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首页> 外文期刊>Fuel Processing Technology >Simultaneous desulfurization and denitrification of flue gas by catalytic ozonation over Ce-Ti catalyst
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Simultaneous desulfurization and denitrification of flue gas by catalytic ozonation over Ce-Ti catalyst

机译:Ce-Ti催化剂上催化臭氧氧化法同时进行烟气脱硫和反硝化

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摘要

A novel oxidation-removal process for simultaneous removal of NO_x and SO2 was developed, which utilized the catalytic ozonation over Ce-Ti catalyst and assisted with a glass made ammonia-based washing tower. Compared with conventional flue gas treatment, the present method acquires non-secondary pollution, minimal waste production and low operating costs. The main byproducts, ammonia sulfate and nitrate, are important fertilizers and industrially raw materials. A maximum removal of 95% for NO_x and nearly complete SO2 removal were obtained with the assistance of washing tower under the following experimental conditions: O3 concentration, 8.5 mg·L~(-1); flow of oxidant mixtures, 100 mL·min~(-1); simulated flue gas temperature, 120 °C; H2O flow, 2.4 mL·min~(-1); and total gas flow, 400 mL·min~(-1). The reaction mechanisms are discussed, and the final oxidation products are characterized. The experimental results show that the ~·OH radicals from catalytic ozonation have an oxidation-removal effect of NO_x and SO2. The multipollutant capacity of the washing tower is largely enhanced with the Ce-Ti catalyst. And the present method performs better stability with the assistance of the washing tower.
机译:开发了一种同时去除NO_x和SO2的新型氧化去除工艺,该工艺利用Ce-Ti催化剂上的催化臭氧化技术,并辅以玻璃制氨基洗涤塔。与常规烟气处理相比,本方法获得了非二次污染,废物产生最少,运行成本低。主要副产品硫酸铵和硝酸盐是重要的肥料和工业原料。在以下实验条件下,借助洗涤塔可最大去除95%的NO_x和几乎完全去除SO2:O3浓度为8.5 mg·L〜(-1)。氧化剂混合物流量,100 mL·min〜(-1);模拟烟气温度120°C; H 2 O流量,2.4mL·min〜(-1);总气体流量为400 mL·min〜(-1)。讨论了反应机理,并对最终的氧化产物进行了表征。实验结果表明,催化臭氧化的〜·OH自由基具有NO_x和SO2的氧化去除作用。 Ce-Ti催化剂大大提高了洗涤塔的多污染物处理能力。并且本发明的方法在洗涤塔的辅助下具有更好的稳定性。

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