Computational investigation on the effect of [Bmim][BF4] ionic liquid addition to MEA alkanolamine absorbent for enhancing CO2 mass transfer inside membranes

被引:37
|
作者
Pishnamazi, Mahboubeh [1 ,2 ,3 ]
Nakhjiri, Ali Taghvaie [4 ]
Taleghani, Arezoo Sodagar [4 ]
Marjani, Azam [5 ]
Heydarinasab, Amir [4 ]
Shirazian, Saeed [6 ,7 ]
机构
[1] Duy Tan Univ, Inst Res & Dev, Da Nang 550000, Vietnam
[2] Duy Tan Univ, Fac Pharm, Da Nang 550000, Vietnam
[3] Univ Limerick, Bernal Inst, Dept Chem Sci, Limerick, Ireland
[4] Islamic Azad Univ, Dept Petr & Chem Engn, Sci & Res Branch, Tehran, Iran
[5] Islamic Azad Univ, Dept Chem, Arak Branch, Arak, Iran
[6] Ton Duc Thang Univ, Dept Management Sci & Technol Dev, Ho Chi Minh City, Vietnam
[7] Ton Duc Thang Univ, Fac Appl Sci, Ho Chi Minh City, Vietnam
关键词
Bmim][BF4] ionic liquid; Mass transfer; CO2; removal; CFD simulation; Mathematical modeling; CARBON-DIOXIDE ABSORPTION; FLUE-GAS; SIMULTANEOUS REMOVAL; CAPTURE; SIMULATION; SEPARATION; CONTACTOR; KINETICS; MONOETHANOLAMINE;
D O I
10.1016/j.molliq.2020.113635
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Nowadays, various types of liquid solutions have been applied to remove acidic contaminants such as CO2 with the aim of mitigating their pernicious emission to atmosphere. Ionic liquids are recently of tremendous attention as promising solutions for CO2 molecular removal from disparate gaseous mixtures due to their superior characteristics such as regeneration simplicity, low volatility and negligible environmental toxicity. The main objective of this paper is to mathematically implement a model based on finite element approach (FEA) to analyze the governing mass and momentum partial differential equations inside the domains of polytetrafluoroethylene-co-perfluorinated alkyl vinyl ether membrane contactor (PFAMC). Also, a computational fluid dynamics (CFD) simulation is carried out to analyze the CO2 molecular removal percentage using MEA absorbent and a mixed solution containing 30% 1-butyl-3-methylimidazolium tetrafluoroborate ([Bmim][BF4]) ionic liquid and 70% MEA amine solution. The results show that although MEA has been able to remove only 18% of CO2 from the inlet gas, the addition of 30% [Bmim][BF4] ionic liquid to MEA significantly improved the CO2 mass transfer performance and consequently its removal efficiency to 79%. Study on the effect of some operational parameters such as inlet feed gas flow rate, packing density and number of hollow fibers on removing the CO2 molecules is another objective of this paper. (C) 2020 Elsevier B.V. All rights reserved.
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页数:8
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