Abstract
Microbial electrosynthesis (MES) is a promising technology for CO2 utilization and renewable electricity storage. The practical application of MES requires high current density and scalable reactor design. Here, we reported a novel 20 L electrochemical continuous stirred-tank reactor (E-CSTR) for methane production from CO2. The E-CSTR was constructed by inserting a tubular electrochemical cell into a CSTR. At 4 A (119.94 A·m−2), the average and maximum methane production rates achieved in the reactor were 317.84 L·m−2·d−1 (0.53 L·L−1·d−1) and 407.8 L·m−2·d−1 (0.68 L·L−1·d−1), respectively, and the average coulombic efficiency was about 98%. The reactor outperformed most reported MES reactors. Increasing the current to 6 A resulted in a deterioration of the performance because O2 across the membrane changed the microbial community composition. However, the reactor quickly recovered when the current was switched back to 4 A, which indicated the excellent robustness of the reactor. These results demonstrated that the E-CSTR holds great potential for scaling up and practical application.
| Original language | English |
|---|---|
| Article number | 138898 |
| Journal | Chemical Engineering Journal |
| Volume | 451 |
| DOIs | |
| State | Published - 1 Jan 2023 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
Keywords
- Electrochemical CSTR
- H-mediated electron transfer
- Methane production
- Microbial electrosynthesis
- Reactor scaling up
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