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- W1966608736 abstract "MFI type zeolite membranes were synthesized in a recirculating flow system at 95 °C where the synthesis solution was flown over the tubular α-alumina supports. The performance of the membranes for the separation of binary gas mixtures and alcohol/water liquid mixtures was investigated. A membrane synthesized by two consecutive synthesis steps had a separation selectivity of 15 and 11 for equimolar mixtures of n-C4H10/CH4 and n-C4H10/N2 at 200 °C, respectively. The membrane selectively permeated large n-C4H10 over small CH4 and N2, suggesting that the separation is essentially adsorption-based and the membrane has few nonselective intercrystalline pores. The selectivities in the pervaporation separation of 5% ethanol/95% water mixture were 43 and 23 with permeate fluxes of 0.2 and 1.9 kg/m2 h at 25 and 85 °C, respectively. The separation performance of membranes showed that MFI type membranes prepared in a recirculating flow system can be used both in the separation of gas and liquid mixtures." @default.
- W1966608736 created "2016-06-24" @default.
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- W1966608736 date "2010-01-01" @default.
- W1966608736 modified "2023-10-14" @default.
- W1966608736 title "Separation of gas and organic/water mixtures by MFI type zeolite membranes synthesized in a flow system" @default.
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- W1966608736 doi "https://doi.org/10.1016/j.micromeso.2009.07.004" @default.
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