首页> 外文期刊>Journal of Catalysis >SELECTIVE CATALYTIC REDUCTION (SCR) OF NO WITH METHANE OVER COZSM-5 AND HZSM-5 ZEOLITES - ON THE ROLE OF FREE RADICALS AND COMPETITIVE OXIDATION REACTIONS
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SELECTIVE CATALYTIC REDUCTION (SCR) OF NO WITH METHANE OVER COZSM-5 AND HZSM-5 ZEOLITES - ON THE ROLE OF FREE RADICALS AND COMPETITIVE OXIDATION REACTIONS

机译:在COZSM-5和HZSM-5沸石上用甲烷选择性催化还原NO(NO)-在自由基和竞争性氧化反应中的作用

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The reactions of CH4 with NO, NO2, and O-2, and with the mixtures of NOx + O-2, were studied over CoZSM-5 and HZSM-5 zeolites. Based on the comparison of the ''light-off' temperatures as well as the activation energies of these reactions, a conclusion is drawn that over both catalysts at temperatures below 500 degrees C NO reduction into N-2 and CH4 oxidation into COx are coupled and initiated by the reaction of CH4 with NO2. The results demonstrate that this reaction may be considered as a limiting reaction step of NO2 reduction into Nz, and of the SCR reaction for the mixture of CH4 + NO + O-2 when O-2 is present in large amounts. With the latter mixture when O-2 concentration is relatively low (up to about 1.5%) another reaction step, namely, the catalytic oxidation of NO by O-2 into NO2 appears to control the rate of the SCR process. Thus, an important role of O-2 is to convert NO into NO2. At low temperatures (below 400 degrees C) O-2 does not compete with NOx for CH4, but even at these temperatures O-2 participates in oxidation of the intermediate reaction species decreasing in this way the selectivity of the SCR process. At higher temperatures (above 450 degrees C) a strong competition between O-2 and NOx for CH4 is observed and this results in a further decrease in the process selectivity. It is shown that the higher SCR selectivity of HZSM-5 catalyst in comparison with CoZSM-5 is due to the stronger competition between O-2 and NO2 for CH4 over the latter catalyst. The effects of space velocity and reactor size were briefly explored. These results show that the reaction pathways are the same for both catalysts studied in this work. Based on these, and literature results, the formation of CH3 . free radical is postulated and possible reactions of this radical with NOx and O-2, that form the pathways of the SCR process, are considered. Finally, the possible role of gas phase reactions in the SCR process is discussed. (C) 1996 Academic Press, Inc. [References: 40]
机译:在CoZSM-5和HZSM-5沸石上研究了CH4与NO,NO2和O-2以及与NOx + O-2混合物的反应。根据“起燃”温度以及这些反应的活化能的比较,得出以下结论:两种催化剂在低于500摄氏度的温度下,NO还原成N-2和CH4氧化成COx都是耦合的并由CH4与NO2反应引发。结果表明,该反应可被认为是当O-2大量存在时CH2 + NO + O-2混合物的NO2还原成Nz和SCR反应的限制性反应步骤。对于后一种混合物,当O-2浓度相对较低(最高约1.5%)时,另一个反应步骤,即由O-2将NO催化氧化为NO2,似乎可以控制SCR过程的速率。因此,O-2的重要作用是将NO转化为NO2。在低温(低于400摄氏度)下,O-2不会与NOx争夺CH4,但即使在这些温度下,O-2也会参与中间反应物种的氧化,从而降低SCR工艺的选择性。在较高的温度(高于450摄氏度)下,观察到O-2和NOx之间对CH4的激烈竞争,这导致工艺选择性进一步降低。结果表明,与CoZSM-5相比,HZSM-5催化剂的SCR选择性更高,是由于O-2和NO2对CH4的竞争性强于后者。简要探讨了空速和反应堆大小的影响。这些结果表明,在这项工作中研究的两种催化剂的反应途径是相同的。基于这些和文献结果,形成CH 3。假定自由基,并考虑该自由基与形成SCR过程途径的NOx和O-2可能发生的反应。最后,讨论了气相反应在SCR过程中的可能作用。 (C)1996 Academic Press,Inc. [参考:40]

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