OCR Text |
Show Figure Captions Figure 1 Gas Kinetic Flow System Figure 2 Cross-sectional Views of the control temperature tower Figure 3 Kinetics of NO oxidation by CHaOH Gas mixture = S~ Oe, 400 ppm CHaOH, 21S ppm NO, balance inert Reaction times = 0.9sec, + O.lsec, * 0.04Bsec, Cl 0.024sec. Figure 4 Experimental data for relative rates of NO oxidation and SOa reduction; Solid points method B, Open points method C Figure S NO conversion during gas and coal firing CHaOH/NO = 1 for all cases = gas firing 240 ppm NO, 0 ppm SOx + c gas firing 240 ppm NO, 1100 ppm SOx • = coal firing lOBO ppm NO, 730 ppm SOx =igure 6 Modeling calculations for Oxidation of NO by CHaOH, 3as mixture = 215 ppm NO, 400 ppm CHaOH, 5Y. De, balance inert ~igure 7 Predictions of the reduction of 30 ppm Sea in the presence of methanol )xidation under isothermal conditions • . Reaction mixture c 4Y. Oe, 2000 ppm SOe, 30 ppm ;Oa, 40 ppm CHaOH, balance inert ~igure B Computer modeling of the relative rate of NO oxidation and SOa reduction :alculations at 6000C with a reaction mixture of 10 ppm SOa, 500 ppm SOe, 600 ppm NO, BOO .pm CHaOH, balance inert |