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Solid oxide membrane reactors: catalyst development and testing for solid oxide fuel cells and oxidative coupling of methane.

机译:固体氧化物膜反应器:用于固体氧化物燃料电池的催化剂开发和测试以及甲烷的氧化偶联。

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摘要

In this dissertation, solid oxide membrane reactors were fabricated and tested as 1) fuel cells operating directly on ethanol and 2) for the production of ethane and ethylene directly from methane. The first part of this dissertation discusses results from a study where solid oxide fuel cells were fabricated with Ni based anodes and operated directly on ethanol fuel. In this study, small amounts of Sn (1wt% on a metals basis) added to the surface of the Ni anode improved the carbon tolerance of the fuel cells. Improved carbon tolerance of the Sn/Ni alloy electrocatalysts led to enhanced electrochemical stability as well as less carbon deposition within the anode as compared to the monometallic Ni samples. The second part of this dissertation presents an analysis of membrane and packed bed plug flow reactors for the process of oxidative coupling of methane (OCM) using kinetic data from the literature. This analysis demonstrated that the use of membrane reactors for OCM can theoretically result in higher yields of ethane and ethylene products compared to packed bed reactors. The final part of the dissertation presents experimental work directed towards the development of membrane reactors for OCM. This work included a catalyst screening which identified lanthanum gallate doped with strontium and magnesium (La0.8Sr0.2Ga0.8Mg0.2O3-x , LSGM) as a promising catalyst for use in membrane reactors for OCM. Integration of this catalyst into a membrane reactor showed high selectivity to ethane and ethylene, however, due to low membrane surface area, the methane conversion was very small and decreased over time, possibly due to carbon poisoning of the catalyst surface.
机译:本文以固体氧化物膜反应器为研究对象,对其进行了测试:1)直接在乙醇上运行的燃料电池; 2)直接由甲烷生产乙烷和乙烯的燃料电池。本文的第一部分讨论了一项研究的结果,在该研究中,使用Ni基阳极制造固体氧化物燃料电池,并直接在乙醇燃料上运行。在这项研究中,向镍阳极表面添加少量的锡(以金属计为1wt%)可改善燃料电池的碳耐受性。与单金属Ni样品相比,Sn / Ni合金电催化剂的碳耐受性提高,导致电化学稳定性增强,阳极内的碳沉积减少。本文的第二部分利用来自文献的动力学数据,对用于甲烷氧化偶联(OCM)过程的膜式和填充床活塞流反应器进行了分析。该分析表明,与填充床反应器相比,将膜反应器用于OCM可以在理论上提高乙烷和乙烯产品的收率。论文的最后一部分提出了针对OCM膜反应器开发的实验工作。这项工作包括催化剂筛选,确定了掺有锶和镁的没食子酸镧(La0.8Sr0.2Ga0.8Mg0.2O3-x,LSGM)是有前途的催化剂,可用于OCM膜反应器。将该催化剂整合到膜反应器中显示出对乙烷和乙烯的高选择性,但是,由于低的膜表面积,甲烷转化率非常小并且随时间降低,这可能是由于催化剂表面的碳中毒。

著录项

  • 作者单位

    University of Michigan.;

  • 授予单位 University of Michigan.;
  • 学科 Chemical engineering.
  • 学位 Ph.D.
  • 年度 2016
  • 页码 184 p.
  • 总页数 184
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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