Plus-ICE TM PHASE CHANGE MATERIALS (PCM) THERMAL

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Plus-ICETMPHASE CHANGE MATERIALS(PCM)THERMAL ENERGY STORAGE(TES)DESIGN GUIDEVersion: 2011Phase Change Material Products Ltd.Unit 32, Mere View Industrial Estate,Yaxley, Cambridgeshire, PE7 3HS, UKTel: 44-(0)-1733 245511Fax: 44-(0)-1733 243344e-mail: info@pcmproducts.netwww.pcmproducts.net

TABLE OF CONTENTPlus-ICE TMSTAINLESS STELL BALLTHERMAL ENERGY STORAGEDESIGN GUIDE10INTRODUCTION1.1 1.2 1.31.4-2.0CURRENT THERMAL ENERGY STORAGE TECHNOLOGIES2.1 2.2 2.3 2.4 -3 .03.5-GeneralEutectic (PCM) BackgroundPlus-ICE Phase Change SolutionsPlusICE TES Concept3.4.1- TubeICE Concept3.4.2- BallICE Design3.4.3- FlatICE Concept3.4.4- Storage Tanks Options3.4.5- Atmospheric Storage TankTank Installation & OperationPlus-ICE THERMAL ENERGY STORAGE APPLICATION4.1 4.2 4.3 4.4 4.5 4.6 -5.0Water Storage SystemsIce Storage SystemsSpecial ApplicationsEutectic (PCM) Energy Storage SystemsPlus- ICE THERMAL ENERGY STORAGE TECHNOLOGY3.1 3.23.3 3.4 -4.0Thermal Energy StorageElectricity Supply & Cooling Load RelationshipTES AdvantagesDesign CriteriaNew ConstructionRetrofit ApplicationRefrigeration SystemsFree Cooling ApplicationsHeat Rejection TES ApplicationsOther ApplicationsCONTROLS5.1-Monitoring & Control

PlusICE THERMAL ENERGY STORAGE DESIGN GUIDE1.0- INTRODUCTION1.1. THERMAL ENERGY STORAGE:Typical cooling load profile in Figure: 1.1.1 can be considered as the universal load patternfor any given cooling application. This pattern depends on the location/position, occupationalpattern and specific internal gains but in principle Thermal Energy Storage (TES) System looksinto total cooling load area i.e. kWh (Ton-hr) demand over a certain time span rather than peakload which is the main criteria for conventional design load.Thermal Energy Storage (TES) is the temporary storage of high or low temperature energy forlater use. It bridges the time gap between energy requirement and energy use. Most TESapplications involve a 24 hour storage cycle and a typical TES load shifting strategy can be seenin Figure: 1.1.2. While the output of the TES is always thermal energy, the input energy may bethermal or electrical.COOL ING LOAD AREA(kW h)1 00T HE RMAL ST ORAGE ARE A(k Wh)10090REFR IG ERA TION8070LOAD% CAPACITYCAPACITY (%)806050SHIFTING60403020HVA C4010CHILLER THERMAL ILDS12021222324ICEBUILD0123456789 10 11 M 13 14 15 16 17 18 19 20 21 22 23 MTIM EFigure 1.1.2: TES Load Shifting StrategyFigure 1.1.1.: Typical Building Load Profile1.2 - ELECTRICITY SUPPLY / COOLING LOAD RELATIONSHIP;Primary energy source such as Hydro, Gas, Coal and Nuclear fuels can be transformed directlyinto Electricity as a power source for industrial and household appliances. In principle, electricitygeneration has to be balanced with the exact time of the consumption to satisfy the fluctuatingdemand at the lowest possible cost.4540COAL & OIL35GENERAT ING CAPACIT Y (GW )However, this phenomena its own createsproblems,ononehand,constantlyfluctuating seasonal and specific timedemands which are outside their control andon the other hand, the essential specificrunning time requirement of electricitygeneration plants which do not necessarilymatch the demand.Utility companies aim to generate electricityusing different types of primary energysources to offset peak demands and a typicalUK electricity generation pattern can be seenin Figure :1.1.1.3025LAR GE C OAL20IMP OR T15C LOSE D COMB IN ED GAS T UR BI N E10N UC LEA R5001234567891 0111213141 5161718192021222324T IM EFigure 1.2.1: Typical UK DailyElectricityGeneration ProfileThe Cooling Load in Figure :1.1.1 and the Electricity Generation in Figure: 1.2.1 generally fallsinto the mid-day or early evening periods. Almost every modern society has a mid-day or lateevening peak electricity demand.PCMPIMAN.V-1PCM Limited1

