Sandip Kumar De, Dong-Il Won, Jeongwon Kim and Dong Ha Kim
{"title":"集成二氧化碳捕获和电化学升级:基础机制和技术-化学分析†","authors":"Sandip Kumar De, Dong-Il Won, Jeongwon Kim and Dong Ha Kim","doi":"10.1039/D2CS00512C","DOIUrl":null,"url":null,"abstract":"<p >Coupling post-combustion CO<small><sub>2</sub></small> capture with electrochemical utilization (CCU) is a quantum leap in renewable energy science since it eliminates the cost and energy involved in the transport and storage of CO<small><sub>2</sub></small>. However, the major challenges involved in industrial scale implementation are selecting an appropriate solvent/electrolyte for CO<small><sub>2</sub></small> capture, modeling an appropriate infrastructure by coupling an electrolyser with a CO<small><sub>2</sub></small> point source and a separator to isolate CO<small><sub>2</sub></small> reduction reaction (CO<small><sub>2</sub></small>RR) products, and finally selection of an appropriate electrocatalyst. In this review, we highlight the major difficulties with detailed mechanistic interpretation in each step, to find out the underpinning mechanism involved in the integration of electrochemical CCU to achieve higher-value products. In the past decades, most of the studies dealt with individual parts of the integration process, <em>i.e.</em>, either selecting a solvent for CO<small><sub>2</sub></small> capture, designing an electrocatalyst, or choosing an ideal electrolyte. In this context, it is important to note that solvents such as monoethanolamine, bicarbonate, and ionic liquids are often used as electrolytes in CO<small><sub>2</sub></small> capture media. Therefore, it is essential to fabricate a cost-effective electrolyser that should function as a reversible binder with CO<small><sub>2</sub></small> and an electron pool capable of recovering the solvent to electrolyte reversibly. For example, reversible ionic liquids, which are non-ionic in their normal forms, but produce ionic forms after CO<small><sub>2</sub></small> capture, can be further reverted back to their original non-ionic forms after CO<small><sub>2</sub></small> release with almost 100% efficiency through the chemical or thermal modulations. This review also sheds light on a focused techno-economic evolution for converting the electrochemically integrated CCU process from a pilot-scale project to industrial-scale implementation. In brief, this review article will summarize a state-of-the-art argumentation of challenges and outcomes over the different segments involved in electrochemically integrated CCU to stimulate urgent progress in the field.</p>","PeriodicalId":68,"journal":{"name":"Chemical Society Reviews","volume":" 16","pages":" 5744-5802"},"PeriodicalIF":39.0000,"publicationDate":"2023-08-04","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"1","resultStr":"{\"title\":\"Integrated CO2 capture and electrochemical upgradation: the underpinning mechanism and techno-chemical analysis†\",\"authors\":\"Sandip Kumar De, Dong-Il Won, Jeongwon Kim and Dong Ha Kim\",\"doi\":\"10.1039/D2CS00512C\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<p >Coupling post-combustion CO<small><sub>2</sub></small> capture with electrochemical utilization (CCU) is a quantum leap in renewable energy science since it eliminates the cost and energy involved in the transport and storage of CO<small><sub>2</sub></small>. However, the major challenges involved in industrial scale implementation are selecting an appropriate solvent/electrolyte for CO<small><sub>2</sub></small> capture, modeling an appropriate infrastructure by coupling an electrolyser with a CO<small><sub>2</sub></small> point source and a separator to isolate CO<small><sub>2</sub></small> reduction reaction (CO<small><sub>2</sub></small>RR) products, and finally selection of an appropriate electrocatalyst. In this review, we highlight the major difficulties with detailed mechanistic interpretation in each step, to find out the underpinning mechanism involved in the integration of electrochemical CCU to achieve higher-value products. In the past decades, most of the studies dealt with individual parts of the integration process, <em>i.e.</em>, either selecting a solvent for CO<small><sub>2</sub></small> capture, designing an electrocatalyst, or choosing an ideal electrolyte. In this context, it is important to note that solvents such as monoethanolamine, bicarbonate, and ionic liquids are often used as electrolytes in CO<small><sub>2</sub></small> capture media. Therefore, it is essential to fabricate a cost-effective electrolyser that should function as a reversible binder with CO<small><sub>2</sub></small> and an electron pool capable of recovering the solvent to electrolyte reversibly. For example, reversible ionic liquids, which are non-ionic in their normal forms, but produce ionic forms after CO<small><sub>2</sub></small> capture, can be further reverted back to their original non-ionic forms after CO<small><sub>2</sub></small> release with almost 100% efficiency through the chemical or thermal modulations. This review also sheds light on a focused techno-economic evolution for converting the electrochemically integrated CCU process from a pilot-scale project to industrial-scale implementation. 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Integrated CO2 capture and electrochemical upgradation: the underpinning mechanism and techno-chemical analysis†
Coupling post-combustion CO2 capture with electrochemical utilization (CCU) is a quantum leap in renewable energy science since it eliminates the cost and energy involved in the transport and storage of CO2. However, the major challenges involved in industrial scale implementation are selecting an appropriate solvent/electrolyte for CO2 capture, modeling an appropriate infrastructure by coupling an electrolyser with a CO2 point source and a separator to isolate CO2 reduction reaction (CO2RR) products, and finally selection of an appropriate electrocatalyst. In this review, we highlight the major difficulties with detailed mechanistic interpretation in each step, to find out the underpinning mechanism involved in the integration of electrochemical CCU to achieve higher-value products. In the past decades, most of the studies dealt with individual parts of the integration process, i.e., either selecting a solvent for CO2 capture, designing an electrocatalyst, or choosing an ideal electrolyte. In this context, it is important to note that solvents such as monoethanolamine, bicarbonate, and ionic liquids are often used as electrolytes in CO2 capture media. Therefore, it is essential to fabricate a cost-effective electrolyser that should function as a reversible binder with CO2 and an electron pool capable of recovering the solvent to electrolyte reversibly. For example, reversible ionic liquids, which are non-ionic in their normal forms, but produce ionic forms after CO2 capture, can be further reverted back to their original non-ionic forms after CO2 release with almost 100% efficiency through the chemical or thermal modulations. This review also sheds light on a focused techno-economic evolution for converting the electrochemically integrated CCU process from a pilot-scale project to industrial-scale implementation. In brief, this review article will summarize a state-of-the-art argumentation of challenges and outcomes over the different segments involved in electrochemically integrated CCU to stimulate urgent progress in the field.
期刊介绍:
Chemical Society Reviews is published by: Royal Society of Chemistry.
Focus: Review articles on topics of current interest in chemistry;
Predecessors: Quarterly Reviews, Chemical Society (1947–1971);
Current title: Since 1971;
Impact factor: 60.615 (2021);
Themed issues: Occasional themed issues on new and emerging areas of research in the chemical sciences