2009
DOI: 10.1016/j.cej.2008.11.021
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Gas separations in fluoroalkyl-functionalized room-temperature ionic liquids using supported liquid membranes

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Cited by 223 publications
(231 citation statements)
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“…Imidazolium-based task-specific ionic liquids on porous hydrophilic polytetrafluoroethylene support 800 7.7 × 10 −9 55 [21] Imidazolium-based ionic liquids in polysulfone support 330-740 7.3 × 10 −10 to 1.6 × 10 −9 4.7-6.0 [28] Imidazolium-based ionic liquids in polyethersulfone microfiltration support 360-980 8.0 × 10 −10 to 2.2 × 10 −9 6.6-10 [6] Phosphonium-based ionic liquids supported on glass fiber disk filters 544-1700 2.8 × 10 −10 to 8.8 × 10 −10 12-13 [27] Supported ionic liquid membranes on poly vinylidene fluorolide support 94-750 2.1 × 10 −10 to 1.7 × 10 −9 5.7-23 [18] Imidazolium-based supported ionic liquid membranes on PES porous disk support 310-740 7.9 × 10 −10 to 1.9 × 10 −9 10-27 [29] Imidazolium-based fluoroalkyl-functionalized supported room-temperature ionic liquid membranes on porous polyethersulfone support 210-320 4.9 × 10 −10 to 7.4 × 10 −10 13-19 [22] Supported ionic liquid membranes prepared on polyvinylidene fluorolide support 6 5.0 × 10 −11 30 [30] Imidazolium-based SILMs on porous hydrophilic polyethersulfone 610-1050 1.3 × 10 −9 to 2.3 × 10 −9 11-20 [8] that several aminopyridinium compounds are thermally stable to at least 550 K [17]. The option of dissolving one ionic liquid with a particular functionality in a bulk ionic liquid with well defined physical properties offers another avenue for obtaining membranes suitable for certain separations.…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…Imidazolium-based task-specific ionic liquids on porous hydrophilic polytetrafluoroethylene support 800 7.7 × 10 −9 55 [21] Imidazolium-based ionic liquids in polysulfone support 330-740 7.3 × 10 −10 to 1.6 × 10 −9 4.7-6.0 [28] Imidazolium-based ionic liquids in polyethersulfone microfiltration support 360-980 8.0 × 10 −10 to 2.2 × 10 −9 6.6-10 [6] Phosphonium-based ionic liquids supported on glass fiber disk filters 544-1700 2.8 × 10 −10 to 8.8 × 10 −10 12-13 [27] Supported ionic liquid membranes on poly vinylidene fluorolide support 94-750 2.1 × 10 −10 to 1.7 × 10 −9 5.7-23 [18] Imidazolium-based supported ionic liquid membranes on PES porous disk support 310-740 7.9 × 10 −10 to 1.9 × 10 −9 10-27 [29] Imidazolium-based fluoroalkyl-functionalized supported room-temperature ionic liquid membranes on porous polyethersulfone support 210-320 4.9 × 10 −10 to 7.4 × 10 −10 13-19 [22] Supported ionic liquid membranes prepared on polyvinylidene fluorolide support 6 5.0 × 10 −11 30 [30] Imidazolium-based SILMs on porous hydrophilic polyethersulfone 610-1050 1.3 × 10 −9 to 2.3 × 10 −9 11-20 [8] that several aminopyridinium compounds are thermally stable to at least 550 K [17]. The option of dissolving one ionic liquid with a particular functionality in a bulk ionic liquid with well defined physical properties offers another avenue for obtaining membranes suitable for certain separations.…”
Section: Resultsmentioning
confidence: 99%
“…It is important to note that this result was obtained at extremely low CO 2 partial pressure of 5 kPa. In another study [22] the imidazolium cation was functionalized with fluoroalkyl groups to investigate the increase in gas solubility. The membranes showed CO 2 permeance of 4.9 × 10 −10 to 7.4 × 10 −10 mol m −2 s −1 Pa −1 and CO 2 /CH 4 selectivity in the range of 13-19.…”
Section: Resultsmentioning
confidence: 99%
“…From these results, it was proposed that IL-based adsorbents might provide a new approach to CO 2 removal from industrial gas streams [71]. Since then, a great deal of work has been performed on understanding the relationships between IL structure and CO 2 adsorption with the aim of enhancing CO 2 uptake [72][73][74][75][76][77][78][79][80][81][82][83].…”
Section: Structure and Propertiesmentioning
confidence: 99%
“…For example, a shortcoming of ammonia vaporisation [53] [54]. The research on fluoroalkyl-functionalised imidazolium-based solvent membranes revealed CO 2 permeabilities of 210-320 and selectivities of 16-27 (CO 2 /N 2 ) and 13-19 (CO 2 /CH 4 ) [55]. Unconventional IL-based solvent membrane tested in [56] showed selectivities 10-52 (CO 2 /N 2 ), 5-13 (CO 2 /H 2 ) and 5-23 (CO 2 /CH 4 ).…”
Section: Practical Examplesmentioning
confidence: 99%