Abstract:Poly(ionic liquid)-based thin film composite membranes capture carbon dioxide from mixed gas streams imitating flue gas separations under various process conditions.
“…However, their CO 2 /N 2 selectivity is less than 31 at 35 °C owing to the physical aging of the polymers. Nikolaeva et al . prepared thin PILMs with post‐modification of commercial polyvinylbenzyl chloride (PVBC) by employing a solvent casting method.…”
Section: Co2 Capture and Separation By Ionic Liquids‐based Membranesmentioning
confidence: 99%
“…However, their CO 2 /N 2 selectivity is less than 31 at 35°C owing to the physical aging of the polymers. Nikolaeva et al [66] prepared thin PILMs with post-modification of commercial polyvinylbenzyl chloride (PVBC) by employing a solvent casting method. (Figure 5a) They demonstrated that the intrinsic material properties of PILs was determined by ion asymmetry and the presence of polar alkyl groups.…”
Section: Ionic Liquid-derived Poly(ionic Liquid)s Based Membranes (Pimentioning
Ionic liquids (ILs) have gained wide‐spread focus owing to its negligible vapor pressure, low heat capacity, high thermal stability, and structural diversity. The solubility and selectivity toward carbon dioxide has made ILs a unique platform that possess the potential in gas separations. In particularly, combining functional ILs with membranes and porous supports is an efficient way to design task‐specific materials for CO2 separations. This minireview summarizes the developments and advances of ionic liquids‐based membranes for CO2 separations in recent three years, with an emphasis on the strategy of incorporating ionic liquids and CO2 separation performance.
“…However, their CO 2 /N 2 selectivity is less than 31 at 35 °C owing to the physical aging of the polymers. Nikolaeva et al . prepared thin PILMs with post‐modification of commercial polyvinylbenzyl chloride (PVBC) by employing a solvent casting method.…”
Section: Co2 Capture and Separation By Ionic Liquids‐based Membranesmentioning
confidence: 99%
“…However, their CO 2 /N 2 selectivity is less than 31 at 35°C owing to the physical aging of the polymers. Nikolaeva et al [66] prepared thin PILMs with post-modification of commercial polyvinylbenzyl chloride (PVBC) by employing a solvent casting method. (Figure 5a) They demonstrated that the intrinsic material properties of PILs was determined by ion asymmetry and the presence of polar alkyl groups.…”
Section: Ionic Liquid-derived Poly(ionic Liquid)s Based Membranes (Pimentioning
Ionic liquids (ILs) have gained wide‐spread focus owing to its negligible vapor pressure, low heat capacity, high thermal stability, and structural diversity. The solubility and selectivity toward carbon dioxide has made ILs a unique platform that possess the potential in gas separations. In particularly, combining functional ILs with membranes and porous supports is an efficient way to design task‐specific materials for CO2 separations. This minireview summarizes the developments and advances of ionic liquids‐based membranes for CO2 separations in recent three years, with an emphasis on the strategy of incorporating ionic liquids and CO2 separation performance.
“…[22] Poly(ionic liquids) (PILs), polymers derived from monomers basedo nI Ls,h ave also been investigated for CO 2 capturing. [23][24][25][26] PILs are ionically conductive and their CO 2 adsorption capacity is between 2a nd 20 mg g À1 ,which is higher than their IL counterparts. [2,[27][28][29][30][31] Managing carbon dioxide (CO 2 )r eleased from large-scale industrialp rocesses is of great importance,y et there remain significant technical challenges.H erein, the fabrication of 1mm-thicks olid-state electrochemical devices based on poly-(ionic liquid) ionogels with embedded electrodes capable of both adsorption and electrochemical reduction of CO 2 is reported.T he ionogelsa re prepared via radical polymerization and chemical crosslinking of avinyl imidazolium trifluoromethanesulfonimide ionic liquid monomer in the presence of additional ionic liquids (ILs) that act as swellinga gents and enhance ionic conductivity.…”
Section: Introductionmentioning
confidence: 96%
“…However, these systems can only operate at low pressures in order to prevent IL loss during the recovery and separation process . Poly(ionic liquids) (PILs), polymers derived from monomers based on ILs, have also been investigated for CO 2 capturing . PILs are ionically conductive and their CO 2 adsorption capacity is between 2 and 20 mg g −1 , which is higher than their IL counterparts …”
Managing carbon dioxide (CO2) released from large‐scale industrial processes is of great importance, yet there remain significant technical challenges. Herein, the fabrication of 1‐mm‐thick solid‐state electrochemical devices based on poly(ionic liquid) ionogels with embedded electrodes capable of both adsorption and electrochemical reduction of CO2 is reported. The ionogels are prepared via radical polymerization and chemical crosslinking of a vinyl imidazolium trifluoromethanesulfonimide ionic liquid monomer in the presence of additional ionic liquids (ILs) that act as swelling agents and enhance ionic conductivity. The effects of the ILs concentration and the degree of crosslinking on the mechanical properties, conductivity, and CO2 adsorption of the ionogels are investigated. The ionogels are shown to have ionic conductivities as high as 0.6 mS cm−1. The results of quartz crystal microbalance analyses demonstrates that the CO2 adsorption of the ionogels reaches up to ≈22 mg g−1, which is 10‐fold higher than that of their native ionic liquid. Moreover, the ionogels are easily recoverable after CO2 adsorption. The flexibility, conductivity, and CO2 capture capacity of this system can be controlled by the crosslinking ratio and ionic liquid content of the ionogels. This electrochemical device has the potential to be used in large scale plants for capturing CO2 for further electrochemical reactions.
“…The separation of carbon dioxide (CO 2 ) from other light gases is a process with considerable attention of researchers in industry and academia . Since membrane technology has several prominent properties such as low energy consumption, low capital investment, and simple operations, it is one of the well‐known energy‐efficient and economical techniques for gas separation applications . Separation through membranes is dominated by diffusivity and solubility of permeating materials in membranes.…”
In this study, the effects of the type and content of reactive diluents on the permeation/separation of carbon dioxide/nitrogen (CO 2 /N 2 ) through acrylate-terminated polyurethane (APU)-acrylate/acrylic diluent (APUA) composite membranes was investigated. A series of APUs based on poly(ethylene glycol) (PEG)-1000 g mol −1 , toluene diisocyanate, and 2-hydroxyethyl methacrylate was synthesized and then diluted with several reactive diluents. The results obtained from differential scanning calorimetry (DSC) and Fourier transform infrared analyses showed that the microphase interference of hard and soft segments increased with increasing reactive diluent content. Furthermore, with increasing alkene double bond of reactive diluents, the degree of phase separation increased, which might be due to the higher gel content of APUAs. APUAs were used as top selective layer on PS/PSF as the support layer to obtain composite membrane. Field emission scanning electron microscopy micrographs revealed that APUAs penetrated into the support layer, leading to strong interfacial adhesion between APUA and support layers. The gas permeation experiments indicated that the gas permeability decreased, while the CO 2 /N 2 selectivity increased with increasing reactive diluent content due to the enhancement of crosslinking density of APUAs. Moreover, the reactive diluent with high polarity, for example, acrylonitrile monomer, exhibited higher CO 2 /N 2 selectivity due to the improvement in solubility of CO 2 in APUA, while the permeability was retained compared with other reactive diluents. The thickness of APUA selective layer exhibited expectedly opposite effect on permeability and selectivity; however, the increment in selectivity is higher than the reduction in permeability when the thickness decreased from 50 to 10 μm.
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