PlusICE THERMAL ENERGY STORAGE DESIGN GUIDEThis essential demand force utility companies to build new additional peak demand powerstations which require considerable investment and they are in operation only during peakdemand periods and shut down the rest of the time. They use expensive primary energy sourcesand are subject to the standard cost of maintenance, consequently production cost per kWh is 3-4times higher than the standard base load electricity production cost. The average level of the UKelectricity cost details can be seen in Figure: 1.2 and this additional cost is reflected directly tothe end user by means of "Demand Charges".4ELEC TR IC ITY C OST ( p / kWh )3. 532. 521. 510. re 1.2.2 - A typical UK Daily Electricity Pool PricesConsidering the significant load on modern office building air conditioning and industrial /processes refrigeration impact on their overall electricity supply network, the utility companiesdiverted their attention towards reducing this short peak demand in addition to their costlyexercise of building new power stations.Utility companies in the majority of the developed world have already reached their peak andshifting the short time peak electricity demand became an essential part of their distributionstrategies. Consequently, utility companies developed various incentive schemes to support anyenergy saving and load shifting applications by means of subsidising the initial investment costand offering off peak rates.1.3 - TES ADVANTAGES:1.3.1- Cheap Electricity Rates:In principle, TES utilises excess electricity energy from the national grid during off-peak periodsto shave the demand during the peak period. Consequently, utility companies normally offerincentives by means of reducing off-peak time electricity cost for such schemes. However, the ratestructure and peak demand periods widely depend on the country and even different regionswithin the country.In England, the off-peak period is between 12.00 PM and 7.00 AM at an average rate of average2.68 p/kWh against the standard charge of 7.35 p/kWh. In the USA, due to the large airconditioning load this structure has been generally divided into Winter and Summer charges butstill offers similar incentives for lower demand charges 2.75 cent/kWh for winter, 3.40 cent/kWh forSummer against 5.45 cent/kWh for winter and 6.75 cent/kWh for summer standard chargesrespectively.It can be clearly seen that off-peak cooling running costs are almost half of those of aconventional system without taking into account the additional demand charges which tips thebalance further towards the TES systems.PCM Design Guide 2011-2PCM Products2

