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Advances in the study of coke formation over zeolite catalysts in the methanol-to-hydrocarbon process

机译:甲醇制烃工艺中沸石催化剂上焦炭形成的研究进展

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摘要

Methanol-to-hydrocarbon (MTH) process over acidic zeolite catalysts has been widely utilised to yield many types of hydrocarbons, some of which are eventually converted into the highly dehydrogenated (graphitized) carbonaceous species (cokes). The coking process can be divided into two parallel pathways based on the accepted hydrocarbon pool theory. From extensive investigations, it is reasonable to conclude that inner zeollite cavity/channel reactions at acidic sites generate cokes. However, coke formation and accumulation over the zeolite external surfaces play a major role in reaction deactivation as they contribute a great portion to the total coke amount. Herein we have reviewed previous literatures and included some recent works from KOPRC in understanding the nature and mechanism of coke formation, particularly during an H-ZSM-5 catalysed MTH reaction. We specially conclude that rapid aromatics formation at the zeolite crystalite edges is the main reason for later stage coke accumulation on the zeolite external surfaces. Accordingly, the catalyst deactivation is in a great certain to arise at those edge areas due to having the earliest contact with the incoming methanol reactant. The final coke structure is therefore built up with layers of poly-aromatics, as the potential sp2 carbons leading to pre-graphite structure. We have proposed a coke formation model particularly for the acidic catalyst, which we believe will be of assistance in understanding—and hence minimising—the coke formation mechanisms.
机译:酸性沸石催化剂上的甲醇制碳氢化合物(MTH)工艺已广泛用于生产多种类型的碳氢化合物,其中一些最终转化为高度脱氢(石墨化)的碳质物质(焦炭)。根据公认的碳氢化合物库理论,焦化过程可以分为两个平行的途径。通过广泛的研究,可以得出合理的结论,即酸性位置的内部沸石腔/通道反应会生成焦炭。然而,在沸石外表面上焦炭的形成和积累在反应失活中起主要作用,因为它们占总焦炭量的很大一部分。本文中,我们回顾了以前的文献,并包括了KOPRC最近的一些工作,以了解焦炭形成的性质和机理,特别是在H-ZSM-5催化的MTH反应过程中。我们特别得出结论,在沸石晶体边缘迅速形成芳烃是后期焦炭在沸石外表面积聚的主要原因。因此,由于与接触的甲醇反应物最早接触,因此在这些边缘区域极有可能发生催化剂失活。因此,最终的焦炭结构是由多环芳烃层构成的,因为潜在的sp2碳会导致预石墨结构。我们提出了一种专门针对酸性催化剂的焦炭形成模型,我们认为该模型将有助于理解并因此最小化焦炭形成机理。

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