Conceptual design and evaluation of membrane gas separation-based CO2 recovery unit for CO2 electrolyzers employing anion exchange membranes

IF 4.6 3区 工程技术 Q2 ENERGY & FUELS International Journal of Greenhouse Gas Control Pub Date : 2024-11-02 DOI:10.1016/j.ijggc.2024.104278
Hyunshin Lee , Wonsuk Chung , Kosan Roh
{"title":"Conceptual design and evaluation of membrane gas separation-based CO2 recovery unit for CO2 electrolyzers employing anion exchange membranes","authors":"Hyunshin Lee ,&nbsp;Wonsuk Chung ,&nbsp;Kosan Roh","doi":"10.1016/j.ijggc.2024.104278","DOIUrl":null,"url":null,"abstract":"<div><div>Anion exchange membrane (AEM)-based electrolysis for CO<sub>2</sub> reduction reaction (CO<sub>2</sub>RR) 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 CO<sub>2</sub>RR is CO<sub>2</sub> crossover, which leads to the loss of introduced CO<sub>2</sub> feedstock and thus detrimentally affects the process's overall economic and environmental viability. We design a 3-stage membrane-based CO<sub>2</sub> recovery unit to capture CO<sub>2</sub> from the mixture of CO<sub>2</sub> and O<sub>2</sub> discharged from the anode side of AEM-based CO<sub>2</sub> electrolyzers. The membrane area is optimized via a hybrid of genetic algorithm and ‘fmincon’ in MATLAB. The estimated CO<sub>2</sub> capture cost ranges from 43.3 to 109.3 USD/tCO<sub>2</sub>, which is economically comparable to piperazine-based amine scrubbing units when recovering CO<sub>2</sub> at a purity of up to 99.5 mol.% under a CO<sub>2</sub>/O<sub>2</sub> molar ratio of 1.5∼2. The carbon footprint of the designed process ranges from −0.936 to −0.838 tCO<sub>2</sub>eq/tCO<sub>2</sub>-captured, indicating superior environmental performance compared to those of the piperazine-based amine scrubbing units.</div></div>","PeriodicalId":334,"journal":{"name":"International Journal of Greenhouse Gas Control","volume":"139 ","pages":"Article 104278"},"PeriodicalIF":4.6000,"publicationDate":"2024-11-02","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"International Journal of Greenhouse Gas Control","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S1750583624002214","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
引用次数: 0

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 O2 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/tCO2, 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/O2 molar ratio of 1.5∼2. The carbon footprint of the designed process ranges from −0.936 to −0.838 tCO2eq/tCO2-captured, indicating superior environmental performance compared to those of the piperazine-based amine scrubbing units.
查看原文
分享 分享
微信好友 朋友圈 QQ好友 复制链接
本刊更多论文
采用阴离子交换膜的二氧化碳电解器基于膜气体分离的二氧化碳回收装置的概念设计和评估
基于阴离子交换膜(AEM)的二氧化碳还原反应(CO2RR)电解技术因其在高电流密度下的卓越能效而备受关注,被视为一种前景广阔的二氧化碳利用技术。基于 AEM 的二氧化碳还原反应电解技术的主要缺点是二氧化碳交叉,这会导致引入的二氧化碳原料的损失,从而对该工艺的整体经济和环境可行性产生不利影响。我们设计了一种基于膜的 3 级二氧化碳回收装置,用于从基于 AEM 的二氧化碳电解槽阳极侧排出的二氧化碳和氧气混合物中捕获二氧化碳。膜面积通过 MATLAB 中的遗传算法和 "fmincon "混合算法进行优化。估计的二氧化碳捕获成本为 43.3 至 109.3 美元/吨二氧化碳,在二氧化碳/氧气摩尔比为 1.5∼2 的条件下,回收纯度高达 99.5 mol.% 的二氧化碳时,其经济效益与基于哌嗪的胺洗涤装置相当。所设计工艺的碳足迹范围为-0.936 至 -0.838 tCO2eq/tCO2-captured,表明与哌嗪基胺洗涤装置相比,该工艺具有更优越的环保性能。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
求助全文
约1分钟内获得全文 去求助
来源期刊
CiteScore
9.20
自引率
10.30%
发文量
199
审稿时长
4.8 months
期刊介绍: The International Journal of Greenhouse Gas Control is a peer reviewed journal focusing on scientific and engineering developments in greenhouse gas control through capture and storage at large stationary emitters in the power sector and in other major resource, manufacturing and production industries. The Journal covers all greenhouse gas emissions within the power and industrial sectors, and comprises both technical and non-technical related literature in one volume. Original research, review and comments papers are included.
期刊最新文献
Putting the genie back in the bottle: Decarbonizing petroleum with direct air capture and enhanced oil recovery A conceptual evaluation of the use of Ca(OH)2 for attaining carbon capture rates of 99% in the calcium looping process Determining the dominant factors controlling mineralization in three-dimensional fracture networks Conceptual design and evaluation of membrane gas separation-based CO2 recovery unit for CO2 electrolyzers employing anion exchange membranes Enhanced cation release via acid pretreatment for gigaton-scale geologic CO2 sequestration in basalt
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
现在去查看 取消
×
提示
确定
0
微信
客服QQ
Book学术公众号 扫码关注我们
反馈
×
意见反馈
请填写您的意见或建议
请填写您的手机或邮箱
已复制链接
已复制链接
快去分享给好友吧!
我知道了
×
扫码分享
扫码分享
Book学术官方微信
Book学术文献互助
Book学术文献互助群
群 号:481959085
Book学术
文献互助 智能选刊 最新文献 互助须知 联系我们:info@booksci.cn
Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。
Copyright © 2023 Book学术 All rights reserved.
ghs 京公网安备 11010802042870号 京ICP备2023020795号-1