Conceptual design and evaluation of membrane gas separation-based CO2 recovery unit for CO2 electrolyzers employing anion exchange membranes
- Authors
- Lee, Hyunshin; Chung, Wonsuk; Roh, Kosan
- Issue Date
- 2024-12
- Publisher
- Elsevier BV
- Citation
- International Journal of Greenhouse Gas Control, v.139
- Abstract
- Anion exchange membrane (AEM)-based electrolysis for CO2 reduction reaction (CO2RR) has garnered attention as a promising carbon dioxide utilization technology due to its superior energy efficiency at high current densities. The major drawback of AEM-based electrolysis for CO2RR is CO2 crossover, which leads to the loss of introduced CO2 feedstock and thus detrimentally affects the process's overall economic and environmental viability. We design a 3-stage membrane-based CO2 recovery unit to capture CO2 from the mixture of CO2 and O-2 discharged from the anode side of AEM-based CO2 electrolyzers. The membrane area is optimized via a hybrid of genetic algorithm and 'fmincon' in MATLAB. The estimated CO2 capture cost ranges from 43.3 to 109.3 USD/tCO(2), which is economically comparable to piperazine-based amine scrubbing units when recovering CO2 at a purity of up to 99.5 mol.% under a CO2/O-2 molar ratio of 1.5 similar to 2. The carbon footprint of the designed process ranges from -0.936 to -0.838 tCO(2)eq/tCO(2)-captured, indicating superior environmental performance compared to those of the piperazine-based amine scrubbing units.
- Keywords
- DIFFUSION ELECTRODE; CARBON-DIOXIDE; REDUCTION; CAPTURE; SIMULATION; REMOVAL; CO 2 RR; Anion exchange membrane; Membrane gas separation; Amine scrubbing; CO 2 crossover; Process design and evaluation
- ISSN
- 1750-5836
- URI
- https://pubs.kist.re.kr/handle/201004/151206
- DOI
- 10.1016/j.ijggc.2024.104278
- Appears in Collections:
- KIST Article > 2024
- Files in This Item:
There are no files associated with this item.
- Export
- RIS (EndNote)
- XLS (Excel)
- XML
Items in DSpace are protected by copyright, with all rights reserved, unless otherwise indicated.