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226    CHAPTER 10 THERMODYNAMICS OF COMBUSTION




             and

                                            p 1 V 1 ¼ n 1 <T 1 ¼ n R <T 1
             giving

                                                   n P <T 3 V 1
                                               p 3 ¼        p 1
                                                   n R <T 1 V 3
                                                   3097
                                                 ¼        8   1 ¼ 82:59 bar:
                                                    300

             Example 3: nonadiabatic combustion in an engine
                In the previous calculation, example 2, the combustion was assumed to be adiabatic. If 10% of the
             energy liberated by the fuel was lost by heat transfer, calculate the final temperature and pressure after
             combustion.
             Solution
                The effect of heat transfer is to reduce the amount of energy available to raise the temperature of the
             products. This can be introduced in Eqn (10.30) to give Eqn (10.31).


                              U P T P ¼ ðQ v Þ   Q HT þ U R T R   U R T s  þ U P T s     (10.31)
                                            s
                In this case Q HT ¼ 0.1(Q v ) s and hence

                                U P T P ¼ 0:9ðQ v Þ þ U R T R   U R T s  þ U P T s       (10.32)
                                                s
                Substituting values gives
                                                                   4
                               U P ðT P Þ¼ 0:9   50144   16 þ 9:8696   10 þ 66802:2
                                      ¼ 887571:8kJ:
                Using a similar technique to before, the first estimate of U P (T P ) is

                                              887571:8
                                     U P ðT P Þ¼      ¼ 84369:9kJ kmol:
                                               10:52
                From the previous calculation the value of T P lies between 2500 and 3000 K, and an estimate is

                                            84369:9   76848:7
                                 T P ¼ 2500 þ                 500 ¼ 2712 K:
                                            94623:3   76848:7
                Try T P ¼ 2700 K to check for energy balance.


                             Constituent     CO 2         H 2 O         N 2
                                           121,807.5     95,927.5     67,877.4
                               u 2700
                                 n            1            2            7.52
                                nu         121,807.5    191,854.9     510,438.1


                                            U P ðT P Þ¼ 823993:7kJ:
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