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https://doi.org/10.1021/ie2005884
DC Field | Value | |
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dc.title | CO2 separation from flue gas using polyvinyl-(room temperature ionic liquid)-room temperature ionic liquid composite membranes | |
dc.contributor.author | Li, P. | |
dc.contributor.author | Pramoda, K.P. | |
dc.contributor.author | Chung, T.-S. | |
dc.date.accessioned | 2014-10-09T06:44:52Z | |
dc.date.available | 2014-10-09T06:44:52Z | |
dc.date.issued | 2011-08-03 | |
dc.identifier.citation | Li, P., Pramoda, K.P., Chung, T.-S. (2011-08-03). CO2 separation from flue gas using polyvinyl-(room temperature ionic liquid)-room temperature ionic liquid composite membranes. Industrial and Engineering Chemistry Research 50 (15) : 9344-9353. ScholarBank@NUS Repository. https://doi.org/10.1021/ie2005884 | |
dc.identifier.issn | 08885885 | |
dc.identifier.uri | http://scholarbank.nus.edu.sg/handle/10635/88660 | |
dc.description.abstract | In this work, a vinyl-functionalized room temperature ionic liquid (RTIL), 1-vinyl-3-butylimidazolium bis(trifluoromethylsulfonyl)imide ([vbim][Tf 2N]), has been successfully synthesized. The RTIL was further polymerized and mixed with 1-butyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ([bmim][Tf2N]) to form the free-standing poly([vbim][Tf2N])-[bmim][Tf2N] composite films. The compositions of [bmim][Tf2N] in the composite membranes were designed at 15, 30, 45, and 60 wt %. The pristine poly([vbim][Tf 2N]) and poly([vbim][Tf2N])-[bmim][Tf2N] composite membranes exhibit similar permeability selectivities as the standard [bmim][Tf2N] but permeabilities are enhanced up to 5 times higher than the equivalent polystyrene-RTIL and polyacrylate-RTIL membranes. An increase in [bmim][Tf2N] concentration of poly([vbim][Tf 2N])-[bmim][Tf2N] composite membranes results in an increase in solubility, diffusivity, and permeability coefficients of CO 2 and N2 but does not change the CO2/N 2 selectivities of the solubility, diffusivity, and permeability. The CO2 permeability of the 60 wt % composite at 35 °C, 10 atm is 559 barrers in pure gas tests which is closer to 60% of the [bmim][Tf 2N] permeability (i.e., 1344 barrers). In addition, the 60 wt % composite membrane exhibits a CO2 permeability of 491.2 barrers and a CO2/N2 selectivity of 20 in mixed gas tests using CO 2/N2 (50:50) as the feed. © 2011 American Chemical Society. | |
dc.description.uri | http://libproxy1.nus.edu.sg/login?url=http://dx.doi.org/10.1021/ie2005884 | |
dc.source | Scopus | |
dc.type | Article | |
dc.contributor.department | CHEMICAL & BIOMOLECULAR ENGINEERING | |
dc.description.doi | 10.1021/ie2005884 | |
dc.description.sourcetitle | Industrial and Engineering Chemistry Research | |
dc.description.volume | 50 | |
dc.description.issue | 15 | |
dc.description.page | 9344-9353 | |
dc.description.coden | IECRE | |
dc.identifier.isiut | 000293196700055 | |
Appears in Collections: | Staff Publications |
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