催化氧化工业过程和汽车尾气排放的气体中的一氧化碳

I. G. Melikova, A. Efendi, E. Babayev, G. M. Faradjev, K.Sh. Musazade, A.M. Salahli, L.G. Maqerramova
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引用次数: 0

摘要

研制了一种不含贵金属氧化物的新型催化剂,并对其在废气中一氧化碳的完全中和和挥发性烃的深度氧化过程中的应用前景进行了研究。结果表明,在673 ~ 693k温度和5000 ~ 10000 h-1体积速度下,以Al2O3、SiO2、tio2为载体的钒磷氧化物及其1 ~ 3%的Cu、Cr、Co、Zn氧化物改性催化剂的活性可将深度氧化过程的转化率提高到95 ~ 100%。在CO和c3h8同时氧化时,CO转化率为90%,c3h8转化率为70%。在合成的催化系列的参与下,CO和C1-C4烃类特别是丙烷的氧化是通过逐步结合的机制进行的。CO和c3h8的氧化需要1:20-25 mol的高氧含量。除了利用机动车废气中的一氧化碳外,这些催化系统还可以成功地用于中和工业气体,特别是炼油厂和火力发电厂排放的气体。初步研究表明,这些催化系统可以在不改变活性的情况下运行约50000小时。
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Catalytic oxidation of CO in gases emitted by industrial processes and vehicle exhaust
A new type of catalysts not containing noble metal oxides have been developed and the possibilities of their application both for the complete neutralization of carbon monoxide in exhaust gases and the process of deep oxidation of volatile hydrocarbons are studied. It has been foundthatthe activity of catalysts based on vanadiumandphosphorus oxides supported on Al2O3, SiO2, TiO2by and their modification withof 1–3% oxides of Cu, Cr, Co, Zn enhanced the conversion of the deep oxidation process to 95–100% at the temperatures of 673–693K and volumetric velocities of 5000–10000 h–1. During the simultaneous oxidation of CO and C3H8at a CO conversion of 90%, the C3H8conversionwas 70%. It has been established that oxidation of CO and C1–C4 hydrocarbons, and especially propane, with the participation of synthesized catalytic series, occurs by stepwise and associative mechanisms. The oxidation of CO and C3H8required a high oxygen content of 1:20–25 mol. Besides utilizing carbon monoxide in exhaust gases from motor vehicles, these catalytic systems can be successfully used to neutralize industrial gases, especially those emitted from oil refineries and thermal power plants. Preliminary research has shown that these catalytic systems can operate for about 50000 hours without changing the activity.
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