Page 39 - Low Temperature Energy Systems with Applications of Renewable Energy
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Principles and operation of refrigeration and heat pump systems    27

                 _
                            _
               DE CN ¼ _ me 3   E Q CN   _ me 4 ¼ 1:8024  ð125:12   84:62Þ  61:88
                                        ¼ 11:12 kW

              Notice that the middle term in this equation is numerically negative because Eq.
           (1.20) assumed that the condenser-heat exergy flowed out.

              At the same time, the heat that is received by the reservoir at 80 C brings an
                          _
           amount of exergy E Q hs where
                                         298:15
                _          T 0  _
               E Q hs ¼ 1     Q CN  ¼ 1           350 ¼ 54:51 kW
                           T hs          353:15
              Thus, the exergy destroyed at the condenser caused by heat transfer from the cycle
           working fluid to the heated space across a large and variable temperature difference
           amounts to 7.37 kW, i.e., about 12% of the exergy of the condensing heat released,
           or about 2.1% of the total heat transfer. The efficiency of the exergy transfer is there-
           fore about 88%.
              Throttle: Since there is no work or heat transfer at the throttle, the exergy decrease
           for the working fluid is the only factor. Thus,

                 _
               DE TH ¼ _ me 4   _ me 1 ¼ 1:8024  ð84:62   59:96Þ¼ 44:45 kW
              This seems quite large but it is the throttling process that creates the low tempera-
           ture that makes the heat transfer from the surroundings possible.
              Evaporator: Here heat is removed from an ambient-temperature space and delivered
           to the R152a which is maintained at a lower temperature. The method used for the
           condenser may be applied to the evaporator with the following results:

                 _          _
               DE EV ¼ _ me 1 þ E Q EV   _ me 2

                _           T 0  _        298:15
               E Q EV ¼ 1       Q EV  ¼ 1          1:8024  ð520:09   403:59Þ
                           T EV           293:15
                                    ¼ 3:581 kW

              This negative result may seem surprising, given that heat is transferred from the sur-
           roundings to the R152a. The term is negative because T 0 > T EV , meaning that the flow
           of exergy is actually from the R152a to the surroundings. And since any exergy dis-
           charged into the dead state is lost, this term constitutes part of the exergy destroyed
           in the evaporator. Therefore, we find

                 _
                            _
               DE EV ¼ _ me 1 þ E Q EV   _ me 2 ¼ 1:8024  ð59:96   57:98Þþ 3:581
                                       ¼ 7:150 kW
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