PEM水电解中具有竞争吸附的多物种离子交换模型

IF 3.9 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Sven Dörner , Johannes Paduch , Cathleen Plath , Matthias Wessling , Alexander Mitsos , Dominik Bongartz
{"title":"PEM水电解中具有竞争吸附的多物种离子交换模型","authors":"Sven Dörner ,&nbsp;Johannes Paduch ,&nbsp;Cathleen Plath ,&nbsp;Matthias Wessling ,&nbsp;Alexander Mitsos ,&nbsp;Dominik Bongartz","doi":"10.1016/j.cherd.2025.09.009","DOIUrl":null,"url":null,"abstract":"<div><div>To mitigate chemical membrane degradation in PEM water electrolyzers, ion exchange systems are typically implemented to remove iron ions from water. Predicting iron ion removal efficiency over time requires a model that captures interactions between the ion exchanger and electrolyzer, including the competitive adsorption of <figure><img></figure> and <figure><img></figure> ions. Building on the single-species model by Thomas (1944), we developed a multi-species ion exchange model by integrating a multi-species Langmuir model and introducing a competitive adsorption factor. Additionally, we coupled the model with an iron ion concentration source term accounting for ion production within the PEM electrolyzer. The model was fitted to new laboratory data by adjusting surface diffusivities. It successfully captures competitive adsorption dynamics, revealing transient peaks in <figure><img></figure> outlet concentrations compared to inlet concentrations due to displacement by <figure><img></figure> . For a specific case study, the model predicts that the ion exchange bed reaches exhaustion after approximately 10<!--> <!-->000<!--> <!-->h.</div></div>","PeriodicalId":10019,"journal":{"name":"Chemical Engineering Research & Design","volume":"222 ","pages":"Pages 325-339"},"PeriodicalIF":3.9000,"publicationDate":"2025-09-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Multi-species ion exchange model with competitive adsorption for iron removal in PEM water electrolysis\",\"authors\":\"Sven Dörner ,&nbsp;Johannes Paduch ,&nbsp;Cathleen Plath ,&nbsp;Matthias Wessling ,&nbsp;Alexander Mitsos ,&nbsp;Dominik Bongartz\",\"doi\":\"10.1016/j.cherd.2025.09.009\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>To mitigate chemical membrane degradation in PEM water electrolyzers, ion exchange systems are typically implemented to remove iron ions from water. Predicting iron ion removal efficiency over time requires a model that captures interactions between the ion exchanger and electrolyzer, including the competitive adsorption of <figure><img></figure> and <figure><img></figure> ions. Building on the single-species model by Thomas (1944), we developed a multi-species ion exchange model by integrating a multi-species Langmuir model and introducing a competitive adsorption factor. Additionally, we coupled the model with an iron ion concentration source term accounting for ion production within the PEM electrolyzer. The model was fitted to new laboratory data by adjusting surface diffusivities. It successfully captures competitive adsorption dynamics, revealing transient peaks in <figure><img></figure> outlet concentrations compared to inlet concentrations due to displacement by <figure><img></figure> . For a specific case study, the model predicts that the ion exchange bed reaches exhaustion after approximately 10<!--> <!-->000<!--> <!-->h.</div></div>\",\"PeriodicalId\":10019,\"journal\":{\"name\":\"Chemical Engineering Research & Design\",\"volume\":\"222 \",\"pages\":\"Pages 325-339\"},\"PeriodicalIF\":3.9000,\"publicationDate\":\"2025-09-13\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Chemical Engineering Research & Design\",\"FirstCategoryId\":\"5\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S0263876225004812\",\"RegionNum\":3,\"RegionCategory\":\"工程技术\",\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q2\",\"JCRName\":\"ENGINEERING, CHEMICAL\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering Research & Design","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0263876225004812","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0

摘要

为了减轻PEM水电解槽中化学膜的降解,通常采用离子交换系统去除水中的铁离子。随着时间的推移,预测铁离子去除效率需要一个模型来捕捉离子交换器和电解槽之间的相互作用,包括离子和离子的竞争性吸附。在Thomas(1944)的单物种模型的基础上,通过整合多物种Langmuir模型并引入竞争吸附因子,建立了多物种离子交换模型。此外,我们将模型与计算PEM电解槽内离子产生的铁离子浓度源项相耦合。通过调整表面扩散系数,该模型拟合了新的实验数据。它成功地捕获了竞争吸附动力学,揭示了与进口浓度相比,出口浓度的瞬态峰值。对于一个具体的案例研究,该模型预测离子交换床在大约10,000 h后达到耗尽。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Multi-species ion exchange model with competitive adsorption for iron removal in PEM water electrolysis

Multi-species ion exchange model with competitive adsorption for iron removal in PEM water electrolysis
To mitigate chemical membrane degradation in PEM water electrolyzers, ion exchange systems are typically implemented to remove iron ions from water. Predicting iron ion removal efficiency over time requires a model that captures interactions between the ion exchanger and electrolyzer, including the competitive adsorption of
and
ions. Building on the single-species model by Thomas (1944), we developed a multi-species ion exchange model by integrating a multi-species Langmuir model and introducing a competitive adsorption factor. Additionally, we coupled the model with an iron ion concentration source term accounting for ion production within the PEM electrolyzer. The model was fitted to new laboratory data by adjusting surface diffusivities. It successfully captures competitive adsorption dynamics, revealing transient peaks in
outlet concentrations compared to inlet concentrations due to displacement by
. For a specific case study, the model predicts that the ion exchange bed reaches exhaustion after approximately 10 000 h.
求助全文
通过发布文献求助,成功后即可免费获取论文全文。 去求助
来源期刊
Chemical Engineering Research & Design
Chemical Engineering Research & Design 工程技术-工程:化工
CiteScore
6.10
自引率
7.70%
发文量
623
审稿时长
42 days
期刊介绍: ChERD aims to be the principal international journal for publication of high quality, original papers in chemical engineering. Papers showing how research results can be used in chemical engineering design, and accounts of experimental or theoretical research work bringing new perspectives to established principles, highlighting unsolved problems or indicating directions for future research, are particularly welcome. Contributions that deal with new developments in plant or processes and that can be given quantitative expression are encouraged. The journal is especially interested in papers that extend the boundaries of traditional chemical engineering.
×
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
确定
请完成安全验证×
copy
已复制链接
快去分享给好友吧!
我知道了
右上角分享
点击右上角分享
0
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 布克学术 All rights reserved.
京ICP备2023020795号-1
ghs 京公网安备 11010802042870号
Book学术文献互助
Book学术文献互助群
群 号:604180095
Book学术官方微信