4.7 Article

An electrolytic-hydrogen-fed moving bed biofilm reactor for efficient microbial electrosynthesis of methane from CO2

期刊

CHEMICAL ENGINEERING JOURNAL
卷 428, 期 -, 页码 -

出版社

ELSEVIER SCIENCE SA
DOI: 10.1016/j.cej.2021.132093

关键词

Microbial electrosynthesis; MBBR; Electrolytic hydrogen; Methane; Mass transfer

资金

  1. National Natural Science Founda-tion of China [22008194, 21878242]
  2. Natural Science of Shaanxi [2020JM-042]
  3. China Postdoctoral Science Foundation [2020 M673414]
  4. Fundamental Research Funds for the Central Uni-versities [xzy012020025]

向作者/读者索取更多资源

A novel electrolytic-hydrogen-fed moving bed biofilm reactor (electroMBBR) for methane production was developed to address the challenge of ensuring high coulombic efficiency under high current density in hydrogen-mediated MES reactors. The reactor achieved a maximum methane production rate of 1.42 L/day at 5 A, demonstrating the potential for scaling up and practical application of this technology. The microbial community analysis revealed Methanobrevibacter as the dominant methane-producing archaea in the reactor.
Microbial electrosynthesis (MES) is an emerging technology for CO2 fixation and renewable energy storage. Currently, the low current density hinders the practical application of this technology. In situ coupling of electrochemical hydrogen production, and hydrogen gas fermentation has been proposed as a promising way to enhance the current density of MES. However, due to the low solubility of hydrogen, how to ensure a high coulombic efficiency (i.e. hydrogen utilization efficiency) under high current density is the main challenge for this type of reactor. Here, we report a novel electrolytic-hydrogen-fed moving bed biofilm reactor (electroMBBR) reactor for methane production. The reactor consists of an electrochemical cell at the bottom and an MBBR column at the top. The MBBR column prolongs the retention time of the electrolytically-produced hydrogen and enhances the mass transfer of hydrogen. Consequently, the methanogens in the reactor could efficiently convert the electrolytically-produced hydrogen and the externally-supplied CO2 into methane. The 4.5 L reactor achieved a maximum methane production rate of 1.42 L center dot L-1 center dot d-1 (141.5 L center dot m- 2cat center dot d- 1) at 5 A (111.1 A center dot m- 2cat). The CH4 production rate is more than two times higher than the maximum reported value based on biofilm-driven MES (0.54 L center dot L-1 center dot d-1, 65 L center dot m- 2cat center dot d-1). Microbial community analysis showed that the Methanobrevibacter was the dominant methane-producing archaea. These results demonstrated under high current density high coulombic efficiency could be achieved if proper hydrogen retention time and good hydrogen mass transfer were ensured in hydrogen-mediated MES reactors. The electro-MBBR appears to be a promising MES setup for scaling up and practical application.

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