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Lecture Objectives: Aabsorption cooling cycles
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Absorption cooling cycle
Rich solution of Heat H2O H2O + NH3 Rich solution of H2O H2O + NH3
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Simple absorption system
3V 3L 3LLP
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Simple absorption system
Saturated vapor at p2=p3=p4 3V 6 3 5V mixing 1’ Needed thermal energy Useful cooling energy 3L 4 3LLP 5 2 Saturated liquid at p2=p3=p4 1 5L Saturated liquid at p1=p5=p6=p3_LLP
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Heat transfer with separation into liquid and vapor (Generator)
How to move point 4 to right ? =2V =2V heating m4 Q12 /m1 2L= 2L= =m2 m1 =m2 mixture Separator sub cooled liquid mixture x1 x1 Q12 m3 Q12 m3
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Heat rejection with separation into liquid and vapor (Enrichment NH3 in the vapor mixture)
This is our point cooling 1 4=2V Separator 6=5V Q12 /m1 cooling Q45 /m4 x8 m8 8 7 m1 =m2 5 2 sub cooled liquid mixture isotherm m3 2L Q12 x1 x8
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Simple absorption system
Generator with of Enrichment NH3 Different 8V 9 8L 10 8LLP 11
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Absorption system with
Saturated vapor at p2=p3=p4 3V 8V 3 mixing 11 8L 1’ Useful cooling energy 8LLP 10 3L 2 9 Saturated liquid at p2=p3=p4 1 Saturated liquid at p1=p5=p6=p3_LLP
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More detailed absorption cooling
Refrigeration and air conditioning (Ramesh et al)
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Carnot Cycle COPvapor_compression=Qcooling/Pelectric COPmax=Tcooling/(Tenviromnet-Tcooling) COPabsorption=Qcooling/Qheating COPmax= Tcooling/Theat_source ∙ (Theat_source-T environment)/(Tenviromnet-Tcooling)
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