Jan Vehrenberg , Georg Gert , Maren Grosseheide , Matthias Wessling , Robert Keller
{"title":"Paired electrochemical synthesis of Cl2 from alkali chloride and CO from CO2","authors":"Jan Vehrenberg , Georg Gert , Maren Grosseheide , Matthias Wessling , Robert Keller","doi":"10.1016/j.cep.2025.110209","DOIUrl":null,"url":null,"abstract":"<div><div>In order to bring electrochemical CO<sub>2</sub> reduction (eCO<sub>2</sub>R) to economical feasibility on an industrial scale, the conventional oxygen evolution reaction (OER) can be replaced with a value added reaction. In this work, we replace OER with chlorine evolution reaction (CER) in a paired synthesis with CO from CO<sub>2</sub>. Hereby, the reaction system is assessed at industrial relevant current densities with respect to electrolyte species & concentration and stability of up to 24 h. We report constant anodic FEs to Cl<sub>2</sub> of <span><math><mo>></mo></math></span>97<span><math><mtext>%</mtext></math></span> for up to 400 <span><math><mrow><mi>mA</mi><mo>/</mo><msup><mrow><mi>cm</mi></mrow><mrow><mn>2</mn></mrow></msup></mrow></math></span> with concurrent FEs to CO of 90<span><math><mtext>%</mtext></math></span> at 100 <span><math><mrow><mi>mA</mi><mo>/</mo><msup><mrow><mi>cm</mi></mrow><mrow><mn>2</mn></mrow></msup></mrow></math></span> and 74<span><math><mtext>%</mtext></math></span> at 200 <span><math><mrow><mi>mA</mi><mo>/</mo><msup><mrow><mi>cm</mi></mrow><mrow><mn>2</mn></mrow></msup></mrow></math></span> over 4.5 h, significantly exceeding previous studies for comparable systems. The FE for CER did not show any decline over 24 h of operation. KCl showed superior results over NaCl and CsCl in terms of cathodic FE and cell potential. CER is affected by educt limitation with FE dropping below 95<span><math><mtext>%</mtext></math></span> at an electrolyte concentration of 0.8 mol/L at 400 <span><math><mrow><mi>mA</mi><mo>/</mo><msup><mrow><mi>cm</mi></mrow><mrow><mn>2</mn></mrow></msup></mrow></math></span>. By successfully pairing eCO<sub>2</sub>R and CER with stable and high FEs at industrially relevant current densities, this work marks an important step towards an industrial application.</div></div>","PeriodicalId":9929,"journal":{"name":"Chemical Engineering and Processing - Process Intensification","volume":"211 ","pages":"Article 110209"},"PeriodicalIF":3.8000,"publicationDate":"2025-02-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical Engineering and Processing - Process Intensification","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S0255270125000583","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
引用次数: 0
Abstract
In order to bring electrochemical CO2 reduction (eCO2R) to economical feasibility on an industrial scale, the conventional oxygen evolution reaction (OER) can be replaced with a value added reaction. In this work, we replace OER with chlorine evolution reaction (CER) in a paired synthesis with CO from CO2. Hereby, the reaction system is assessed at industrial relevant current densities with respect to electrolyte species & concentration and stability of up to 24 h. We report constant anodic FEs to Cl2 of 97 for up to 400 with concurrent FEs to CO of 90 at 100 and 74 at 200 over 4.5 h, significantly exceeding previous studies for comparable systems. The FE for CER did not show any decline over 24 h of operation. KCl showed superior results over NaCl and CsCl in terms of cathodic FE and cell potential. CER is affected by educt limitation with FE dropping below 95 at an electrolyte concentration of 0.8 mol/L at 400 . By successfully pairing eCO2R and CER with stable and high FEs at industrially relevant current densities, this work marks an important step towards an industrial application.
期刊介绍:
Chemical Engineering and Processing: Process Intensification is intended for practicing researchers in industry and academia, working in the field of Process Engineering and related to the subject of Process Intensification.Articles published in the Journal demonstrate how novel discoveries, developments and theories in the field of Process Engineering and in particular Process Intensification may be used for analysis and design of innovative equipment and processing methods with substantially improved sustainability, efficiency and environmental performance.