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8. For the conditions listed below, rank from highest to lowest, the mole fractions xi = N;/Ntot of i= CO2, CO, H20, H2, OH, 02, 0, N2, NO and N for a. propane-air constant pressure combustion at their AFT with o=0.8 (fuel lean) b. same as a., but for o=1.2 (fuel rich) Use the following supplemental data as needed: 01.05 10000 2400 CO 02 CH,-air P = 1 atm T = 298K Tmax 2278K 2200 5000 Tad 20 2000 NO Tad (K) 2000 1800 1600 1000 H2O 154 OH 1400 500 OH CO2 200 MOLE FRACTION (%) CO Ny +10 MOLE FRACTION (ppm) 100 NO 500 O2 , H2 20 0.6 0.8 1.2 1.4 1.0 EQUIVALENCE RATIO, 10 5 5 FIGURE 2.13 Equilibrium adiabatic flame temperatures and major product species for propane-air combustion at 1 atm. . H C3H8-air P = 1 atm T-298 K 2 0.7 0.8 1.2 1.3 0.9 1.0 1.1 EQUIVALENCE RATIO, FIGURE 2.14 Minor species distributions for propane-air combustion at 1 atm. Ans. a. AFT = 2020 K | | N2 H20 CO2 02 NO CO 0 H H2 0.74 0.125 0.095 0.047 3500 1700 850 160 23.5 0 ppm ppm ppm ppm ppm b. AFT = 2200 K N2 H20 CO H2 o CO2 0.078 OH 800 . 725 NO 200 02 70 0.68 0.155 0.054 0.022 20 ppm ppm ppm ppm ppm

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