Page 236 - Advanced Thermodynamics for Engineers, Second Edition
P. 236

224    CHAPTER 10 THERMODYNAMICS OF COMBUSTION




                Combustion equation is:

                                                                                         (10.30)
                                 U P T P ¼ ðQ v Þ þ U R T R   U R T s  þ U P T s
                                               s
                Reactants energy [U R (T R )   U R (T s )] is

                                Constituent     CH 4        O 2         N 2
                                              21,883.9    15,105.9    14,587.7
                                   u 689.2
                                               5719.6      6032.0     6025.8
                                   u 298
                                 Difference   16,164.3     9073.9     8561.9
                                    n            1           2         7.52
                                    nu        16,164.3    18,146.4    64,385.5


                                                                     4
                                   Thus U R T R   U R T s  ¼ 9:8696   10 kJ
                Products energy at standard temperature, U P (T s ), is


                                 Constituent    CO 2       H 2 O       N 2
                                    u 298      7041.6     7223.3      6025.8
                                     n           1          2          7.52
                                   nu 298      7041.6     14,446.6   45,314.0

                                          Hence U P ðT s Þ¼ 66802:2kJ:

                Substituting these values into Eqn (10.30), and converting the calorific value to molar terms gives
                                                                4
                                  U P ðT P Þ¼ 50144   16 þ 9:8696   10 þ 66802:2
                                                   5
                                        ¼ 9:678   10 kJ:
                The value of specific internal energy for the mixture of products is

                                                 9:678   10 5

                                         U P ðT P Þ
                                                            ¼ 92000 kJ kmol:
                                 u P T P ¼     ¼
                                           n P      10:52
                An approximate value of the temperature can be obtained by assuming the exhaust products to be
             70% N 2 and 30% CO 2 . Using this approximation gives
                                               T          U P (T P )
                                             2500        76,848.7
                                             3000        94,623.3
   231   232   233   234   235   236   237   238   239   240   241