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首页> 外文期刊>ACS catalysis >Kinetics on NiZn Bimetallic Catalysts for Hydrogen Evolution via Selective Dehydrogenation of Methylcyclohexane to Toluene
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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对氢化氢进化氢化的动力学

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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 degrees C showed an almost zero order with respect to MCH pressure in the high-pressure region (= 10 kPa) and nearly a positive half order with respective to H-2 pressure (= 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 H-2 present 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 H-2 pressure than that of MCH to TOL, which can be explained by the absence of a methyl group in the stnicture, 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.
机译:液体有机化学水化合物是有效的储氢介质,用于易于安全的运输。甲基环己烷(MCH)和甲苯(Tol)的化学耦合已被认为是氢载体的可行性循环之一,但仅使用Pt基贵金属催化剂报道MCH对甲苯的选择性脱氢。本研究向使用负载的NizN作为选择性的非贵金属催化剂向Tol报告MCH脱氢。进行了组合的实验和计算研究,以了解对甲基脱氢的现场要求和反应机制,与环己烷(CH)脱氢对苯(BZ)进行比较。在300-360摄氏度下进行的动力测量值对于高压区域(& = 10kPa)中的MCH压力表示几乎零级,并且几乎是与H-2压力相应的正半阶(&lt ;. = 40 KPA)。用于脱氢反应的这些动力学数据矛盾表明源自β的强化学中间体的氢化是速率确定步骤。密度函数理论(DFT)计算证实,脂族(甲基)位置基团(C6H5CH2)的脱氢Tol物种在表面上强烈地吸附,必须氢化以解吸以解吸。该氢辅助解吸机理解释了在维持氢化的金属表面活性的饲料中存在过量的H-2的基本作用。 CH至BZ反应的速率对H-2压力敏感而不是MCH对甲状腺的压力,这可以通过脱节中没有甲基来解释,这反过来减少了吸附物种的结合能量。 DFT表明,通过向Ni添加Zn的改善的Tol选择性是由于Zn原子优先占据表面(角和边缘位点)上的低配位位点,这可能是负责甲基的CC解离的未选择性位点tol。

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