Synthesis, characterization and gas permeation study of ZIF-11/Pebax® 2533 mixed matrix membranes

被引:96
作者
Ehsani, Ali [1 ]
Pakizeh, Majid [1 ]
机构
[1] Ferdowsi Univ Mashhad, Fac Engn, Dept Chem Engn, POB 9177948974, Mashhad, Iran
关键词
Mixed matrix membrane; Zeolitic imidazolate framework; ZIF-11; Pebax (R); Gas permeation; ZEOLITIC IMIDAZOLATE FRAMEWORKS; CARBON-DIOXIDE; TRANSPORT PROPERTIES; CO2/CH4; SEPARATION; INORGANIC FILLERS; CO2; ZIF-8; MMMS; PERVAPORATION; SIMULATIONS;
D O I
10.1016/j.jtice.2016.07.005
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
In this research, ZIF-11 crystals were successfully synthesized, characterized and incorporated into Pebax (R) 2533 polymer in the range of 10-70 wt% to fabricate mixed matrix membranes (MMMs). SEM images as well as results of TGA and tensile testing analyses confirmed excellent adhesion between ZIF-11 and polymer matrix, especially at 30 wt% loading. The effect of filler loading on gas transport properties of the ZIF-11/Pebax (R) 2533 MMMs was studied for pure H-2, N-2, CH4 and CO2 gases. The ZIF-11 /Pebax (R) 2533 MMMs were found to suffer from polymer chain rigidification and possibly blockage of the fillers by the polymer chains (more obvious at 10 wt% loading); which reduced the permeability of the MMMs. Results showed that at higher loadings, the sieving effect of ZIF-11 dominated the rigidification or pore blockage defects. At 50 and 70 wt% ZIF-11 loadings, a few voids were seen throughout the membranes, but no agglomeration occurred even at 70 wt% loading. Nevertheless, hydrogen ideal selectivities over other gases continued the increasing trend at 50 wt% and did not significantly reduce even at 70 wt% due to high compatibility between ZIF-11 and Pebax (R) 2533. Addition of ZIF-11 to the polymer improved the gas transport properties of the Pebax (R) 2533, especially towards H-2 separation. The highest H-2/N-2 (12.86) and H-2/CH4 (4.81) ideal selectivities were obtained at 50 and 70 wt% loadings, respectively. The highest CO2 permeability (402.89 Barrer) and CO2/CH4 selectivity (12.49) were obtained for 70 wt% loading among all the prepared membranes. (C) 2016 Taiwan Institute of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:414 / 423
页数:10
相关论文
共 49 条
[1]
Highly permeable poly(4-methyl-1-pentyne)/NH2-MIL 53 (Al) mixed matrix membrane for CO2/CH4 separation [J].
Abedini, Reza ;
Omidkhah, Mohammadreza ;
Dorosti, Fatereh .
RSC ADVANCES, 2014, 4 (69) :36522-36537
[2]
CO2-CH4 permeation in high zeolite 4A loading mixed matrix membranes [J].
Adams, Ryan T. ;
Lee, Jong Suk ;
Bae, Tae-Hyun ;
Ward, Jason K. ;
Johnson, J. R. ;
Jones, Christopher W. ;
Nair, Sankar ;
Koros, William J. .
JOURNAL OF MEMBRANE SCIENCE, 2011, 367 (1-2) :197-203
[3]
[Anonymous], 2010, ANGEW CHEM, DOI DOI 10.1002/ange.201006141
[4]
Fabrication of PEBA/ceramic nanocomposite membranes in gas sweetening [J].
Ardestani, M. Akhfash ;
Babaluo, A. A. ;
Peyravi, M. ;
Aghjeh, M. K. Razavi ;
Jannatdoost, E. .
DESALINATION, 2010, 250 (03) :1140-1143
[5]
Gas Separation Membrane Materials: A Perspective [J].
Baker, Richard W. ;
Low, Bee Ting .
MACROMOLECULES, 2014, 47 (20) :6999-7013
[6]
Polymeric mixed matrix membranes containing zeolites as a filler for gas separation applications: A review [J].
Bastani, Dariush ;
Esmaeili, Nazila ;
Asadollahi, Mahdieh .
JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY, 2013, 19 (02) :375-393
[7]
Asymmetric Matrimid®/[Cu3(BTC)2] mixed-matrix membranes for gas separations [J].
Basu, Subhankar ;
Cano-Odena, Angels ;
Vankelecom, Ivo F. J. .
JOURNAL OF MEMBRANE SCIENCE, 2010, 362 (1-2) :478-487
[8]
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
[9]
Bondar VI, 2000, J POLYM SCI POL PHYS, V38, P2051, DOI 10.1002/1099-0488(20000801)38:15<2051::AID-POLB100>3.0.CO
[10]
2-D