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CO2 capture with room temperature ionic liquids; coupled absorption/desorption and single module absorption in membrane contactor

机译:CO2捕获室温离子液体; 膜接触器中的耦合吸收/解吸和单模块吸收

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A membrane gas CO2 capture setup, based on the concept of single module absorption and single cycle coupled absorption/desorption, was developed in this work. Ionic liquids (ILs) 1-ethyl-3-methylimidazolium methylsulfate ([emim][MS]) and 1-ethyl-3-methylimidazolium dicyanamide ([emim][DCA]) were used as absorbents. The CO2 absorption rate decreased initially and reached to a nearly constant value achieving pseudo steady state. Coupled absorption/desorption revealed very high performance by retaining 82% and 66% absorption efficiency, for [emim][MS] and [emim][DCA], respectively, even after 70 min of operation. Mass transfer coefficients of the coupled absorption/desorption at pseudo steady state were 9 and 5 folds higher than single module absorption, for [emim] [MS] and [emim] [DCA], respectively. Parametric analysis for the membrane absorber outlet concentration and optimization of the parameters to achieve zero concentration at the membrane stripper outlet were studied in simulations. As a conclusion, coupled absorption/desorption in combination with ILs, can be considered very suitable for continuous post-combustion carbon capture. (C) 2020 Elsevier Ltd. All rights reserved.
机译:基于单模块吸收和单循环耦合/解吸的概念,在这项工作中开发了一种膜气体CO2捕获设置。将离子液体(ILS)1-乙基-3-甲基咪唑鎓甲基硫酸盐([emim] [MS])和1-乙基-3-甲基咪唑二氰胺([emim] [DCA])用作吸收剂。二氧化碳吸收率最初降低,并达到实现伪稳态的几乎恒定值。偶联的吸收/解吸甚至在70分钟后,均可通过保留82%和66%的吸收效率,分别为[emim] [ms]和[emim] [dca]。对于伪稳态的耦合吸收/解吸的传质系数分别比单个模块吸收的9和5倍,分别用于[emim] [MS]和[emim] [DCA]。在模拟中研究了对膜吸收出口浓度和参数的优化参数的参数分析。作为结论,可以考虑与ILS组合的偶联吸收/解吸,非常适合于连续的燃烧后碳捕获。 (c)2020 elestvier有限公司保留所有权利。

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