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首页> 美国政府科技报告 >Direct conversion of methane to methanol in a non-isothermal catalytic membrane reactor
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Direct conversion of methane to methanol in a non-isothermal catalytic membrane reactor

机译：在非等温催化膜反应器中将甲烷直接转化为甲醇

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The direct partial oxidation of CH{sub 4} to CH{sub 3}OH has been studied in a non-permselective, non-isothermal catalytic membrane reactor system. A cooling tube introduced coaxially inside a tubular membrane reactor quenches the product stream rapidly so that further oxidation of CH{sub 3}OH is inhibited. Selectivity for CH{sub 3}OH formation is significantly higher with quenching than in experiments without quenching. For CH{sub 4} conversion of 4% to 7% CH{sub 3}OH selectivity is 40% to 50% with quenching and 25% to 35% without quenching.

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