TY - JOUR Y1 - 2015/// ID - scholars6307 N2 - Polyethersulfone (PES) as a polymer along with carbon molecular sieves (CMS) as an inorganic filler and di-ethanolamine (DEA) as the third component were used to fabricate amine mixed matrix membranes (A3Ms). The CMS and the developed membranes were characterized by variable pressure field emission scanning electron microscopy (VPFESEM) and thermal gravimetric analysis (TGA). FESEM micrographs showed that with the addition of DEA, uniform distribution of CMS particles in the PES matrix was achieved with good polymer-filler contact. The combined effect of DEA concentration (5-15 wt), feed pressure (2-10 bar) and CMS loading on the CO2/CH4 transport properties of the PES-CMS-DEA membranes were studied. The results revealed that the PES-CMS-DEA (15 wt DEA) membrane showed a CO2 permeance of 123.49 GPU at 2 bar, which is more than a threefold increment with respect to the native PES membrane. The corresponding CO2/CH4 ideal selectivity was increased from 5.40 for PES to 51.39 for PES-CMS-DEA (15 wt DEA). The CO2 permeance of the PES-CMS-DEA (A3Ms) membranes was higher than PES membranes over the operating pressure range. © The Royal Society of Chemistry 2015. AV - none KW - Carbon; Carbon dioxide; Field emission microscopes; Filled polymers; Fillers; Gravimetric analysis; Membranes; Molecular sieves; Scanning electron microscopy; Sieves; Thermogravimetric analysis KW - Carbon molecular sieve; Ideal selectivities; Inorganic fillers; Mixed matrix membranes; Operating pressure; Polyethersulfones; Thermal gravimetric analyses (TGA); Uniform distribution KW - Ethanolamines VL - 5 SN - 20462069 A1 - Nasir, R. A1 - Mukhtar, H. A1 - Man, Z. A1 - Shaharun, M.S. A1 - Abu Bakar, M.Z. PB - Royal Society of Chemistry SP - 60814 UR - https://www.scopus.com/inward/record.uri?eid=2-s2.0-84937468548&doi=10.1039%2fc5ra09015f&partnerID=40&md5=567c9105af436279430a87810f824fc8 EP - 60822 TI - Effect of fixed carbon molecular sieve (CMS) loading and various di-ethanolamine (DEA) concentrations on the performance of a mixed matrix membrane for CO2/CH4 separation JF - RSC Advances N1 - cited By 43 IS - 75 ER -