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电化学(中英文) ›› 2020, Vol. 26 ›› Issue (3): 359-369.  doi: 10.13208/j.electrochem.190305

• 研究论文 • 上一篇    下一篇

膜电极构型CO2还原电解单池的稳定性研究

毛庆1*(), 李冰玉1, 景维云1, 赵健1, 刘松2, 黄延强2*(), 杜兆龙3   

  1. 1. 大连理工大学化工学院,辽宁 大连 116023
    2. 中国科学院大连化学物理研究所,航天催化与新材料研究室,辽宁 大连 116023
    3. 全球能源互联网研究院,北京 102200
  • 收稿日期:2019-03-05 修回日期:2019-04-08 出版日期:2020-06-28 发布日期:2019-04-12
  • 通讯作者: 毛庆,黄延强 E-mail:maoqing@dlut.edu.cn;yqhuang@dicp.ac.cn
  • 基金资助:
    辽宁省自然科学基金项目(No. 201602162)、大连理工大学GF创新基金项目(No. DUT18GF308)和国家电网公司科技项目(No. SGRI-DL-71-16-015)资助

Stability Studies for a Membrane Electrode Assembly Type CO2 Electro-Reduction Electrolytic Cell

MAO Qing1*(), LI Bing-yu1, JING Wei-yun1, ZHAO Jian1, LIU Song2, HUANG Yan-qiang2*(), DU Zhao-long3   

  1. 1. School of Chemical Engineer, Dalian University of Technology, Dalian 116024, China
    2. Laboratory of Aerospace Catalysts and New Materials, Dalian Institute of Chemical Physics, Chinese Academy of Science, Dalian 116023, China
    3. Global Energy Interconnection Research Institute, Beijing 102200, China
  • Received:2019-03-05 Revised:2019-04-08 Published:2020-06-28 Online:2019-04-12
  • Contact: MAO Qing,HUANG Yan-qiang E-mail:maoqing@dlut.edu.cn;yqhuang@dicp.ac.cn

摘要:

电化学还原CO2可实现CO2的资源化转化,是缓解因其过度排放所导致诸多环境问题的关键技术. 本文提出了一种膜电极(membrane electrode assembly,MEA)构型CO2还原电解单池的结构设计,可同步实现气体扩散阴极两侧CO2的供给与电解质液层的更新. 基于该MEA构型电解池,实验考察了电解质液层中KHCO3浓度和更新与否对氮掺杂石墨烯锚定的Ni电极表面CO2电还原制备CO的反应活性、产物分布与稳定性的影响. 结果表明,若电流密度低于5 mA·cm-2,KHCO3浓度显著影响电解电势而非产物分布. CO2还原电解单池在稳定运行中存在着“可逆”与“不可逆”两种衰减模式. 其中,阴极/电解质界面处催化剂的流失是 “不可逆”衰减形成的原因;而电解质液层中KHCO3溶液的流失导致了MEA构型CO2还原单池的“可逆”衰减,周期性更新KHCO3电解质是降低其“可逆”衰减的有效方法.

关键词: 二氧化碳电还原, 膜电极, 电解池, 稳定性

Abstract:

Electro-catalytic reduction is an efficient way to achieve resourcable transformation of CO2, which is one of the important techniques to solve the global environmental problems originated from excessive CO2 emission. In this study, a membrane electrode assembly(MEA) type CO2 electro-reduction electrolytic cell was constucted, which enables CO2 feeding and real-time KHCO3 aqueous updating on both sides of the cathode gas diffusion electrode (GDE). By means of the electrolytic cell, effects of KHCO3 concentration and updating inside the liquid electrolytic chamber on CO2 electro-reduction activity, production distribution and stability were investigated. The experimental results suggested that the KHCO3 concentration exerted strong influence on the cell voltage rather than the production distribution for the current densities lower than 5 mA·cm-2. The performance of MEA type CO2 electro-reduction cell decayed in both “reversible” and “irreversible” ways. Catalysts leaking at the GDE/liquid electrolyte interface might be respossible for the cell “irreversible” decay. Meanwhile, th leakage of KHCO3 aqueous electrolyte arose from gas accumulation in the liquid electrolytic chamber contributed to the “reversible” degradation, which could be recovered effectively by updating the KHCO3 aqueous electrolyte.

Key words: CO2 electro-reduction, membrane electrode assembly, electrolytic cell, stability

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