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• W2040884416 startingPage "508" @default.
• W2040884416 abstract "The permeation and separation performance of an ultramicroporous carbon membrane for separation of CO2/N2 mixtures were investigated. The experiments were conducted using the steady-state measurement method with pure gases (dead-end mode) and a CO2/N2 gas mixture (20/80 mol.-%) (cross-flow mode) in the temperature range from 293 K to 363 K and at feed pressures of up to 1.4 MPa and atmospheric pressure on the permeate side. The membrane exhibited a selectivity of about 25 and permeability of about 500 Barrer for CO2 in the mixture with N2. The single-gas measurements do not reflect the membrane performance correctly. An adsorption-selective effect is assumed to be the main separation mechanism. Moreover, membrane-aging effects causing blocking due to pore constrictions through adsorption were observed. These pore constrictions lower the permeability, but they raise the selectivity. Operation at high temperatures leads to a reduction of aging effects." @default.
• W2040884416 created "2016-06-24" @default.
• W2040884416 creator A5006271977 @default.
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• W2040884416 date "2012-02-06" @default.
• W2040884416 modified "2023-09-26" @default.
• W2040884416 title "Separation of CO2/N2 by Means of a Carbon Membrane" @default.
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• W2040884416 doi "https://doi.org/10.1002/ceat.201100433" @default.
• W2040884416 hasPublicationYear "2012" @default.
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