Preparation and characterization of novel Ionic liquid/Pebax membranes for efficient CO2/light gases separation

被引:101
作者
Estahbanati, Ehsan Ghasemi [1 ]
Omidkh, Mohammadreza [1 ]
Amooghin, Abtin Ebadi [2 ]
机构
[1] Tarbiat Modares Univ, Fac Chem Engn, POB 14115-143, Tehran, Iran
[2] Arak Univ, Fac Engn, Dept Chem Engn, Arak 3815688349, Iran
关键词
Gas separation; CO2; permselectivity; Pebax1657; copolymer; 1-Butyl-3-methylimidazolium; tetrafluoroborate ([BMIM][BF4]) ionic liquid; MIXED MATRIX MEMBRANES; CARBON-DIOXIDE; TRANSPORT-PROPERTIES; COMPOSITE MEMBRANES; GEL MEMBRANES; CO2; LIQUIDS; TEMPERATURE; ZEOLITE; IMIDAZOLIUM;
D O I
10.1016/j.jiec.2017.02.017
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
In this study, the goal is to incorporate superior features of the Pebax 1657 copolymer, such as high mechanical resistance and exceptional gas permeability especially for polar gases, with the affinity of the 1-butyl-3-methylimidazolium tetrafluoroborate ([BMIM[BF4]) ionic liquid to CO2 gas, which results in increasing the permselectivity of the membranes for CO2/light gases separation. Generally, the CO2 solubility in ILs increases with pressure increment, and temperature decrement. Therefore, gas permeation results of prepared membranes were obtained at temperature of 35 C and feed pressure range 2-10 bar. SEM, ATR and DSC analysis were carried out on different compositions of membranes and the results showed that adding the IL to the polymer make membranes more amorphous and less crystalline which lead to increase permeability for all tested gases. In addition, due to the high affinity of CO2 in both polymer and IL, both CO2 permeability and selectivity increased simultaneously with increasing IL content. This is confirmed by gas permeation results, where at 35 degrees C and 10 bar, the CO2 permeability increased from 110 Barrer for neat Pebax to 190 Barrer in the blended membrane containing 50 wt.% IL (about 73%). The related CO2/CH4 and CO2/N-2 selectivities were increased from 20.8 to 24.4 (about 17%) and from 78.6 to 105.6 (about 34%), respectively. Thus, these types of membranes are promising to be utilized in gas separation processes in industries for CO2 separation in order to postpone the global warming, which is nowadays the biggest threat to the universe. (C) 2017 The Korean Society of Industrial and Engineering Chemistry. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:77 / 89
页数:13
相关论文
共 79 条
[1]   Preparation and characterization of Ag+ ion-exchanged zeolite-Matrimid®5218 mixed matrix membrane for CO2/CH4 separation [J].
Amooghin, Abtin Ebadi ;
Omidkhah, Mohammadreza ;
Sanaeepur, Hamidreza ;
Kargari, Ali .
JOURNAL OF ENERGY CHEMISTRY, 2016, 25 (03) :450-462
[2]   The effects of aminosilane grafting on NaY zeolite-Matrimid®5218 mixed matrix membranes for CO2/CH4 separation [J].
Amooghin, Abtin Ebadi ;
Omidkhah, Mohammadreza ;
Kargari, Ali .
JOURNAL OF MEMBRANE SCIENCE, 2015, 490 :364-379
[3]   Enhanced CO2 transport properties of membranes by embedding nano-porous zeolite particles into Matrimid®5218 matrix [J].
Amooghin, Abtin Ebadi ;
Omidkhah, Mohammadreza ;
Kargari, Ali .
RSC ADVANCES, 2015, 5 (12) :8552-8565
[4]   A novel CO2-selective synthesized amine-impregnated cross-linked polyvinylalcohol/glutaraldehyde membrane: fabrication, characterization, and gas permeation study [J].
Amooghin, Abtin Ebadi ;
Pedram, Mona Zamani ;
Omidkhah, Mohammadreza ;
Yegani, Reza .
GREENHOUSE GASES-SCIENCE AND TECHNOLOGY, 2013, 3 (05) :378-391
[5]   Modification of ABS Membrane by PEG for Capturing Carbon Dioxide from CO2/N2 Streams [J].
Amooghin, Abtin Ebadi ;
Sanaeepur, Hamidreza ;
Moghadassi, Abdolreza ;
Kargari, Ali ;
Ghanbari, Davood ;
Mehrabadi, Zahra Sheikhi .
SEPARATION SCIENCE AND TECHNOLOGY, 2010, 45 (10) :1385-1394
[6]  
Anthony JL, 2005, J PHYS CHEM B, V109, P6366, DOI 10.1021/jp0464041
[7]   Gas transport properties of Pebax®/room temperature ionic liquid gel membranes [J].
Bernardo, Paola ;
Jansen, Johannes Carolus ;
Bazzarelli, Fabio ;
Tasselli, Franco ;
Fuoco, Alessio ;
Friess, Karel ;
Izak, Pavel ;
Jarmarova, Veronika ;
Kacirkova, Marie ;
Clarizia, Gabriele .
SEPARATION AND PURIFICATION TECHNOLOGY, 2012, 97 :73-82
[8]  
Bondar VI, 2000, J POLYM SCI POL PHYS, V38, P2051, DOI 10.1002/1099-0488(20000801)38:15<2051::AID-POLB100>3.0.CO
[9]  
2-D
[10]  
Bondar VI, 1999, J POLYM SCI POL PHYS, V37, P2463, DOI 10.1002/(SICI)1099-0488(19990901)37:17<2463::AID-POLB18>3.0.CO