasytohandle.Inaddition,manysolidmaterialsexhibitamuchwideroperatingtemperaturerangethanmoltensalts.Rock,sand,andsinteredbauxitehaveallbeenutilizedinthermalstoragesystemsandcanoperateinsub-freezingto>1000°Ctemperatures.Largevolumesofbulksolidmaterialcanalsoprovideself-insulationfromthecoolerambientenvironment.Asthevolumeofthebulkstoragetankincreases,theratioofitssurfaceareatovolumedecreases,whichreducesheatloss.So,largestoragetanksorcontainmentsystemsyieldbothperformancebenefitsandeconomiesofscale.
Pumpedthermalenergystorageuseselectricityinaheatpumptotransfersheatfromacoldreservoirtoahotreservoirsimilartoarefrigerator.Whenelectricityisneeded,theheatpumpisreversedtoallowtheheatfromthehotreservoirtodriveaheatengineandspinaturbine/generator.Thelargepotentialtemperaturedifferencesbetweenthehotandcoldreservoirscanenablehighlyefficientpowercycles.Malta,aspinofffromGoogleX,isdesigningapumped-thermalenergystoragesystem(Figure6).
Chapter12ThermalEnergyStorage
Figure6.Malta’spumpedthermalenergystorageconcept[Malta,2020#13799]
MITisinvestigatinganotherstoragetechnologythatwouldusecheaporexcesselectricitytosensiblyheatmoltensilicontoultra-hightemperaturesinlarge,insulatedgraphitetanks.Themoltensiliconwouldbeheldat“cold”temperaturesof~1900°C(aboveitsmeltingpointof1414°C)andheatedwithelectricalheatingelementstonearly2400°C,whereitisstoredinasecond“hot”tank.Whenelectricityisneeded,themoltensiliconispumpedfromthehottankthroughtubesthatemitthermalradiationtomultijunctionphotovoltaiccellsthatgenerateelectricity.Thecooledmoltensiliconisthencollectedinthecoldstoragetank.
Latentheatstorage
Latentheatstoragesystemsusethelatentheatofphasechangetostoreenergy.Latentheatoffusionistheenergyrequiredtochangethestateofsubstancefromasolidtoaliquid,andlatentheatofevaporationistheenergyrequiredtochangethestateofsubstancefromaliquidtoagas.Saltsandmetalscanbemelted,andthecombinedsensibleandlatentheatcanbeusedtostoretheaddedthermalenergy.
Table3
summarizesthethermophysicalpropertyvaluesofdifferentlatent-heatstoragematerials.Thelatentheatofreaction(kJ/kg)showninthesecondcolumnwouldbeaddedtothesensibleheatcapacityinEq.(1)todeterminethetotalheatcapacityoflatentheatstoragematerialsbeingheatedfromonestatetoanother.Inmostcases,thematerialsaresolid/liquidphasechangematerialsthatarestoredasliquidsthatcansubsequentlyreleaseenergywhenconvertedbacktoasolidstate.Someliquid/gassubstances(nitrogenandoxygen)arealsoshownbecausecryogenic“liquidair”storagehasalsobeendemonstratedforgridenergystorageapplications.
Chapter12ThermalEnergyStorage
Table3.Thermophysicalpropertiesofphase-changestoragematerialsatstandardconditions,unlessotherwisenoted(adaptedfrom[5])
StorageMedium
SpecificHeat(kJ/kg-K)
LatentorReactionHeat
(kJ/kg)
Density(kg/m3)
MeltingPoint(°C)
BoilingPoint(°C)
GravimetricStorageDensity(kJ/kg)
VolumetricStorageDensity
(MJ/m3)
Liquid/SolidPhaseChangeMaterials
Aluminum
1.2
397
2380
660
-
397
945
Aluminumalloys(ex.Al-0.13Si)
1.5
515
2250
579
-
515
1159
Copperalloys(ex.Cu-0.29Si)
-
196
7090
803
-
196
1390
Carbonatesalts(ex.Li2CO3)
-
607
2200
726
-
607
1335
Nitratesalts
(ex.KNO3-0.46NaNO3)
1.5
100
1950
222
-
100
195
Bromidesalts(ex.KBr)
0.53
215
2400
730
-
215
516
Chloridesalts(ex.NaCI)
1.1
481
2170
801
-
481
1044
Fluoridesalts(ex.LiF)
2.4
1044
2200
842
-
1044
2297
Lithiumhydride
8.04
2582
790
683
-
2582
2040
Hydroxidesalts(ex.NaOH)
1.47
160
2070
320
-
160
331
Silicon
0.71
1800
2300
1414
-
1800
4140
Liquid/GasPhaseChangeMaterials
Nitrogen
1.04
199
809
(liquid)
-
-196
199
161
Oxygen
0.92
213
1140
(liquid)
-
-183
213
243
CurrentImplementation
Phasechangematerials(PCMs)havebeenencapsulatedinspherestoformpackedbedsofencapsulatedPCMs[9].Heat-transferfluidcanbepassedthroughthepacked-bedofspherestochargeordischargeenergyto/fromtheencapsulatedPCMs.Thephasechangeoccursatnearlyisothermalconditions,sothismethodisusefulforapplicationswheretheheatadditionneedstooccurataspecifictemperature.Atlargertemperatureranges,cascadedPCMsystemscanbedesigned,butwithadditionalcomplexityandcost.Todate,encapsulatedPCMsystemshavebeentestedanddemonstratedatsmallscales.Commercialsystemshavenotbeendemonstrated.
