Journal
JOURNAL OF MEMBRANE SCIENCE
Volume 451, Issue -, Pages 85-93Publisher
ELSEVIER SCIENCE BV
DOI: 10.1016/j.memsci.2013.09.029
Keywords
Zeolitic imidazolate frameworks; ZIF-8 membrane; Gas permeation; Diffusion; C3H6/C3H8; separation
Categories
Funding
- National Science Foundation [CBET-1160084]
- Petroleum Research Fund
- American Chemical Society [50928-ND9]
- Guangzhou Elite Project
- Div Of Chem, Bioeng, Env, & Transp Sys
- Directorate For Engineering [1160084] Funding Source: National Science Foundation
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High qualify ZIF-8 membranes of about 2.5 mu m in thickness were prepared on alpha-Al2O3 support by secondary growth synthesis in water solution. Single He, H-2, CO2, N-2, CH4, C3H6 and C3H8 permeation data for the ZIF-8 membranes were measured and analyzed by a permeation model to obtain diffusivity values of these gases in ZIF-8 crystals. The diffusivity values obtained from gas pet meance tests were in the range of 1 x 10(-6)- X 10(-4) cm(2)/s. Diffusivity value decreases with increasing molecular size in the order He > H2> CO2, > N-2> CH4. Gas permeance for the above light gases remains constant while for C3H6 and C3H8 pet meance decreased with increasing pressure due to the specific pressure dependency of the adsorption isotherm respective to each gas. The determined diffusivity for propylene and propane is 1.25 x 10(-8) cm(2)is and 3.99 x 10(-10) cm2/s with activation energy for diffusion of 12.7 kJimol and 38.8 kilmol respectively. With equal-molar binary feed, the ZIF-8 membranes exhibit consistent C3H6/C3H8 selectivity of about 30 and C3H6 permeance of 11 x 10(-8) mol/m(2)sPa. A month long stability test shows stable gas permeance and separation performance of the ZIF-8 membranes in both atmospheric conditions and C3H6/C3H8 mixture stream. (C) 2013 Elsevier B.V. All rights reserved.
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