首页> 外文OA文献 >Hydro-Metathesis of Long-Chain Olefin (1-decene) using Well-Defined Silica-Supported Tungsten (VI), Molybdenum (VI) and Tantalum (V) Catalysts
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Hydro-Metathesis of Long-Chain Olefin (1-decene) using Well-Defined Silica-Supported Tungsten (VI), Molybdenum (VI) and Tantalum (V) Catalysts

机译:使用定义明确的二氧化硅负载的钨(VI),钼(VI)和钽(V)催化剂进行长链烯烃(1-癸烯)的加氢复分解

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摘要

Nowadays, catalysis lies at the heart of economy growth mainly in the petroleum industry. Catalysis can offer real and potential solutions to the current challenges for a long-term sustainable energy, green chemistry, and environmental protection. In this context, one of the most important and future prosperity promising catalytic applications in the petrochemical field is hydrocarbons metathesis; it consists on the conversion of both renewable and non-petroleum fossil carbon sources to transportation fuels. ududOlefin metathesis has become one of the standard methodologies for constructing C-C bonds in many organic transformation reactions. This owed to the numerous types of metathesis reactions that have been developed, for example, enyne, ring-opening and closing, self and cross metathesis, etc. But the one step conversion of olefin to alkanes has not been studied much. Recently, only one such a work has been published for the hydro-metathesis of propylene by tantalum hydride supported on KCC-1 in dynamic reactor.ududWith this knowledge, we thought to study the hydro-metathesis using liquid olefin (1-decene). Another aspect of using 1-decene comes from our previous experience on metathesis of n-decane where the first step is the conversion of decane to 1-decene and subsequently to different chain length alkanes with W-alkyl/alkylidene catalyst. In this way, it would be easy for us to use different catalysts and compare them with parent catalyst concerning TON. We found 100% conversion with TON of 1010 using supported WMe6 onto SiO2-700 [(≡Si-O-)WMe5] against the previous results for n-decane showing 20% conversion and TON of 153.ududIn this work, we disclose the hydro-metathesis reaction of 1-decene using well-defined silica supported W(VI), Mo(VI) and Ta(V) alkyl catalysts in batch reactor condition. udThis work is divided into three major sections; first chapter contains an introduction to the field of catalysis and surface organometallic chemistry. In second chapter, we describe all the experimental procedures of the catalysts. The third chapter is devoted to the characterization and interpretation followed by catalytic reactions. Finally, a brief conclusion of the present study is given.
机译:如今,催化是经济增长的核心,主要是在石油工业中。催化可以为长期可持续能源,绿色化学和环境保护方面的当前挑战提供切实可行的解决方案。在这种情况下,在石化领域最有希望的催化应用之一是碳氢化合物复分解。它包括将可再生和非石油化石碳源都转化为运输燃料。烯烃复分解已成为许多有机转化反应中构建C-C键的标准方法之一。这归因于已开发出多种类型的易位反应,例如烯炔,开环和闭环,自和交叉易位等。但是,对烯烃向烷烃的一步转化的研究还很少。最近,只有一种这样的工作公开发表在动态反应器中,用于负载在KCC-1上的氢化钽氢化丙烯进行丙烯的加氢复分解。 ud ud基于此知识,我们认为要研究使用液态烯烃(1-癸烯)。使用1-癸烯的另一个方面来自我们之前在正癸烷复分解方面的经验,其中第一步是将癸烷转化为1-癸烯,然后再通过W-烷基/亚烷基催化剂转化为不同链长的烷烃。这样,我们很容易使用不同的催化剂,并将它们与涉及TON的母体催化剂进行比较。我们发现,使用支持的WMe6在SiO2-700 [(SiSi-O-)WMe5]上,TON的转化率为1010,100%的转化率与先前的正癸烷转化率20%和TON值为153的结果相反。 ud ud我们公开了在间歇反应器条件下使用定义明确的二氧化硅负载的W(VI),Mo(VI)和Ta(V)烷基催化剂进行1-癸烯的加氢复分解反应。 ud这项工作分为三个主要部分;第一章介绍了催化和表面有机金属化学领域。在第二章中,我们描述了催化剂的所有实验步骤。第三章专门介绍了催化反应的表征和解释。最后,给出了本研究的简要结论。

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    Saidi Aya;

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  • 年度 2016
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  • 原文格式 PDF
  • 正文语种 en
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