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

机译:用于烟道气脱硝的镁基催化剂性能研究

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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°C, Through the analyses above, presumed that magnesia base catalyst exist activating of vice, and analyzed this vice preliminarily.
机译:控制烟气排放NOx的污染,制备新镁碱催化剂的静置混合方法,并通过直接催化分解研究脱氮烟气。通常,否则的去除率被认为是主要的评估标准。作者分析了催化剂制造工艺的煅烧温度,烟道气解吸塔的温度,床高度和效率反硝化无浓度。并讨论了FT-IR和XRD的脱硝酸盐前后的结果。实验表明,氧化镁基催化剂可用于指导催化分解不计烟道气。通过反硝化率为85%至95%。氧化镁基催化剂的成分由氧化镁,固定剂,加成剂制成。高度脱硝床为4-5厘米,脱硝反应温度为130-170℃,通过上述分析,假定氧化镁基础催化剂存在于副的副,并分析初步的副。

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