PlusICE THERMAL ENERGY STORAGE DESIGN GUIDE1.3.2 - Low er Ambient Operation:765Compressor CO PIn many countries the variationsbetween day and night timeambient temperatures reachesup to 10-15 Deg C andconsequently any type of heatrejection equipment operatesmore efficiently.HH VV A CC43T EE S // H VV A CCODCHH II LL LLEEDD FFOOOD2The head pressure (CondensingPressure)changesproportionally with the ambienttemperature and the lower theambient temperature, the lowerthe condensing pressure whichcan be achieved in any type ofmechanical refrigeration.FR O ZE N F OO D150454035302520C o n dd e n ssiinn gg TT e m p eerr a t u r e ( C )Notes;1) HVAC Chiller Evaporation at 3 oC, R134a Refrigerant2) TES/HVAC Chiller Evaporation at -13 oC, R134a Refrigerant3) Chilled Food Evaporation at -13 oC, R404a Refrigerant4) Frozen Food Evaporation at -35 oC, R404a RefrigerantFigure 1.3.2.1 Ambient Effect on SupermarketRefrigeration Machinery EfficiencyA typical example of a cooling system operating data Vs condensing temperature can be seen inFigure : 1.3.2.1. In a climate where the night ambient temperature drops below the thermalstorage temperature, the storage system can be charged by means of FREE COOLING fromexisting heat rejection equipment such as Condensers and Cooling Towers.This technique is particularly suitable for sensible chilled water and PCMs (Eutectic) thermalstorage systems. Typical annual weather data and daily ambient profile for London, Englandcan be seen in Figure :1.3.2.2 and Figure 1.3.2.3 respectively.Free Cooling schemes become extremely beneficial for many buildings that have winter daycooling loads such as large computerised offices, banks, dealer rooms, sport halls, hospitals,theatres etc., food processing such as dairy, brewery and industrial process applications,A Free Cooling strategy provides cooling with little or no chiller operation and as a result givessignificant energy savings. Free Cooling can be applied to both the chilled water and heatrejection side of the system and offers unmatched overall system performance.H O U R L Y D R Y A N D W E T B U LB T E M PE R A T U R ESF O R J U LY IN L O N D O N , T H E U N IT E D KIN G DO M30282622AMBIENT TEMPERATURE ( C)24Temp era ture (Deg C)2220181614121086420J ANFE BM ARA PRMA YLO ND O N ( U K ) ,A V ER A G E WE A T H E R D A T A ,( K ew 1 941 - 70)J UNEJ UL YA UGSEPO CTNO VD ry B ul b18W E T - BU LB16141210D ECW et B u l bD R Y- BU L B20MD esi gnFigure 1.3.2.2 Annual MeanTemperature123456789 10 11 M123456789 1 0 11 MT IM EFigure 1.3.2.3 - A typical UK Daily Summer AmbientProfile1.3.3 - Smaller Chiller / Running at full load:Chillers for thermal storage applications are generally in the region of 30-60% smaller than theconventional system chillers due to the longer running periods and large latent heat storagecapacity to satisfy the maximum demand. Consequently, chiller(s) run most of their expected lifespan running at full load during the charging mode and if it is required to supplement theoperation for partial storage strategy.PCM Design Guide 2011-2PCM Products3

PlusICE THERMAL ENERGY STORAGE DESIGN GUIDE1.3.4 - Future / Expansion additional capacity:Any future or additional cooling/heating demand can be easily satisfied by means of changingthe thermal storage strategy for the system.In principle, the additional capacity can beprovided by shifting from a full storage to a partial storage or even weekly storage systemdepending on the required additional capacity over the existing capacity limits.1.3.5 - Large Short Term Load:TES becomes essential for short period large energy requirements. Prime examples arechurches, sport halls, theatres etc. for space conditioning and food processing, dairy, brewery,processing and gas turbine air inlet gas cooling for industrial applications.The time span for the duration of peak demand is usually in the region of a couple of hours aday. Nevertheless, the conventional system has to be designed to satisfy the maximum demandwhich is not required most of the time. If the cooling load can be spread by means of TES, thecooling apparatus can be reduced dramatically.1.3.6- Full Stand-by Capacity:The stored thermal energy can easily provide reasonable safety periods for any regular and/oremergency repair works to be carried out without disturbing the system. Full Stand-by capacitybecomes quite essential for industrial and continuous space conditioning applications.1.3.7 - Env ironmentally Friendly Option:Surprisingly, an integrated TES design approach does not only provide an economical initialinstallation but also offers considerable environmental benefits by means of reducing both thedirect global warming impact via reduction in refrigeration machinery hence reduced refrigerantcharge and the reduction in the indirect global warming impact attributed to the CO2 emissionrelated to electricity generation.0 .7W IN T E R ( 2 9 N O V 19 9 3)0 .60 .50 .4S U M M E R ( 1 A U G 19 9 3)0 .30 .20 .124232221201918171615141312119108765432100kg CO2 / kWhIf one can shift the peakrefrigerationdemand bymeans of Thermal EnergyStorage to off-peak periods,the system will not only berunning more economicallyby means of lower energycosts and reduction inmaximum demand chargesbut also the refrigerationsystems will be relying onless CO2 emission basedpower generation plants andeffectively less overall CO2emission for the system as awhole, Figure 1.3.7.1.T IMEFigure 1.3.7.1 : England & WalesElectricity Generation Daily CO2 Emission ProfileFurthermore, the lower ambient temperatures as illustrated in Figure 1.3.2.2 and 1.3.2.3 result inlower energy consumption due to a lower condensing temperature operation as well as thepossibility of utilising smaller refrigeration machinery. Consequently, the systems direct andindirect global warming impact as part of the TEWI calculation can be reduced for any givensystem with additional financial benefits.PCM Design Guide 2011-2PCM Products4

