Porous Al2O3/TiO2 tubes in combination with 1-ethyl-3-methylimidazolium acetate ionic liquid for CO2/N2 separation

被引:76
作者
Albo, Jonathan [1 ]
Yoshioka, Tomohisa [1 ]
Tsuru, Toshinori [1 ]
机构
[1] Hiroshima Univ, Dept Chem Engn, Higashihiroshima 7398527, Japan
基金
日本学术振兴会;
关键词
CO2; recovery; Supported liquid membranes; Ionic liquids; Ceramic supports; Membrane stability; CARBON-DIOXIDE CAPTURE; PHASE-BEHAVIOR; MEMBRANES SILMS; CO2; CAPTURE; PERMEABILITY; SELECTIVITY; SOLUBILITY; PERFORMANCE; PERMEATION; ABSORPTION;
D O I
10.1016/j.seppur.2013.11.024
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The highest CO2 solubility and commercially-available ionic liquid, 1-ethyl-3-methylimidazolium acetate ([emim][Ac]), was immobilized in porous Al2O3/TiO2 tubes in order to study the potential of using supported ionic liquid membranes based on ceramic supports for CO2/N-2 separation. The supported ionic liquid membranes (SILMs) were first prepared using a conventional immobilization procedure based on ionic liquid impregnation, and then, by coating the TiO2 mesoporous outer layer, reducing the membrane resistance to gas permeation. The permeation of these membranes to carbon dioxide and nitrogen was measured, yielding a CO2 permeance as high as P-CO2 = 2.78 +/- 0.11 x 10(-8) mol/(m(2) s Pa), with an ideal CO2/N-2 selectivity of alpha(CO2/N-2) = 30.72 +/- 0.86 for membranes prepared under the coating procedure, which outperformed the state of the art for CO2/N-2 separation in polymeric materials. The membrane stability tests demonstrated that the hydrophilic ceramic support was very effective for the immobilization of the liquid phase in the membrane for a period of 25 h and at applied feed pressures of 4 bar. Finally, the effect of water vapor in the gas stream and the effect of operation temperature on membrane separation performance were evaluated and compared. The high CO2 permeance values and comparable selectivity to polymeric materials may suggest the potential application of using Al2O3/TiO2 tubes in combination with [emim][Ac] ionic liquid for the selective removal/recovery of CO2 from a gas stream in industrial applications. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:440 / 448
页数:9
相关论文
共 56 条
[1]   Separation performance of CO2 through Supported Magnetic Ionic Liquid Membranes (SMILMs) [J].
Albo, J. ;
Santos, E. ;
Neves, L. A. ;
Simeonov, S. P. ;
Afonso, C. A. M. ;
Crespo, J. G. ;
Irabien, A. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2012, 97 :26-33
[2]   Non-dispersive absorption of CO2 in parallel and cross-flow membrane modules using EMISE [J].
Albo, Jonathan ;
Irabien, Angel .
JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2012, 87 (10) :1502-1507
[3]   Absorption of coal combustion flue gases in ionic liquids using different membrane contactors [J].
Albo, Jonathan ;
Luis, Patricia ;
Irabien, Angel .
DESALINATION AND WATER TREATMENT, 2011, 27 (1-3) :54-59
[4]   Carbon Dioxide Capture from Flue Gases Using a Cross-Flow Membrane Contactor and the Ionic Liquid 1-Ethyl-3-methylimidazolium Ethylsulfate [J].
Albo, Jonathan ;
Luis, Patricia ;
Irabien, Angel .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2010, 49 (21) :11045-11051
[5]  
Anthony JL, 2005, J PHYS CHEM B, V109, P6366, DOI 10.1021/jp0464041
[6]   Examination of the potential of ionic liquids for gas separations [J].
Baltus, RE ;
Counce, RM ;
Culbertson, BH ;
Luo, HM ;
DePaoli, DW ;
Dai, S ;
Duckworth, DC .
SEPARATION SCIENCE AND TECHNOLOGY, 2005, 40 (1-3) :525-541
[7]   Guide to CO2 Separations in Imidazolium-Based Room-Temperature Ionic Liquids [J].
Bara, Jason E. ;
Carlisle, Trevor K. ;
Gabriel, Christopher J. ;
Camper, Dean ;
Finotello, Alexia ;
Gin, Douglas L. ;
Noble, Richard D. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (06) :2739-2751
[8]   An experimental study on permeability, diffusivity, and selectivity of CO2 and CH4 through [bmim][PF6] ionic liquid supported on an alumina membrane: Investigation of temperature fluctuations effects [J].
Barghi, S. H. ;
Adibi, M. ;
Rashtchian, D. .
JOURNAL OF MEMBRANE SCIENCE, 2010, 362 (1-2) :346-352
[9]   CO2 capture by a task-specific ionic liquid [J].
Bates, ED ;
Mayton, RD ;
Ntai, I ;
Davis, JH .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 2002, 124 (06) :926-927
[10]   High-pressure phase behavior of ionic liquid/CO2 systems [J].
Blanchard, LA ;
Gu, ZY ;
Brennecke, JF .
JOURNAL OF PHYSICAL CHEMISTRY B, 2001, 105 (12) :2437-2444