Moltensiliconsystemshavebeendevelopedtoexploitthelargeheatofphasechangewhenmelting/solidifyingsilicon(~1800kJ/kg).TheAustraliancompany,1414Degrees,hasdesignedthermalenergystoragesystemsrangingfrom10–200MWh,andtheybeganoperatingaprototypefacilityin2019.Thesystemsmeltsiliconat~1400°Candrecoupthelatentenergyduringsolidificationtopowercombinedcycles.
Ontheoppositeendofthetemperaturescale,HighviewPowerhasdemonstratedcryogenicenergystorageusing“liquidair”atdemonstrationfacilitieswith2.5kWh(300kWpeakpower)and15MWh(5MWpeakpower)ofenergystorage.Thesystemoperatesbyusingelectricitytocoolairfromambienttemperaturesto-195°CusingtheClaudeCycle.Theliquifiedairisstoredatatmosphericpressureinlargevacuum-insulatedtanks.Thevolumeoccupiedbytheliquidairis
~1,000timeslessthanthatofairatambientconditions.Whenelectricityisneeded,theliquidairispumpedathighpressuresthroughaheatexchangerthatexposestheliquidairtoambienttemperatures(orwasteheatfromanindustrialheatsource).Theliquidairvaporizes,causingsuddenexpansion,whichspinsandturbine/generatorforelectricityproduction.Theheat
Chapter12ThermalEnergyStorage
exchangercanconsistofagravelbedthatservesasacoldstoreoflow-temperaturematerialaftergivingupitsenergytovaporizetheliquidair.Thelow-temperaturematerialcanthenbeusedtohelpcooltheairduringthenextrefrigerationcycle.
Challenges
ChallengeswithPCMsincluderelativelyhighcostsandnarrowoperatingtemperatureranges.UsingPCMstoprovideenergytoaheatenginewilltypicallyrequireacascadedsystemwithmultiplePCMswithdifferentmeltingpoints.Theuseofmoltensiliconathightemperaturesprovideschallengeswithmaterialscontainmentandheatloss.Phase-changesystemsmuststillbewellinsulatedtopreventheatlossandsubsequentphasechange.
Opportunities
1414Degreesappearstohavesuccessfullydevelopedaprototypemolten-siliconsystemthatexploitsveryhighlatentheatsoffusion.Othersystemsandmaterialsthatcanexploithighlatentheatsoffusionatlowcostsmayprovidealternativethermalstoragecapabilities.
Thermochemicalstorage
Thermochemicalenergystorage(TCES)isapromisingstoragetechnology,especiallyathightemperatures(>700°C),asitallowsforthestorageofheatthroughchemicalreactions,forexample,thebreaking/reformingofbonds.AconceptualillustrationofTCESisshownin
Figure
7
.
Figure7.SchematicofstepsinvolvedinTCES:charging,storage,anddischarging[18]
Thethermochemicalstoragereaction,initsmostbasicform,canbewrittenas
AB+ΔHrxn↔A+B (2)
Inthisequation,ReactantABisdissociatedintoProductsA+Bviatheapplicationofheat(heatofreactionshownin
Table3
)inanendothermicreaction.Theindividualproductscanbestoredseparatelyforanindefiniteamountoftime.Intimesofthermaldemand,A+Brecombineinanexothermicreaction,releasingheat(thereactionproceedstotheleft).
