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Catalysis of ethanol synthesis from syngas.

机译:合成气催化合成乙醇。

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Catalytic synthesis of ethanol and other higher alcohols from CO hydrogenation has been a subject of significant research since the 1980s. The focus of this research is to establish a better fundamental insight into heterogeneous catalysis for CO hydrogenation reactions, in an attempt to design the best catalysts for ethanol synthesis.;It has been reported widely that promoted Rh-based catalysts can exhibit high selectivity to C2+ oxygenates during CO hydrogenation. The doubly promoted Rh-La-V/SiO2 catalysts exhibited higher activity and selectivity for ethanol and other C2+ oxygenates than singly promoted catalysts. The better performance appears to be due to a synergistic promoting effect of the combined La and V additions through intimate contact with Rh.;The kinetic study carried out in this study shows that, in general, increasing H2 pressure resulted in increased activities while increasing CO partial pressure had an opposite effect. Langmuir-Hinshelwood rate expressions for the formation of methane and of ethanol were derived and compared to the experimentally derived power law parameters. It was found that the addition of different promoters appeared to result in different rate limiting steps.;Strong metal-oxide interactions (SMOI) of Rh and vanadium oxide (as a promoter) supported on SiO2 was studied. It was found by SSITKA (steady-state isotopic transient kinetic analysis) that the concentration of surface reaction intermediates decreased on Rh/V/SiO2 as the reduction temperature increased, but the activities of the reaction sites increased. The results suggest that Rh being covered by VOx species is probably the main reason for the decreased overall activity induced by high reduction temperature, but more active sites appear to be formed probably at the Rh-VOx interface.;The mechanism of C1 and C2 hydrocarbon and oxygenate formation during CO hydrogenation on Rh/SiO2 was for the first time investigated in detail using multiproduct SSITKA. Based on SSITKA results, methanol and CH4 appeared to be produced on different active sites. It is possible that C2 products share at least one intermediate with CH4, but not with methanol. Moreover, C2 hydrocarbons are not likely to be formed from adsorbed acetaldehyde.
机译:自1980年代以来,由CO加氢催化合成乙醇和其他高级醇一直是重要的研究课题。这项研究的重点是建立一个更好的基础知识,以了解CO加氢反应的非均相催化,以尝试设计用于乙醇合成的最佳催化剂。;广泛地报道,已推广的Rh基催化剂对C2 +具有较高的选择性。在CO加氢过程中氧化。与单促进催化剂相比,双促进Rh-La-V / SiO2催化剂对乙醇和其他C2 +含氧化合物具有更高的活性和选择性。更好的性能似乎归因于La和V的混合添加通过与Rh的紧密接触产生的协同促进作用。动力学研究表明,总体上讲,增加H2压力会导致活动增加,同时增加CO分压产生相反的效果。得出了甲烷和乙醇形成的Langmuir-Hinshelwood速率表达式,并将其与实验得出的幂律参数进行了比较。发现添加不同的促进剂似乎导致了不同的限速步骤。研究了Rh和负载在SiO2上的钒氧化物(作为促进剂)之间的强金属-氧化物相互作用(SMOI)。通过SSITKA(稳态同位素瞬态动力学分析)发现,随着还原温度的升高,Rh / V / SiO2表面反应中间体的浓度降低,但反应位点的活性增加。结果表明,Rh被VOx所覆盖可能是高还原温度引起整体活性下降的主要原因,但在Rh-VOx界面上似乎形成了更多的活性位。; C1和C2烃的机理首次使用多产品SSITKA详细研究了在Rh / SiO2上CO加氢过程中形成的氧化物。根据SSITKA结果,甲醇和CH4似乎在不同的活性位点产生。 C2产品有可能与CH4共享至少一种中间体,而不与甲醇共享。而且,C 2烃不太可能由吸附的乙醛形成。

著录项

  • 作者

    Gao, Jia.;

  • 作者单位

    Clemson University.;

  • 授予单位 Clemson University.;
  • 学科 Engineering Chemical.
  • 学位 Ph.D.
  • 年度 2010
  • 页码 151 p.
  • 总页数 151
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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