PlusICE THERMAL ENERGY STORAGE DESIGN GUIDE1.4 - DESIGN CRITERIA:In principle, all TES systems have the same fundamental concepts, and consist of the followingsimilar fundamental equipment.1) The cooling machine provides cooling or alternatively heating source capacitieswhich may directly match the load or to be added to storage.2) A storage system which may either accept excess cooling/heating capacity from thecooling/heating source or supply to a required type of load.3) A load which can accept cooling/heating from either cooling/heating equipment orstorage system separately or combined kWhBtuTon-HourENERGY 284Btu/hr0.2931Ton-hr3.5212,0008.3 x 10-51The following Cardinal rule applies whatever the type of system or components used to achievedto satisfy the demand."THE CAPACITY OF THE COOLING/HEATING SOURCE OVER THE DESIGN TIME MUSTBE EQUAL TO THE SYSTEM LOADS PLUS SYSTEM LOSSES OVER FULL EMHEATING/COOLINGHEATING/COOLINGLOADSLOADSFor a daily cycle the 24 hours capacity of the cooling/heating source must be equal to the systemload plus losses over a 24 hour period and the same fundamental concept can be applied forweekly or seasonal storage systems.In principle, " THE PERFORMANCE OF ANY TYPE OF TES SYSTEM WILL BE A FUNCTION OFLOAD, WATER FLOW RATES, WATER CIRCULATION TEMPERATURES AND AMBIENTTEMPERATURES".PCM Design Guide 2011-2PCM Products5

PlusICE THERMAL ENERGY STORAGE DESIGN GUIDE1.4.1 - Storage Techniques:Designers all over the world have developed over the years different techniques and manyunique applications but the main design criteria remains the same as "FULL” or “PARTIALSTORAGE".FULL STORAGE systems shift the total cooling/heating load to the off-peak period and thecooling/heating source is never used during the peak period in order to achieve the maximumeconomy, this type of system results in a smaller cooling/heating source but a larger storagevolume.PARTIAL STORAGE system utilises the cooling/heating source during the peak periods in orderto reduce the initial storage capacity. This type of system is widely used to limit the demandduring the peak period and this technique is calledDEMAND LIMITING which is a type of Partial Storage system whereby the excess capacity issupplemented by a TES source in order to stay below the maximum electrical demand limit.Any of the above techniques can be used either over a daily cycle (DAILY PARTIAL / FULLSTORAGE) or longer period of weekly or seasonal (WEEKLY PARTIAL / FULL STORAGE).In principle, FULL STORAGE provides the most economical running cost with a penalty of largerinitial investment cost and volume (space) requirement and PARTIAL STORAGE cost isrelatively cheaper in comparison with full storage but the running cost may be higher.Both of the above techniques can be applied for either an existing system or new installation.The practical applications show that if a TES system is applied carefully in full consultation withthe utility companies, the existing system modification cost can be recovered in a very shortdepending on the application and a new installation can be provided within the same budgetlimits as conventional systems.2.0 - CURRENT THERMAL ENERGY STORAGE TECHNOLOGIES;Thermal Energy Storage (TES) in simple terms can be explained as " Storing High or LowTemperature energy for later use in order to bridge the time gap betw een energy av ailabilityand energy use ".Water and Phase Change Materials (PCM's) constitute the principle storage media for HVAC andRefrigeration purposes but Coil, Rock and Solid Materials are also used as storage media.2.1 WATER STORAGE:Water has the advantages of universal availability, low cost and transport ability over othersystems and in principle the simplest thermal energy storage is a water tank which can store hotor cold water during the off-peak periods and be withdrawn during the peak periods.There are many application techniques of water storage but the main criteria can be describedas " mixing the return w ater w ith the stored v olume in such a w ay to prov ide uniform supplytemperature to the system". The following techniques have been successfully appliedcommercially throughout the world.- Labyrinth Method:This system was developed by Japanese Engineers and has been successfully applied incommercial buildings since 1950. Water flows back and forth through high and low apertures inadjacent cubicles in order to minimise the temperature swing for the supply water.- Temperature Stratification:The return water from the system can float normally above the stored chilled water and the sameprinciple is applicable for a 45 ºC ( 113 ºF) water supply which can successfully float above 39ºC ( 102 ºF) return water, since the density difference is much larger.PCM Design Guide 2011-2PCM Products6

