Abstract
The H2-mediated microbial electrosynthesis (MES) reactors can be run in high current density, but it is challenging to ensure high Coulombic efficiency (CE) due to the limited hydrogen solubility. Here, we introduce a unique electrolytic bubble column featuring gas recirculation to tackle the challenge. The bubble column and gas recirculation extended the H2 retention time and enhanced gas-liquid mixing in the reactor, thereby ensuring a high H2 uptake efficiency. When a current density of 337 A/m2cathode (1.2 A/Lcatholyte) was applied, the reactor achieved an average acetate production rate of 87 g/m2cathode/d (2 g/Lcatholyte/d), an acetate titer of 15.6 g/L, and an H2 uptake efficiency of 87%, which significantly exceeded the reported H2-mediated MES reactors. In addition, the reactor size of 6 L was about 10 times larger than that of previously reported MES reactors. The results indicate that this reactor design is promising for large-scale MES applications.
| Original language | English |
|---|---|
| Pages (from-to) | 16616-16621 |
| Number of pages | 6 |
| Journal | Industrial and Engineering Chemistry Research |
| Volume | 62 |
| Issue number | 41 |
| DOIs | |
| State | Published - 18 Oct 2023 |
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