Effectiveness of ionic liquid-supported membranes for carbon dioxide capture: a review

被引:0
作者
Tushar Patil
Swapnil Dharaskar
Manishkumar Sinha
Surendra Sasikumar Jampa
机构
[1] Pandit Deendayal Energy University,CO2 Research Group, Department of Chemical Engineering, School of Technology
来源
Environmental Science and Pollution Research | 2022年 / 29卷
关键词
Ionic liquids; Supported ionic liquid membranes; Gas separation; CO; capture;
D O I
暂无
中图分类号
学科分类号
摘要
The world’s population explosion creates a need for natural resources for energy, which will become a significant contributor to global climate change. As we all know, carbon dioxide (CO2) is one of the most critical elements of the global greenhouse gas effect. CO2 capture and storage innovations have piqued researchers’ attention in recent decades. Compared to other methods, membrane separation has some positive performance in CO2 capture. CO2 capture with membrane separation using enhanced ionic liquids (ILs) is described in this review. ILs have made an appearance in CO2 capture work as the potential additive, and companies and academics have been interested in CO2 separation for the past two decades. This article comprehensively analyzes the current modern approach in ILs and IL-based membranes for gas separation processes. Based on the latest literature and performance data, this work provides a complete compressive examination of types of ILs and IL-supported membrane performances. ILs for CO2 capture were also explored, and IL-based membranes for different ILs were also studied. This study emphasizes the supremacy of novel ILs for CO2 capture in membrane separation.
引用
收藏
页码:35723 / 35745
页数:22
相关论文
共 465 条
[1]  
Afshoun HR(2017)Effect of support layer on gas permeation properties of composite polymeric membranes Korean J Chem Eng 34 3178-3184
[2]  
Chenar MP(2017)Permeability and selectivity of acid gases in supported conventional and novel imidazolium-based ionic liquid membranes Sep Purif Technol 176 92-106
[3]  
Ismail AF(2014)Porous Al Sep Purif Technol 122 440-448
[4]  
Matsuura T(2018)O Fluid Phase Equilib 459 30-43
[5]  
Akhmetshina AI(2005)/TiO J Phys Chem B 109 6366-6374
[6]  
Gumerova OR(2002) tubes in combination with 1-ethyl-3-methylimidazolium acetate ionic liquid for CO J Phys Chem B 106 7315-7320
[7]  
Atlaskin AA(2019)/N J Mol Liq 275 71-83
[8]  
Albo J(2013) separation Int J Hydrogen Energy 38 9673-9687
[9]  
Yoshioka T(2004)Low viscosity protic ionic liquid for CO J Phys Chem B 108 721-727
[10]  
Tsuru T(2020)/CH J Energy Chem 46 30-52