14 ASHRAE Journal ashrae.org June 2006 June 2006 ASHRAE Journal 15
Solarcoolinghasastrongpotentialforsignifi cantprimaryenergysavings.
About the Authors
Constantinos A. Balaras, Ph.D., Group Energy
Conservation, Institute for Environmental Research
& Sustainable Development, at the National Obser-
vatory of Athens, Greece; Hans-Martin Henning,
Ph.D., and Edo Wiemken, Thermal Systems and
Buildings, Fraunhofer Institute for Solar Energy
Systems, Freiburg, Germany; Gershon Gross-
man, Dr.Sci., professor of mechanical engineer-
ing, Technion-Israel Institute of Technology, Haifa,
Israel; Erich Podesser, Ph.D., Joanneum Research,
Institute of Energy Research, Graz, Austria; Carlos
A. Infante Ferreira, Ph.D., Delft University of
Technology, Delft, The Netherlands.
S
olar air conditioning is an emerging market with a huge growth
potential. Peak cooling demand in summer is associated with
high availability of solar radiation, which offers an excellent opportunity
to exploit solar energy with heat-driven cooling machines. The main
obstacles for large-scale applications, besides high first cost, are
the lack of practical experience with the design, control, operation,
installation and maintenance of these systems.
* Defined as the ratio of the cooling capacity of the system and the heating power delivered
to the system by the solar collectors—directly or indirectly through the storage vessel.
By Constantinos A. Balaras, Ph.D., Member ASHRAE, Hans-Martin Henning, Ph.D., Edo Wiemken, Gershon
Grossman, Dr.Sci., Erich Podesser, Ph.D., and Carlos A. Infante Ferreira, Ph.D.
Forlowpowercoolingsystems,com-
mercialtechnologiesareavailableona
limitedbasis.However,astrongfocus
existsforresearchonotherapplications
includingphotovoltaic-operatedrefrig-
eration cycles and solar mechanical
refrigeration.
1
ThisarticlereviewsrepresentativeEu-
ropeansolarcoolinginstallationsandpro-
videssomepracticaldesignguidelines.
The main heat-driven cooling tech-
nologiesinclude:
• Closed-cycle systems.Absorption
2
andadsorption
3
cyclesareexamples.
Theyproducechilledwaterthatcan
beusedincombinationwithanyair-
conditioningequipmentsuchasan
air-handlingunit,fan-coilsystems,
chilledceilings,etc.
• Open-cycle systems .Desiccant
systemsareoneexample.
3
Theterm
“open”cycleisusedtoindicatethat
therefrigerantisdiscardedfromthe
systemafterprovidingthecoolingef-
fect,andnewrefrigerantissuppliedin
itsplaceinanopen-endedloop.
Comparing Technologies
Single-anddouble-effectgas-fi redab-
sorptionsystems,primarilymanufactured
intheU.S.,China,Japan,andIndia,are
provenandmarketabletechnologiesthat
maybeadaptedandintegratedinasolar-
assistedinstallation.Typicalcoeffi cientof
performance(COP)*forlargesingle-ef-
fectmachinesare0.7to0.8.Forimproved
Solar Cooling
An Overview of European Applications & Design Guidelines
performance,double-effectabsorptionsystemsare
available,withtypicaloperatingCOPsof1.0to1.2.
Currentresearchisfocusingonthree-andfour-effect
systems, which present an attractive potential for
improvedcoolingperformance,withaCOPof1.7
to2.2.
4
Forsolar-assistedsystems,itisimportantto
selecttheappropriatesolarcollectortypetomeetthe
temperatureneedsofthecoolingmachine.Systems
withhighCOPvaluesneedhigheroperatingtem-
peratures. For example, double-effect cycles need
high-effi ciencyconcentratingcollectors.
Commerciallyavailableabsorptionchillersrange
incapacityfrommedium(40to100kW[11to28
tons])tohigh(300kW[85tons]andup).Anumber
oflarge-scalesolarcoolingsystemsforlargecom-
mercialbuildingandindustrialapplicationshavebeen
successfullydemonstratedanditisnownecessaryto
supportwidemarketintroduction.However,giventhe
increasingcoolingdemandinresidentialandsmall
sizebuildingapplications,agrowingmarketexistsfor
lowcoolingcapacityequipment(i.e.lessthan10kW
[34,000 Btu/h]). Small-scale solar cooling systems
couldbereadywithinadecadeorearlier,ifresearch
anddevelopmentsupportisprovided.
Today, adsorptionchillershaveahighereffi ciency
thanabsorptionchillersatlowdrivingtemperatures(defi nedas
theaveragetemperatureoftheheatingfl uidbetweeninletand
outletoftheheatingsystem).Theadvantageisthattheirinternal
cycledoesnothaveanymovingparts(nopumps,noelectrically
drivenvalves).Also,crystallizationcannotoccur,asinthecaseof
LiBr/H
2
Oabsorptionchillers.However,duetotheirintermittent
operation (periodic cycle), they require more effort in system
designandoperationcontrol.Inaddition,comparedtoabsorption
machines,theyarelarger,heavier,andmoreexpensiveperkW
coolingcapacity.Onlyafewmanufacturersmakethesystems,
limitingequipmentchoices.TheCOPofcommerciallyavailable
systemsis0.55to0.65,dependingonoperatingconditions.
Theuseofsorptionairdehumidifi cation,usingsolidorliquid
desiccants,offersanalternativetoconventionalvaporcompres-
sionequipment.Whencombined,theyleadtohighereffi ciency
byincreasingtheevaporatortemperatureofthecompression
cycle.Mostdesiccantsystemspresentlyuseasoliddesiccant
material like silica gel. Since the solid desiccant cannot be
pumped,thesesystemsusuallyuseadesiccantwheeltoallow
continuousoperation.Theuseofsoliddesiccantsmakessense,
iftheairchangeand/orthedehumidifi cationoftheindoorair
arenecessaryorstrictlyprescribed.Examplesexistinsuper-
markets,museums,andassemblyhallswithhighoccupancy.
Systemsusing liquiddesiccantsarelesswidespread.The
liquiddesiccantsystemessentiallyisanopen-cycleabsorption
system,wherewaterservesastherefrigerant.Ithasvarious
advantagesincluding:
• Fewercomponentssincecondensationoftherefrigerantno
longerusesacondenserbutratherusestheenvironment;
• Thewholesystemoperatesatatmosphericpressure,thus
alleviatingtheneedforpressure-sealedunits;
• The amount of refrigerant (water) evaporated in the re-
generatorisindependentofanevaporator,thusproviding
greaterfl exibility;and
• Moreeffi cientuseoflowheatdrivingtemperatures(down
toabout60°Cto70°C[140°Fto158°F]).
However,thistechnologyhasnotyetarrivedinthemarket,
andfurthersystemoptimizationsarenecessary.Commercially
availablesystemsareexpectedsoon.
Desiccantair-conditioningplantsneedagoodcontrolsystem
withareliablecontrolstrategy,whichcanensureaneconomi-
calyear-roundoperation—airconditioninginsummer,heating
andhumidifi cationinwinter,anddedicatedventilationduring
intermediateseasons,iftherearenoheatingorcoolingloads.
TheCOPofdesiccantsystemsisdefi nedasthechangein
enthalpyoftheprocessair(resultingfromreductionofboth
humidityandtemperature)dividedbytheheatinputinthe
regenerator.TheCOPofadesiccantcoolingsystemstrongly
© 2006 American Society of Heating, Refrigerating and Air-Conditioning Engineers, Inc. (www.ashrae.org). Published in ASHRAE Journal (Vol. 48, June 2006).
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