发明名称 Process for the Selective Oxidation of Methane
摘要 The present invention is a process for converting methane to methanol, comprising: feeding methane and gaseous air or oxygen or gaseous air enriched with oxygen to a reactor under an elevated pressure; said reactor having an internal surface, made of silica or coated with silica, surrounding a zone in which said gases react; and reacting said gases in said reaction zone at an elevated temperature at conditions effective to produce methanol and for valuable oxygenates. Advantageously the internal surface is made of quartz or coated with quartz Advantageously the internal surface, made of silica (advantageously quartz) or coated with silica (advantageously quartz), is treated with HF before the conversion of methane to methanol. Advantageously the reaction is carried out in the absence in said reaction zone of any added material which measurably affects the rate of the reaction or the yield of the product. Advantageously the reactor is operated under a pressure from 1 to 7.5 MPa. Advantageously the reactor is operated at a temperature from 300° C. to 600° C. Advantageously the reactor is operated at a residence time from 0.1 to 100 s. Advantageously the reactor is operated at a methane to oxygen molar ratio from 1 to 50. The present invention also relates to a reactor having an internal surface made of silica (advantageously quartz) or coated with silica (advantageously quartz)
申请公布号 US2010280289(A1) 申请公布日期 2010.11.04
申请号 US20080669566 申请日期 2008.07.04
申请人 TOTAL PETROCHEMICALS RESEARCH FELUY 发明人 DE WINNE HENDRIK;JACOBS PIERRE;SELS BERT;VERMEIREN WALTER
分类号 C07C27/14;B01J8/04;B01J8/06;B01J19/00 主分类号 C07C27/14
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