2020
DOI: 10.1016/j.memsci.2019.117779
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Perfluorinated polymers as materials of membranes for gas and vapor separation

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Cited by 76 publications
(37 citation statements)
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“…As indicated by Park et al [ 83 ], all synthetic membranes exhibit a trade-off between permeability/conductivity (the rate of transfer of molecules and ions through a membrane material) and permselectivity (the ability to separate the target component from the feed solution): the higher membrane permeability, the lower permselectivity, and vice versa. For example, the well-known Robeson diagram illustrates this correlation for gas separation membranes [ 85 , 86 , 87 , 88 , 89 , 90 ].…”
Section: The Ion Exchange Membrane Structure and Ion Transfermentioning
confidence: 99%
“…As indicated by Park et al [ 83 ], all synthetic membranes exhibit a trade-off between permeability/conductivity (the rate of transfer of molecules and ions through a membrane material) and permselectivity (the ability to separate the target component from the feed solution): the higher membrane permeability, the lower permselectivity, and vice versa. For example, the well-known Robeson diagram illustrates this correlation for gas separation membranes [ 85 , 86 , 87 , 88 , 89 , 90 ].…”
Section: The Ion Exchange Membrane Structure and Ion Transfermentioning
confidence: 99%
“…Although polymeric membranes made of different commercial materials—e.g., polysulfone (PSF), polyethersulfone (PES), polyvinylidene fluoride (PVDF), polyamide (PA), polyimide (PI), and polybenzimidazole (PBI)—could be used for gas separation [ 9 , 10 , 11 ], most of them still suffer from the trade-off limitation between permeability and selectivity [ 12 , 13 ]. In order to address this problem, researchers always come up with new strategies to modify existing polymer-based membranes, aiming to overcome their limitations.…”
Section: Introductionmentioning
confidence: 99%
“…[1][2][3][4][5][6] Besides that, they are meaningful candidates for the real-world separation membranes as they remain stable [7,8] up to the temperatures relevant for the industrial membrane separations (100-150 C [9] ). Moreover, the PFIE membranes can undergo ion-exchange reactions: the gas permeation [7,8,[10][11][12][13][14][15] and pervaporation [16][17][18][19] characteristics were shown to depend strongly on the actual counter ion. Generally, membrane separations could reuse the regenerated PFIE membranes after their service in the chlor-alkali industry, which would prolong their service time and thus postpone their ecologically problematic disposal.…”
Section: Introductionmentioning
confidence: 99%