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• W2082409196 abstract "A H2-selective MFI zeolite membrane has been crystallized as layer on a porous ceramic tube. At 510°C, this membrane can separate H2 from iso-butane/iso-butene with mixture separation factors of 70 and H2 permeances of ca. 1m3(STP)/m2 hbar. In membrane supported iso-butane dehydrogenation the conversion of iso-butane was increased by almost a factor of 2. However, a detailed analysis of the experiment showed that 2/3 of the conversion increase is based on the dilution of the feed by the sweep gas and 1/3 is due to the H2 removal." @default.
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• W2082409196 date "2001-12-01" @default.
• W2082409196 modified "2023-10-11" @default.
• W2082409196 title "Membrane supported catalytic dehydrogenation of iso-butane using an MFI zeolite membrane reactor" @default.
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• W2082409196 doi "https://doi.org/10.1016/s1566-7367(01)00053-x" @default.
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