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Kinetics on NiZn Bimetallic Catalysts for Hydrogen Evolution via Selective Dehydrogenation of Methylcyclohexane to Toluene

机译:甲基环己烷选择性脱氢制甲苯的NiZn双金属催化剂的动力学研究

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摘要

Liquid organic chemical hydrides are effective hydrogen storage media for easy and safe transport. The chemical couple of methylcyclohexane (MCH) and toluene (TOL) has been considered one of the feasible cycles for a hydrogen carrier, but the selective dehydrogenation of MCH to TOL has been reported using only Pt-based noble metal catalysts. This study reports MCH dehydrogenation to TOL using supported NiZn as a selective, non-noble-metal catalyst. A combined experimental and computational study was conducted to provide insight into the site requirements and reaction mechanism for MCH dehydrogenation to TOL, which were compared with those for cyclohexane (CH) dehydrogenation to benzene (BZ). The kinetic measurements carried out at 300-360°C showed an almost zero order with respect to MCH pressure in the high-pressure region (â\u89¥10 kPa) and nearly a positive half order with respective to H2pressure (â\u89¤40 kPa). These kinetic data for the dehydrogenation reaction paradoxically indicate that hydrogenation of a strongly chemisorbed intermediate originating from TOL is the rate-determining step. Density functional theory (DFT) calculation confirms that the dehydrogenated TOL species at the aliphatic (methyl) position group (C6H5CH2) were strongly adsorbed on the surface, which must be hydrogenated to desorb as TOL. This hydrogen-assisted desorption mechanism explains the essential role of excess H2present in the feed in maintaining the activity of the metallic surface for hydrogenation. The rate of the CH to BZ reaction was less sensitive to H2pressure than that of MCH to TOL, which can be explained by the absence of a methyl group in the structure, which in turn reduces the binding energy of the adsorbed species. DFT suggests that the improved TOL selectivity by adding Zn to Ni was due to Zn atoms preferentially occupying low-coordination sites on the surface (the corner and edge sites), which are likely the unselective sites responsible for the C-C dissociation of the methyl group of TOL. (Chemical Equation Presented).
机译:液态有机化学氢化物是有效且容易运输的有效氢存储介质。甲基环己烷(MCH)和甲苯(TOL)的化学对被认为是氢载体可行的循环之一,但据报道仅使用Pt基贵金属催化剂将MCH选择性脱氢为TOL。这项研究报告了使用负载型NiZn作为选择性非贵金属催化剂将MCH脱氢成TOL。进行了组合的实验和计算研究,以深入了解MCH脱氢制TOL的位点要求和反应机理,并与环己烷(CH)脱氢制苯(BZ)的条件和反应机理进行了比较。在300-360°C下进行的动力学测量表明,高压区(â€10 kPa)的MCH压力几乎为零阶,而H2压力(â89)则几乎为正半序。 40 kPa)。这些脱氢反应的动力学数据反常地表明,源自TOL的强烈化学吸附的中间体的氢化是决定速率的步骤。密度泛函理论(DFT)的计算证实,脂族(甲基)位置基团(C6H5CH2)上的脱氢TOL物质强烈吸附在表面上,必须进行氢化才能作为TOL脱附。这种氢辅助解吸机理解释了进料中存在的过量H2在维持金属表面氢化活性方面的重要作用。 CH对BZ的反应速率对H2压力的敏感性不如MCH对TOL敏感,这可以通过结构中不存在甲基来解释,这继而降低了吸附物质的结合能。 DFT表明,通过向Zn中添加Zn改善的TOL选择性是由于Zn原子优先占据了表面上的低配位位点(角和边缘位点),这很可能是造成CC甲基CC解离的非选择位点。 TOL。 (呈现化学方程式)。

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