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Condensed phase conversion of bioethanol to 1-butanol and higher alcohols.

机译:生物乙醇的冷凝相转化为1-丁醇和高级醇。

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摘要

Higher alcohols are important chemical feedstocks as well as potential fuels. With the recent surge in bioethanol production, it would be advantageous to convert bioethanol to butanol and higher alcohols. Results by various authors for a wide range of reaction conditions are presented. For butanol specifically, the highest yields have been obtained with hydroxyapatite, hydrotalcite and alumina-supported nickel catalysts. The literature shows it is a challenge to convert ethanol to butanol, since no one has achieved butanol yields higher than ~30%.;In this research project, attention is focused on alumina-supported nickel, since it is robust, stable, and well suited for condensed phase ethanol Guerbet chemistry. Catalyst screening of different compositions was performed and higher alcohol selectivities were analyzed. The 8%Ni/8%La-Al2O 3 was proven to produce over 80% selectivity to higher alcohols at 50% ethanol conversion. The impacts of water removal on target alcohol yield with the 8Ni/8La catalyst were investigated in a batch reactor. Removing water decreased selectivity to CH4 and CO2 from 15% without water removal to 8% with water removal.;Preliminary kinetics of 1-butanol and 1-hexanol formation were investigated by looking at initial rates of their formation at 215°C, 230°C, and 239°C. Runs with ethanol/acetaldehyde/H2 were performed to investigate the steps of the ethanol Guerbet reaction mechanism. Runs completed at 150°C and 200°C were modeled and rate constants were determined for acetaldehyde hydrogenation, acetaldehyde condensation, and butyraldehyde hydrogenation. It was found ethanol dehydrogenation is in equilibrium and is the rate limiting step of the ethanol Guerbet mechanism. The activation energy for ethanol dehydrogenation was calculated to be 150 KJ/mol. Therefore, the effect of H2 on a neat ethanol run was examined and found to have little effect on ethanol conversion rate. Ethanol conversion rates were the same due to the side reaction of H2 with ethanol to CH 4 and water, which offsets the negative effect of hydrogen on acetaldehyde formation rate. The presence of excess H2 was found to decrease 1-butanol and 1-hexanol formation rates.
机译:高级醇是重要的化学原料以及潜在的燃料。随着最近生物乙醇生产的激增,将生物乙醇转化为丁醇和高级醇将是有利的。提出了各种作者针对各种反应条件的结果。特别是对于丁醇,使用羟基磷灰石,水滑石和氧化铝负载的镍催化剂可获得最高的收率。文献表明,将乙醇转化为丁醇是一个挑战,因为没有人能将丁醇的收率提高到约30%以上。在该研究项目中,注意力集中在氧化铝负载的镍上,因为它坚固,稳定且性能良好。适用于凝聚相乙醇Guerbet化学。进行了不同组成的催化剂筛选,并分析了更高的醇选择性。事实证明,在50%的乙醇转化率下,8%Ni / 8%La-Al2O 3对高级醇的选择性超过80%。在间歇反应器中研究了脱水对8Ni / 8La催化剂目标醇收率的影响。去除水使对CH4和CO2的选择性从未去除水的15%降低到去除水的8%。;通过研究在215°C,230°C下的初始生成速率研究了1-丁醇和1-己醇的形成动力学℃和239℃。用乙醇/乙醛/ H 2进行运行以研究乙醇Guerbet反应机理的步骤。对在150°C和200°C下完成的运行进行建模,并确定乙醛加氢,乙醛缩合和丁醛加氢的速率常数。发现乙醇脱氢是平衡的,并且是乙醇Guerbet机理的限速步骤。乙醇脱氢的活化能经计算为150 KJ / mol。因此,检查了氢气对纯乙醇运行的影响,发现对乙醇转化率的影响很小。由于H2与乙醇反应生成CH 4和水的副反应,乙醇转化率相同,这抵消了氢对乙醛形成速率的负面影响。发现过量的H 2的存在降低了1-丁醇和1-己醇的形成速率。

著录项

  • 作者

    Jordison, Tyler L.;

  • 作者单位

    Michigan State University.;

  • 授予单位 Michigan State University.;
  • 学科 Chemical engineering.
  • 学位 Ph.D.
  • 年度 2016
  • 页码 157 p.
  • 总页数 157
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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