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Study of the Performance on Magnesia Base Catalyst Used for Flue Gas Denitration

机译:氧化镁基烟气脱硝催化剂的性能研究

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To control contamination of flue gas emission NOx, the auther mixed method of preparing new magnesia base catalyst and researched on denitrificating flue gas by directness catalytic decomposition. Usually removal rate of NO is regarded on the main evaluation criteria. The author analysed calcination temperature of catalyzer manufacturing process, the temperature of flue gas desorption tower, bed height and efficiency denitrification of NO concentration. And discussed the result of both denitrate fore-and-aft of FT-IR and XRD. The experiment indicate that magnesia base catalyst is available to directness catalytic decomposition denitrificate flue gas. Through denitrification rate is from 85% to 95%.The ingredient of magnesia base catalyst is made from magnesia, firming agent, addition agent. Height denitration bed was 4-5 cm, denitration reaction temperature is 130-170 ℃, Through the analyses above, presumed that magnesia base catalyst exist activating of vice, and analyzed this vice preliminarily.
机译:为了控制烟气排放NOx的污染,采用混合法制备新型镁碱催化剂,并通过直接催化分解法对烟气进行脱氮研究。通常,将NO去除率视为主要评估标准。作者分析了催化剂制造过程中的煅烧温度,烟气脱附塔的温度,床高和NO浓度的有效脱氮。并讨论了FT-IR和XRD前后反硝化的结果。实验表明,氧化镁碱催化剂可用于催化分解脱硝烟气。通过反硝化率为85%至95%。氧化镁碱催化剂的成分由氧化镁,固化剂,添加剂组成。高度脱硝床为4-5 cm,脱硝反应温度为130-170℃,通过以上分析,假定氧化镁碱催化剂存在副反应活化,并对此进行了初步分析。

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