Page 183 - Low Temperature Energy Systems with Applications of Renewable Energy
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¼  3735  3826  q alloted  3736  3765  þ q 0  q g  ¼  þ q r:c:  þ q c  q a  ¼  Q 0  0.85  0.87  ¼  q 0  2170  a)  2305  a)  m$q g ;  ¼  1835  b)  1705  b)  m$q a ;  ¼  94.5  c)  43.5  c)  m$q c ;  ¼  985  d)  1044  d) m$q cond ;  ¼  354  e)  526  e)  m$q r ;  ¼  2.17  2.3  Q g /Q 0  0.463  0.43  Q 0 /Q g  ¼  q 0 ðs q Þ 0 0.373  0.
             q letdown  q letdown  q alloted  m NH 3  Q g  a)  Q a  b)  Q c  c)  Q cond  d)  Q r  e)  ¼  q sp  E cooling  ¼  h ex  ðs q Þ 0  ðs q Þ s










                      kg/s
                      rate,
                      flow

             kJ/kg    mass
             plant,                           plant

             of       (ammonia)  kW:    consumption  the
             balance  fluid  loads,  condenser  condenser  heat  coefficient  of  COP


             Thermal  Working  Thermal  generator  a)  absorber  b)  cooler  c)  d)  reflux  e)  Specific  Cooling  Exergy
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