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Heating with geothermal systems                                   219

              Loss of exergy in the economizer EC is:


               E _ EC  ¼ T env ½ _ m EV ðs 9   s 6 Þþð _ m C   _ m EV Þðs 8   s 7 ފ  (5.30)
                Dk
           where ð _ m C   _ m EV Þ is the R123 mass flow rate through the economizer.
              Exergy loss in a throttle valve at the low-pressure side is:


               E _ TV1  ¼ _ m EV T env ðs 10   s 9 Þ                      (5.31)
                Dk
              For the throttle valve at the high-pressure side, the loss of exergy is determined by:

               E _ TV2  ¼ð _ m C   _ m EV Þ T env ðs 7   s 6 Þ            (5.32)
                Dk
              The overall exergy efficiency for the system is:

                            s
                       Q _ HPU cond
                ex                                                        (5.33)
               h ¼ P    _      _
                       W comp þ Q s 0
                                0
           5.7   Summary


           Geothermal energy, either alone or in conjunction with heat pumps, is providing heat-
           ing for residents and businesses in cities all over the world. Historical accounts of very
           old systems in Europe and in the United States show that these systems have a long
           life, give reliable service, and are environmentally friendly as well as economic.
           Greenhouses warmed by geothermal fluids allow year-round crop growing even in se-
           vere climates. A wide variety of fish and other water creatures such as alligators are
           raised in geothermally-heated ponds. The outflow from geothermal electric power
           plants can be used as the heating medium. Such facilities are good businesses and
           can often be promoted as tourist attractions. The use of heat pumps with geothermal
           energy offers a multiplier effect to achieve high performance even under cold ambient
           temperatures.

           Nomenclature


           E _   exergy loss
           C     specific heat capacity
           k     isentropic index
            _ m  mass flow
           p     pressure
           q     specific heat transfer
           q*    specific cooling capacity
           Q _   heat
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