Page 312 - Advanced Thermodynamics for Engineers, Second Edition
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13.5 THE EFFECT OF DISSOCIATION ON THE COMPOSITION             301




                                  0.20
                                                                HO
                                  0.15                             no dissociation
                                Mole fraction, x  0.10       Weak   dissociation


                                                                       Rich
                                  0.05
                                                          O
                                                                            H
                                  0.00
                                    0.50  0.60  0.70   0.80  0.90  1.00  1.10  1.20
                                                  Equivalence ratio, φ
               FIGURE 13.8
               Variations of hydrogen reactions, with and without dissociation for combustion of methane.


               equivalence ratios of greater than unity if there is no dissociation. However, when there is dissociation
               the quantity of oxygen in the products is increased, simply due to the reverse reaction. This reverse
               reaction also produces some unreacted hydrogen, and dissociation causes this to be produced even
               with weak mixtures. It should be noted that it was assumed that the hydrogen would be oxidised in
               preference to the carbon in the reactions without dissociation, and this explains the absence of
               hydrogen in those cases.
                  The carbon related reactions are shown in Fig. 13.7. When dissociation is neglected the carbon is
               completely oxidised to carbon dioxide in the weak and stoichiometric mixtures, with no carbon
               monoxide being formed. After the mixture becomes rich, the level of carbon monoxide increases
               linearly with equivalence ratio. When dissociation is considered carbon monoxide is formed even in


                             1.50E-01
                               0.15
                                                                  HO

                             Mole fraction, x 0.10  CO      Weak    Rich
                             1.00E-01

                                                 O
                               0.05
                             5.00E-02
                                                                   CO
                                                                          H
                                0.0
                             0.00E+00
                                                                1
                                  0.5   0.6   0.7   0.8   0.9   1.0   1.1   1.2   1.3
                                                                                  1.3
                                                                      1.1
                                                                            1.2
                                              0.7
                                        0.6
                                  0.5
                                                          0.9
                                                    0.8
                                                  Equivalence ratio, φ
               FIGURE 13.9
               Variation of composition of products with equivalence ratio for combustion of octane. Initial pressure: 1 bar,
               Initial temperature: 300 K, Compression ratio: 12, Compression index: 1.4.
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