Catalytic carbon dioxide absorption and stripping using nanofibrous membrane contactors

被引:0
作者
Kim, Seungju [1 ]
Momeni, Arash [2 ]
Alivand, Masood S. [2 ]
Bolne, Pravin C. [2 ]
Mumford, Kathryn A. [2 ]
Kentish, Sandra E. [2 ]
机构
[1] RMIT Univ, Sch Engn, Dept Chem & Environm Engn, Melbourne, Vic 3000, Australia
[2] Univ Melbourne, Dept Chem Engn, Parkville, Vic 3010, Australia
基金
澳大利亚研究理事会;
关键词
Catalytic regeneration; Electrospinning; Membrane gas-solvent contactor; CO2; capture; absorption; stripping; SOLVENT REGENERATION; CO2; ABSORPTION; CAPTURE; THERMODYNAMICS; SORPTION; SULFATE; MCM-41;
D O I
10.1016/j.seppur.2025.133079
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Catalyst-assisted CO2 capture processes are developed using membrane gas-solvent contactors. While chemical absorption-based capture methods are among the most practical for CO2 capture, they are generally regarded as energy-intensive, particularly for the regeneration of CO2-rich solvents. Herein, we propose catalytic membrane-based CO2 absorption and desorption processes which significantly lower the solvent regeneration temperature and offer additional CO2 sorption sites within mesoporous MCM-41 based catalysts. The incorporation of membrane gas-solvent contactors with hydrophobic polymer nanofibres enhances CO2 transfer by creating a larger mass transfer area. The resulting catalytic CO2 capture process, incorporating 1.0 wt% of SO42-/MCM-41 nanocatalysts in 5 M monoethanolamine (MEA) solution and Thermally Rearranged polymer (TR-PBOI) nano-fibre membranes, demonstrates 23.5mmol m-2 s-1 of CO2 absorption flux at 50 degrees C and 32.6mmol m-2 s-1 of CO2 desorption flux at 90 degrees C, presenting a catalytic enhancement of 150 %.
引用
收藏
页数:11
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