The thesis studies the influences of the desulfurization and denitrification efficiencies with oxygen and carbon dioxide in the flue gas using the oxygen-rich high active adsorbent in the optimized reaction conditions, and the inter-influence between sulfur dioxide and nitrogen oxide in a fixed bed; the kinetic parameters of heterogeneous reactions on denitrification; the products of the desulfurization and denitrification reactions are investigated by chemical analysis, physical property analysis and the SEM and X-ray analysis. The results show that the oxygen has a help to improve the desulfurization and denitrification efficiencies; the carbon dioxide is adverse to the desulfurization efficiencies and favorable to the denitrification efficiencies. There is a mutual enhancement between sulfur dioxide and nitrogen oxide. The research finds the reaction orders with respect to NO and C are 2.2 and 0.7, respectively. The activation energy in that reaction is 66.89kJ/mol. The results of products analysis show that the highly active adsorbent has a porous surface. The C adsorbent has a bigger BET surface and monolayer volume than M. The main products of the desulfurization and denitrification reactions were sulfate and nitrate, respectively. The reductive production of C is chloride. On the basis of above results, the main reactions and the mechanism of desulfurization and denitrification in the fixed bed are discussed.
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