Page 114 - Entrophy Analysis in Thermal Engineering Systems
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Irreversible engines—Open cycles                             107


                               1
                                        f    p
                                    a           ¼ HHV n v L w            (8.11)
                                   0
                                        0
                                  H + H  H   0              0
                               _ n f
              Eq. (8.11) expresses the first right-hand-side term from Eq. (8.6) as a simple
              function of HHV and the enthalpy of water evaporation. Next, the second
              right-hand-side term from Eq. (8.6) is determined as follows.

               1                h                                           i p
                   p       f                             y   z
                       a                       + Λ x  +
                   0
                       0
                                                         4   2               0
                  S  S  S  0  ¼ xs CO 2  + n v s H 2 O vðÞ     s O 2  +3:76Λs N 2
              _ n f

                                                                 y
                                        ð              Þ  s f ,0 +
                                                        a
                                        Λs O 2  +3:76Λs N 2 0      n v s H 2 O lðÞ,0
                                                                 2
                                                                         (8.12)
              Rearranging Eq. (8.12) to group similar species together yields
                1
                    p        f          p      a              p      a
                        a          ð       ð             ð       ð
                    0
                        0
                                       Þ   s O 2 0
                                                             Þ   s N 2 0
                   S  S  S   0  ¼ Λ s O 2 0   Þ +3:76Λ s N 2 0      Þ  s f ,0
                _ n f
                                     h                                i
                                                                       p
                                                             y
                       y
                                                                 z
                    +    n v s H 2 O lðÞ,0  + xs CO 2  +  x  +     s O 2
                       2                    + n v s H 2 O vðÞ  4  2    0
                                                                         (8.13)
              where
                                                         !
                                                       a
                                                      y O 2
                                             a
                                 ð s O 2 0 p  ð  Þ ¼ R ln                (8.14)
                                    Þ   s O 2 0
                                                       p
                                                      y
                                                       O 2

                                                       a
                                                      y  N 2
                                 ð s N 2 0 p  ð  Þ ¼ R ln                (8.15)
                                             a
                                     Þ   s N 2 0
                                                       p
                                                      y
                                                       N 2

                                      p                p
                                 ð s CO 2 0                              (8.16)
                                     Þ ¼ s CO 2 ,0  R ln y
                                                       CO 2

                                                                   ð

                                                                p sat T 0 Þ
                       p
                                                ¼ s H 2 O vðÞ ,0  R ln   (8.17)
                                          p
                        ¼ s H 2 O vðÞ ,0  R ln y  H 2 O vðÞ
                s H 2 O vðÞ
                       0                                          p 0

                                       p              p
                                  ð s O 2 0                              (8.18)
                                      Þ ¼ s O 2 ,0  R ln y
                                                      O 2
              where y denotes the mole fraction of species i (O 2 ,N 2 ,CO 2 ,H 2 O) in mix-
                     j
                     i
              ture j (air, combustion products), R is the universal gas constant, and s i,0 is the
              standard entropy of species i.
                 Substituting Eqs. (8.14)–(8.18) into Eq. (8.13) and rearranging yields
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