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A DFT study and micro-kinetic analysis of acetylene selective hydrogenation on Pd-doped Cu(111) surfaces

机译:Pd掺杂Cu(111)表面乙炔选择性加氢的DFT研究和微动力学分析

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摘要

Semi-hydrogenation of acetylene in a hydrogen-rich stream is an industrially important process. Inspired by the recent experiments that Cu(111) surface doped by a small number of Pd atoms can exhibit excellent catalytic performance toward the dissociation of H-2 molecule as well as the high selective hydrogenation of acetylene as compared with pure Cu and Pd metal alone at low-temperature, here we performed systematic first-principles calculations to investigate the corresponding reaction mechanism related to the acetylene hydrogenation processes on single atom alloys (SAAs) and monolayer Pd/Cu(111) (i.e.,1.00 ML Pd/Cu(111)) model catalysts in detail, and to explore the possible factors controlling the high selectivity on SAAs. Our results clearly demonstrate that the SAA catalyst has higher selectivity for the ethylene formation than that of 1.00 ML Pd/Cu(111), and lower activity for the acetylene conversion compared with that of 1.00 ML Pd/Cu(111). The relatively high selectivity on SAA is mainly due to the facile desorption of ethylene and moderate activity in the dissociation of molecular H-2. The main factor which lowers the selectivity towards the ethylene formation on 1.00 ML Pd/Cu(111) is that this system has a higher capacity to promote the breaking of C-H/C-C bonds, which leads to the formation of carbonaceous deposits and polymers such as benzene, and thus reduces the selectivity for the ethylene formation. Meanwhile, it was found that the desorption energy of ethylene on these two surfaces was smaller than the energy barrier of further hydrogenation, which results in the absence of ethane on these two systems. Micro kinetic model analysis provides a further valuable insight into the evidence for the key factors controlling the catalytic activity and selectivity towards the selective hydrogenation,of acetylene. Our findings may help people to design a highly selective hydrogenation catalyst by controlling the balance between the H-2 dissociation and C-H/C-C bond broken processes, and a good catalyst should be the one with the modest catalytic activity in the activation of molecular H-2. At the same time, the present work provides an extremely significant mechanism, of acetylene trimerization to form benzene and carbon formation. (C) 2017 Elsevier B.V. All rights reserved.
机译:富氢流中乙炔的半氢化是工业上重要的过程。受最近实验的启发,与纯Cu和Pd金属相比,少量Pd原子掺杂的Cu(111)表面对H-2分子的解离以及乙炔的高选择性加氢表现出出色的催化性能。在低温下,我们在这里进行了系统的第一性原理计算,以研究与单原子合金(SAAs)和单层Pd / Cu(111)(即1.00 ML Pd / Cu(111) ))详细模拟催化剂,并探索控制SAA高选择性的可能因素。我们的结果清楚地表明,与1.00 ML Pd / Cu(111)相比,SAA催化剂对乙烯的形成具有更高的选择性,比1.00 ML Pd / Cu(111)具有更高的乙炔转化活性。对SAA的相对较高的选择性主要归因于乙烯的轻松解吸和分子H-2分解中的适度活性。降低1.00 ML Pd / Cu(111)上形成乙烯的选择性的主要因素是该系统具有更高的促进CH / CC键断裂的能力,这导致形成碳质沉积物和聚合物,例如苯,因此降低了乙烯形成的选择性。同时,发现在这两个表面上乙烯的解吸能小于进一步氢化的能垒,这导致在这两个系统上不存在乙烷。微观动力学模型分析为控制乙炔选择性催化加氢反应的催化活性和选择性的关键因素提供了更有价值的见解。我们的发现可能会帮助人们通过控制H-2解离与CH / CC键断裂过程之间的平衡来设计高度选择性的加氢催化剂,而良好的催化剂应该是在活化H-分子时具有适度催化活性的催化剂。 2。同时,本工作提供了乙炔三聚形成苯和碳的极其重要的机理。 (C)2017 Elsevier B.V.保留所有权利。

著录项

  • 来源
    《Applied Surface Science》 |2017年第15期|154-165|共12页
  • 作者单位

    Nankai Univ, Minist Educ, Key Lab Adv Energy Mat Chem, Dept Chem, Tianjin 300071, Peoples R China|Nankai Univ, Collaborat Innovat Ctr Chem Sci & Engn Tianjin, Tianjin 300071, Peoples R China;

    Shanxi Datong Univ, Coll Chem & Environm Engn, Datong 037009, Shanxi Province, Peoples R China;

    Nankai Univ, Minist Educ, Key Lab Adv Energy Mat Chem, Dept Chem, Tianjin 300071, Peoples R China|Nankai Univ, Collaborat Innovat Ctr Chem Sci & Engn Tianjin, Tianjin 300071, Peoples R China;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    First-principles calculations; Acetylene selective hydrogenation; Single atom alloys (SAM); 1.00 ML Pd/Cu(111);

    机译:第一性原理计算;乙炔选择性加氢;单原子合金(SAM);1.00 ML Pd / Cu(111);

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