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Efficient synthesis of ethanol and acetic acid from methane and carbon dioxide with a continuous, stepwise reactor

Authors

  • W. Huang,

    Corresponding author
    1. Key Laboratory of Coal Science and Technology, Ministry of Education and Shanxi Province, Institute Coal Chemical Engineering, Taiyuan University of Technology, Taiyuan 030024, P.R. China
    • Key Laboratory of Coal Science and Technology, Ministry of Education and Shanxi Province, Institute Coal Chemical Engineering, Taiyuan University of Technology, Taiyuan 030024, P.R. China
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  • W. Z. Sun,

    1. Key Laboratory of Coal Science and Technology, Ministry of Education and Shanxi Province, Institute Coal Chemical Engineering, Taiyuan University of Technology, Taiyuan 030024, P.R. China
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  • F. Li

    1. Key Laboratory of Coal Science and Technology, Ministry of Education and Shanxi Province, Institute Coal Chemical Engineering, Taiyuan University of Technology, Taiyuan 030024, P.R. China
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Abstract

The synthesis of C2-oxygenates such as ethanol and acetic acid accomplished by CH4 dissociation and subsequent CO2 insertion onto methyl radicals, named the stepwise reaction technology, has been demonstrated to be both feasible and efficient through initial experiments conducted in microreactor units. This article describes the development of this technology, highlighting the aforementioned stepwise technology using a dual-reactor system, which can ensure that two raw gases enter the reactor uninterruptedly and are not mixed after reaction. The system productivity for acetic acid and ethanol displayed efficiencies greater than 5–10 times that of previous microreactor units. The investigation of mechanism indicates that acetic acid arises from insertion of CO2 into M[BOND]CHx, while ethanol is formed either by hydrogenation of acetic acid or by hydration of C2H4, which results from homo-coupling of CH4. The latter route is the preferred of the two. © 2009 American Institute of Chemical Engineers AIChE J, 2010

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