4.7 Article

A single step methane conversion into synthetic fuels using microplasma reactor

期刊

CHEMICAL ENGINEERING JOURNAL
卷 166, 期 1, 页码 288-293

出版社

ELSEVIER SCIENCE SA
DOI: 10.1016/j.cej.2010.08.001

关键词

Non-thermal discharge; Microreactor; Methanol; Syngas; DME

资金

  1. MEXT, Japan [20656038]
  2. foundation STW
  3. applied science division of NWO
  4. Ministry of Economic Affairs, The Netherlands [06626]
  5. Grants-in-Aid for Scientific Research [20656038] Funding Source: KAKEN

向作者/读者索取更多资源

Direct conversion of natural gas into synthetic fuels such as methanol attracts keen attention because direct process can reduce capital and operating costs of high temperature, energy intensive, multi-step processes. We report a direct and selective synthesis of organic oxygenates such as methanol, formaldehyde, and formic acid via methane partial oxidation at room temperature using non-thermal discharge microreactor. Heat generated by methane partial oxidation is removed efficiently in the microreactor configuration: liquid components are condensed on the reactor wall and separated from O(2)-rich reactive plasma, enabling selective synthesis of oxygenates while high methane conversion is achieved in a single reactor. As a result, organic oxygenates were synthesized with one-pass yield of 5-20% with 70-30% selectivity. In addition to oxygenates, syngas was produced with selectivity of 40% and H(2)/CO = 1. Assuming one step catalytic DME synthesis as a post-discharge process, one-pass liquid yield of 30% with 80% selectivity is feasible. (C) 2010 Elsevier B.V. All rights reserved.

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