Mixed Matrix Membranes for O-2/N-2 Separation: The Influence of Temperature

被引:26
作者
Fernandez-Barquin, Ana [1 ]
Casado-Coterillo, Clara [1 ]
Valencia, Susana [2 ]
Irabien, Angel [1 ]
机构
[1] Univ Cantabria, Dept Chem & Biomol Engn, Ave Los Castros S-N, E-39005 Santander, Spain
[2] Univ Politecn Valencia, Inst Tecnol Quim, Consejo Super Invest Cient, Ave Los Naranjos S-N, E-46022 Valencia, Spain
关键词
zeolites; Si; Al = 5; poly(trimethylsilylpropyne) (PTMSP); Rho; chabazite; LTA; temperature; oxygen; nitrogen;
D O I
10.3390/membranes6020028
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
In this work, mixed matrix membranes (MMMs) composed of small-pore zeolites with various topologies (CHA (Si/Al = 5), LTA (Si/Al = 1 and 5), and Rho (Si/Al = 5)) as dispersed phase, and the hugely permeable poly(1-trimethylsilyl-1-propyne) (PTMSP) as continuous phase, have been synthesized via solution casting, in order to obtain membranes that could be attractive for oxygen-enriched air production. The O-2/N-2 gas separation performance of the MMMs has been analyzed in terms of permeability, diffusivity, and solubility in the temperature range of 298-333 K. The higher the temperature of the oxygen-enriched stream, the lower the energy required for the combustion process. The effect of temperature on the gas permeability, diffusivity, and solubility of these MMMs is described in terms of the Arrhenius and Van't Hoff relationships with acceptable accuracy. Moreover, the O-2/N-2 permselectivity of the MMMs increases with temperature, the O-2/N-2 selectivities being considerably higher than those of the pure PTMSP. In consequence, most of the MMMs prepared in this work exceeded the Robeson's upper bound for the O-2/N-2 gas pair in the temperature range under study, with not much decrease in the O-2 permeabilities, reaching O-2/N-2 selectivities of up to 8.43 and O-2 permeabilities up to 4,800 Barrer at 333 K.
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页数:12
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共 45 条
[1]   Development of matrimid/zeolite 4A mixed matrix membranes using low boiling point solvent [J].
Ahmad, Jamil ;
Hagg, May-Britt .
SEPARATION AND PURIFICATION TECHNOLOGY, 2013, 115 :190-197
[2]   Correlation of Gas Permeability and Diffusivity with Selectivity: Orientations of the Clouds of the Data Points and the Effects of Temperature [J].
Alentiev, Alexandre ;
Yampolskii, Yuri .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (26) :8864-8874
[3]  
Baker R., 2004, MEMBRANE TECHNOLOGY, P545
[4]   Synthesis and performance of polymerizable room-temperature ionic liquids as gas separation membranes [J].
Bara, Jason E. ;
Lessmann, Sonja ;
Gabriel, Christopher J. ;
Hatakeyama, Evan S. ;
Noble, Richard D. ;
Gin, Douglas L. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (16) :5397-5404
[5]   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
[6]   Energy efficiency of oxygen enriched air production technologies: Cryogeny vs membranes [J].
Belaissaoui, Bouchra ;
Le Moullec, Yann ;
Hagi, Hayato ;
Favre, Eric .
SEPARATION AND PURIFICATION TECHNOLOGY, 2014, 125 :142-150
[7]   Membrane Gas Separation: A Review/State of the Art [J].
Bernardo, P. ;
Drioli, E. ;
Golemme, G. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (10) :4638-4663
[8]   High-temperature membranes in power generation with CO2 capture [J].
Bredesen, R ;
Jordal, K ;
Bolland, O .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2004, 43 (09) :1129-1158
[9]   Hybrid membrane/cryogenic separation of oxygen from air for use in the oxy-fuel process [J].
Burdyny, Thomas ;
Struchtrup, Henning .
ENERGY, 2010, 35 (05) :1884-1897
[10]   An Efficient Polymer Molecular Sieve for Membrane Gas Separations [J].
Carta, Mariolino ;
Malpass-Evans, Richard ;
Croad, Matthew ;
Rogan, Yulia ;
Jansen, Johannes C. ;
Bernardo, Paola ;
Bazzarelli, Fabio ;
McKeown, Neil B. .
SCIENCE, 2013, 339 (6117) :303-307