PlusICE THERMAL ENERGY STORAGE DESIGN GUIDE- Flexible Diaphragms:The natural temperature stratification can be replaced by a sheet of coated fabric diaphragmwhich is anchored securely at the mid point of the tank, this floats up and down depending onthe water supply and return volumes and as a result the diaphragm dramatically improvesstorage and constant supply temperature accuracy.- Empty Tank Concept:The Empty Tank concept can be described as the installation of as many tank sections which canbe used to pump chilled water back and forth between the numbers of compartments. Thistechnique provides an excellent separation of temperature for HVAC applications.2.2 - ICE STORAGE SYSTEMS;Ice production techniques can be divided into two main groups namely “Dynamic” and “Static”systems. and the produced ice can be used either directly or indirectly to chill the product orsystem.The direct usage generally remains within the food sector to chill products such as fish,vegetables, meat, poultry etc. and indirect usage generally utilised for the latent heat coolingeffect for process cooling such as ice storage, TES systems for air conditioning and processcooling as secondary cooling medium.2.2.1 - Static Ice Production SystemsThis technique is probably the oldest in use. In principle, the ice formation and melting takesplace without any physical removal of the ice . The most common used techniques are asfollows:-Ice on CoilRefrigerant or Glycol water solutionat a temperature of between -4 Cand -10 C is circulated within aserpentine coil, which is submergedin an insulated tank of water in orderto form ice on it. The ice buildertank consist of a low pressure airpump or paddle blade to agitate thesystem in order to achieve evendistribution of ice melting andformation. The thickness of ice ismeasured by a sensor to control theoperation and the relevant detailscan be seen in Figure : 2.2.2.RefrigerationSystemCoolingSystemIce BuilderAirPumpFigure 2.2.1 : Ice Builder ConceptIce Banks:The ice bank consists of a pressurised, closelypacked polyethylene tube heat exchanger.Low temperature glycol solution is circulatedthrough the tubes, which freezes the wateraround them. The water in the insulated tankis almost frozen solid at the end of thecharging cycle. The control of the system canbe provided by the ice level sensor in thetank. The system water is circulated throughthe tank for both techniques, to satisfy thecooling demand Figure : 2.2.2.CHILLE RCHILLERICE BANKSHVAC SYSTEMFigure 2.2.2 : Ice Bank Systems Encapsulated Ice StorageThe charging and discharging cycle can be controlled by water levels in an inventory tank whichis subject to level change due to ice expansion and contraction during the freezing and meltingprocess respectively or by process fluid temperatures.PCM Design Guide 2011-2PCM Products7

