Journal
JOURNAL OF NATURAL GAS SCIENCE AND ENGINEERING
Volume 35, Issue -, Pages 980-985Publisher
ELSEVIER SCI LTD
DOI: 10.1016/j.jngse.2016.09.036
Keywords
DMF; PEBA membrane; Gas separation; Carbon dioxide; Methane
Categories
Funding
- National Iranian Gas Company [193102]
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As the casting solvent affects the domain structure and hence, the permeability and diffusivity of molecules through the membrane, it is found that Dimethylformamide (DMF) changes the gas separation properties of PEBAX-1074. Membranes were prepared by solvent-evaporation method. The solvent reduced the time required for preparation the polymer solution in comparison with other solvents. In order to determine the influence of the evaporation temperature on the performance and morphology of the final membrane, three different evaporation temperatures 60, 80 and 100 degrees C were utilized. The membranes which were dried at 80 degrees C, were more selective towards CO2. Non-defective microstructure of fabricated membrane was confirmed by N-2 permeation measurement. Membrane performances were investigated by single gas permeability measurements of CO2 and CH4 at different operating temperatures (30-55 degrees C) and feed pressures (3-7 bar). The results indicated that CO2 permeability and CO2/CH4 ideal selectivity increased with feed pressure and decreased with temperature. The highest selectivity was about 24.4 at 7 bar and 30 degrees C. In this condition, CO2 permeability was 591 Barrer. Obtained result implied that utilization of DMF as a polymer solvent, considerably improves the CO2 permeability with a slight change in the ideal selectivity. (C) 2016 Elsevier B.V. All rights reserved.
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