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- W260242425 abstract "Objective is to demonstrate the effectiveness of a catalytic membrane reactor (ceramic membrane combined with catalyst) to selectively produce methanol by partial oxidation of methane. None of the membranes tested in a high pressure system could selectively remove methanol, until a cooling tube was inserted inside the membrane reactor to quench the product stream; this effectively increased methanol selectivity 2{times} during methane oxidation. For both conditions, combined selectivity for methanol and CO is constant, 85%. The remaining product is CO{sub 2}. The membranes were broken when removed from the system; this was remedied when a cooling tube with a smaller diameter was used." @default.
- W260242425 created "2016-06-24" @default.
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- W260242425 date "1992-12-03" @default.
- W260242425 modified "2023-09-24" @default.
- W260242425 title "Direct methane conversion to methanol. Quarterly project status report, July 1, 1992--September 30, 1992" @default.
- W260242425 doi "https://doi.org/10.2172/10131031" @default.
- W260242425 hasPublicationYear "1992" @default.
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