Chapter12ThermalEnergyStorage
TheTCESprocesscomparedtootherthermalstoragetechnologiesissummarizedin
Table1
.ThepotentialbenefitsofTCESinclude(1)enablingmoreefficienthigh-temperaturepowercycles(sCO2orairBrayton)thatareinaccessibleusingcurrentmoltensalttechnologies,(2)potentialhigher-densityandlong-termstorage,and(3)higherexergy.Inaddition,certainTCESprocesses(e.g.,redox-activeoxides)arealsoamenabletogeneratinghydrogenviawater-splitting.Thehydrogencanthenbeusedon-sitetorunafuelcellforback-upgeneration.ForTCEStobeapracticalstoragetechnology,thematerialsmusthavealargereactionenthalpyandfastreactionkinetics,highthermalconductivity,goodcyclicstabilitywithouttheformationofunwantedphasesorsidereactions.Theyshouldalsoconsistofabundantandeconomicallyinexpensiveelements[19-22].
Implementation
AvarietyofpotentialTCESprocessesexist,thoughnoTCESmaterialhasbeenimplementedonanindustrialscale.TCEScanbeapplicableoverawiderangeoftemperaturesandconditions.Heatsource,thetypeofpowercycle,operatingtemperature,andreceiverconfigurationallinfluencetheselectionofacandidateTCESmaterial.
Table4
liststhemostpromisingTCESreactionsbytype,reactiontemperatures,enthalpies,andgravimetricstorageenergies.Theoperatingtemperaturesandstoragedensitiesarerepresentativevalues,butcandifferdependingonoperatingconditions,suchaspressure,aswellasthemorphologyofthesolidspecies.Thesolidspeciescanbeparticles,monoliths,orsupportedoninertorreactivescaffoldstoavoidsinteringordeactivationofthematerial[23].
Table4.Candidatematerialssystemsforthermochemicalenergystorage
StorageMedium
ReactionEnthalpy(kJ/mol)
TemperatureRange(°C)
GravimetricStorageDensity(kJ/kg)
VolumetricStorageDensity(MJ/m3)
Carbonates
CaCO3(s)+ΔH↔CO2(g)+CaO(s)+CO2(g)
178
850-1273
1764
2491
SrCO3(s)+ΔH↔SrO(s)+CO2(g)
234
900-1200
300-1000
1200-1500
BaCO3(s)+ΔH↔BaO(s)+CO2(g)
273
~1290
Hydroxides
Ca(OH)2(s)+ΔH↔CaO(s)+H2O(g)
104
400600
1406
1640
Mg(OH)2(s)+ΔH↔MgO(s)+H2O(g)
81
350-
1340
1396
Hydrides
MgH2(s)+ΔH↔Mg(s)+H2(g)
75
300-480
2880
2088
Mg2FeH6(s)+ΔH↔2Mg(s)+Fe(s)+H2(g)
74
300-500
2106(theo.),
1921(expt)
5768(theo)2344(expt)
Mg2NiH4(s)+ΔH↔Mg2Ni(s)+2H2(g)
77
300-500
1160
3142
NaMg2H3(s)+ΔH↔NaH(s)+Mg(s)+H2(g)
87
430-585
1721
~1721
NaMgH2F(s)+ΔH↔NaF(s)+Mg(s)+H2(g)
97
510-605
1416
1968
CaH2(s)+ΔH↔Ca(s)+H2(g)
186
1000-1400
3587
7374
Chapter12ThermalEnergyStorage
StorageMedium
ReactionEnthalpy(kJ/mol)
TemperatureRange(°C)
GravimetricStorageDensity(kJ/kg)
VolumetricStorageDensity(MJ/m3)
Ammonia
NH3(g)↔½N2(g)+3/2H2(g)
67
400-700
3924
2682
RedoxActiveOxides*
-
2Co3O4(s)+ΔH↔6CoO(s)+O2(g)
205
900
844
-
2BaO2(s)+ΔH↔6BaO(s)+O2(g)
79
693-780
474
-
6Mn2O3(s)+ΔH↔4Mn3O4(s)+O2(g)
32
1000
204
-
4CuO(s)+ΔH↔2Cu2O(s)+O2(g)
64
1030
-
-
Ca0.95Sr0.05MnO3(s)+ΔH↔Ca0.95Sr0.05MnO2.7(s)+
0.15O2(g)
-
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