PlusICE THERMAL ENERGY STORAGE DESIGN GUIDE2.2.2 - Dynamic Ice Production SystemsIce is periodically harvested from the freezing apparatus to a storage bin and the stored energy isrecovered by circulation of water through ice in the bin to supply the chilled water system duringnormal operation. There are many commercially available systems in the market and the mostcommon used systems are as follows:Ice Harv ester:Ice is built on a vertical surface which is theevaporator section of the refrigeration RefrigerationSystemsystem. Water is circulated from the storageCoolingtank, over the plates until a certainSystem123thickness, normally in the region of 8-10ICE HARVESTERmm ice is formed. This freezing processSECTIONStakes approximately 20 minutes .The ice isharvested by means of hot-gas by-pass fromthe delivery port to the evaporator plates toIce Build Areawarm the surface to about 5 ºC, resultingICE STORAGE TANKin the ice in contact with the plates meltingand falling into a sump or ice tank, to whichFigure 2.2.4 : Ice Harvesterchilled water from the system is circulated.Tubular Ice:In principle this technique is identical to the Ice Harvester system, the only difference being thatthe ice is produced within a tube rather than on the surface of plates. The storage and systemapplications are identical to the ice harvester techniques.Ice Flakes:A revolving freezing apparatus produces ice flakes continuously and theflake ice is collected at the bottom drum of the machine for later use by means of circulatingchilled water through the ice tank to satisfy the cooling demand.Slurry Ice:In this system a binary solution is cooled below its freezing temperature within a Falling Film,scraper, vacuum or supercooling heat exchangers as illustrated in Figure 2.2.5. The refrigerantwhich is circulated outside the tube supercools the binary solution into millions of fine crystalswhich are then pumped into a storage tank for later use, or directly to satisfy the process load.During the cooling mode, warm solution is circulated through the storage tank where it is cooledby the crystallised solution and then pumped directly to satisfy the air conditioning chilled watercircuit.SSLURRYLURRY ICEICE MACHINEMACH INE TTYPESYPESRefriggeerrantRefriantOutRefri gerge raantntOutSoll uti onSoInInSo lutioSoluti o nInSl ururryryOutRefrRe fr ig era ntntInIn1)1) S UPER COOLI NG TECHNTEC HNIIQUQU E2)CHN2) S CR APER TETECHN IQUEIQU ESoSollutiuti ononInRef rigerantRefrigerantInRefriiggeeraRefrra ntOutSlurr yOutSo lutioluti onnInSl ururryryOut3) V AC UU MTECHN IQUETECHNIQU ERefri geg erara ntInSlurr geerraantRefrintInIn4) FAFALLILLI NG FIFILMLM TTEECHNCHNIIQUQUEE5 ) EJ5)EJECECTORTOR TTEECHNCHNIIQUQUEEFigure 2.2.5. Slurry Ice Generator TypesPCM Design Guide 2011-2PCM Products8

PlusICE THERMAL ENERGY STORAGE DESIGN GUIDE2.3. - SPECIAL APPLICATIONS:-Seasonal Storage:This type of system aims to utilise seasonal temperature variations over prolonged periods forlater use. Most research has been linked to storing heat from a Solar Source for heating andIce/Snow storage for air conditioning purposes but waste incineration, nuclear cooling water,industrial reject heat have been also used for seasonal thermal storage.An excavated pit system in Illinois State University and a container ice system in Kansas StateUniversity have been successfully applied for cool storage. Seasonal energy can be also stored inthe form of sensible heat storage and the most common applications are the lake storage, tanks,excavated pits for either cooling or heating purposes.Canada and Sweden are the leading countries for such systems. Solar ponds are widely used inIsrael, Switzerland and England for hot water storage and some applications utilise an artificiallake which is constructed in front of the building specifically for TES for chilled water system ofthe air conditioning.-Ground Couple Storage:The earth is used as a storage medium which provides the heat source for use usually for spaceconditioning. In practice, two types of ground couple storage, namely direct heating/cooling andheat pump systems have been applied.The direct system stores available heat and/or coolness in a buried media i.e. vessel or localisedvolume of ground and the stored energy can be recovered when required satisfying the demand.On the other hand, the heat pump system removes heat from or rejects heat to the groundstorage media for space conditioning.- Packed Rock Beds:A variety of solids namely rocks can be used to store thermal energy for later use. A packed rockbed which may also be called a pebble bed or rock pile storage utilises the available thermalenergy by means of circulating through a packed rock bed to add heat to or remove heat fromthe system for charging and discharging respectively. The energy can be transferred from a fluidbut the most common systems utilise air due to the high heat transfer coefficient between air androck.- Low Temperature CO2 Storage System:Carbon Dioxide offers the most compact latent heat storage system due to the commerciallyobtainable triple point which allows the utilisation of a single substance as static latent heat offusion storage and in the mean time the liquid overfeed continues the discharging operation andvapour compression technology to charge the system.Carbon Dioxide can be stored at it's triple point of -57 ºC (-70 ºF) and 518 kPa with solid fractionof 70-80 % by mass and the system can provide 140 kJ/Kg thermal storage capacity within therequired volume of 166.6 MJ/m 3.- Cogeneration:Cogeneration offers the facility to utilise the waste heat from the engine which is the drivingforce for the generators or alternatively to enable to use those system over a 24 hour periodwhich increases their economic viability. In practice, there are two types of cogenaration systemswhich have been successfully applied in industry.The first type of system utilises the waste heat from the engine to drive an absorption chiller forcooling or direct heat storage facility.PCM Design Guide 2011-2PCM Products9

