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Chemical kinetic modeling of oxidation of hydrocarbon emissions in spark ignition engines

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Academic year: 2021

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Figure  2.2:  Simulated in-cylinder temperature and pressure for the baseline case of Kaiser et al
Figure  2.3:  Mole fractions of propane and its primary products of partial oxidation for T=1200  K, unburned mixture  fraction:  1%,  )=0.9.(top) burned gas composition in equilibrium
Figure  3.2:  Mole fractions of n-butane and its primary products of partial oxidation for T=1000 K, X u (fraction of unburned gas)=0.01, (top) lean mixture (=-0.9);  (bottom) rich mixture  ()=1.15)
Figure  3.4:  Mole fractions of toluene and its primary products of partial oxidation for T=1000  K, X u (fraction of unburned gas)=0.01, (top) lean mixture (=-0.9);  (bottom) rich mixture  ((I=l.15).
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