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5.4 EXAMPLES      113





                  Hence the isentropic turbine work is

                                  ¼ c p T 3   T 4s ¼ 1:0045   1200   509:9 ¼ 693:2kJ kg:
                             w T isen
                  The net work from the cycle is w net ¼ w T þ w C ¼ 693.2 þ ( 407.9) ¼ 285.3 kJ/kg and the
                                     w net  285:3
               thermal efficiency is h ¼  ¼       ¼ 0:575:
                                  th
                                      q 2s3  496:1
                  This value is equal to the standard expression for the efficiency of a Joule cycle, defined as
                         1
               h ¼ 1     k 1 , see Chapter 3.
                th
                          k
                        r p
                  The maximum net work output is defined by
                                                  b w net ¼ b 3   b 2 :
                  Now, the values of exergy are defined, for a perfect gas as

                                                                                T   k   1  p
                b ¼ðh   T 0 sÞ ðh 0   T 0 s 0 Þ¼ðh   h 0 Þ  T 0 ðs   s 0 Þ¼ c p ðT   T 0 Þ  T 0 ln     ln  :
                                                                                T 0   k    p 0
                  Thus, along an isobar,

                                                                 T
                                            b ¼ c p ðT   T 0 Þ  T 0 ln  :
                                                                T 0
                  Since both 2s and 3 are at the same pressure

                                             T 3                 T 2                      T 3
                  b 3   b 2s ¼ c p ðT 3   T 0 Þ  T 0 ln    ðT 2   T 0 Þ  T 0 ln  ¼ c p ðT 3   T 2 Þ  T 0 ln
                                             T 0                 T 0                      T 2
                  Thus

                                                                1200

                             b w net ¼ 1:0045   ð1200   706:1Þ  300 ln  ¼ 336:3kJ=kg:
                                                                706:1
                  The rational efficiency of the cycle based on these dead state conditions is
                                                 w net  285:3
                                            h ¼      ¼      ¼ 0:848:
                                             R
                                                  b w net  336:3
                  This means that the ideal Joule cycle is only capable of extracting 84.8% of the maximum
               net work from the working fluid, whereas under similar conditions (with the dead-state
               temperature defined as the minimum cycle temperature) the Rankine cycle had a rational effi-
               ciency of 100%. The reason for this is that the energy rejected by the Joule cycle, from 4s to 1, still
               has the potential to do work. The maximum net work obtainable from the rejected energy is
               b 4s – b 1 .Thisisequal to

                                                                  T 4s
                          ½ b w net Š rejected  ¼ b 4s   b 1 ¼ c p ðT 4s   T 1 Þ  T 0 ln
                                                                  T 1

                                                                   509:9
                                    ¼ 1:0045   ð509:9   300Þ  300 ln     ¼ 50:99 kJ=kg:
                                                                   300
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