PlusICE THERMAL ENERGY STORAGE DESIGN GUIDEThe second type of system utilises the excess electric energy to drive an electrically driven chillerand/or heat pump to charge any type of thermal storage or direct cooling/heating requirement.Asuccessful district heating with cogenaration system has been applied in Des Moines, Iowa, USAwhere many large buildings utilise their stand-by generators as cogeneration plants to driveeither an Absorption chiller/s or electrically driven chiller/s along side their standard airconditioning chillers during the peak demand period.In other words, they produce their own electricity during the peak demand period or even insome cases, sell the excess power back to the utility grid. If it is carefully designed, thecogeneration system offers the most economical return for the investment.-Thermochemical Energy Storage:Recent research shows that various alcohols and ketones are potential thermochemical storagemedia but due to the relative cost and complexity, no commercially viable systems have yetemerged.Typical examples are the mixture of Sulphuric Acid and water, and alternatively SodiumHydroxide and water, Systems in which the water is separated by the heat input to the mixtureand as soon as the two substances are mixed, the chemical reaction of the substances liberatesheat.2.4 - EUTECTIC (PHASE CHANGE MATERIAL) ENERGY STORAGE:A substance can exist in the solid, liquid or gaseous states depending on the temperature andpressure of the storage conditions. The three phases may exist together in equilibrium but twophase states are commonly used in practice. The latent change of certain substances can beused to store heating or cooling for later use.The substances used for latent heat storage are called " Phase Change Materials (PCMs)" whichprovide the advantages of smaller size, constant temperature during phase change, lower standby losses over sensible energy storage materials.The most commonly used form of Phase Change is the heat of fusion between solid and liquidphases, although solid/solid and liquid/gas phase changes can also be used.- Phase Change Materials (PCMs) & Eutectics:The basic and most commonly used form of PCMs is the water/ice phase change at 0 C ( 32 ºF)Salt Hydrates, Organics and Clathrates are also widely used in industry.Salt Hydrates are compounds of salt and water and have the advantage of high latent heat offusion due to their high water content but the salts also create major disadvantages of life cyclein the form of phase segregation during the charging and discharging mode which results inheavier salt settling at the bottom of the solution and consequently, the TES capacity of thesolution changes. The process is progressive and irreversible.Eutectics on the other hand are mixtures of two or more substances mixed in such a way as toprovide the desired melting/freezing point. The mixture melts completely at the designtemperature and has the overall composition in both liquid and solid phases which has the maincriteria of a PCM.Organics have low density and poor thermal conductivity. They are relatively expensive andcombustible. The prime example is paraffin wax.Clathrates (Gas Hydrates) are a mixture of chemical substances in which one chemical substanceis bound inside another in a cage-like fashion. In practice, water forms the bonding structure forthe clathrates for thermal energy storage applications. The most commonly used clathrates areR-11, R-12 and R-22 refrigerants.PCM Design Guide 2011-2

PCM Design Guide2011-2 PCM Products 3 1.3.2 - Lower Ambient Operation: In many countriesthe variations between day and night time ambient temperatures reaches up to 10-15 Deg C and consequently any type of heat rejection equipment operates more efficiently. The head pressure (Con

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