Abstract
Microbial electrosynthesis (MES) offers a promising route for converting CO2 into value-added products, yet low energy efficiency remains a major obstacle, especially during scale-up. To address this issue, an up-scaled zero-gap MES reactor with an extended 30-cm flow path was developed and operated under a range of applied voltages to assess energy conversion and methane production performances. Increasing the cell voltage from 2.3 V to 2.7–2.8 V boosted the current density by 131%, reaching 17.5 A m-2. This improvement produced a corresponding rise in methane production from 1.4 to 6.9 L/L-d, achieving high coulombic efficiencies (>95%) and one of the highest energy efficiencies (45.2%) for methane synthesis at 30 °C. Simulations underscored the key role of hydrogen as the mediator of electron transfer, showing that sufficient in-situ hydrogen generation was essential for sustaining high methane production in the up-scaled reactor. Microbial community analysis revealed minimal spatial heterogeneity along the extended flow path, with the cathodic biofilms consistently dominated by hydrogenotrophic Methanobacterium (59.8% and 50.5% at the bottom and top), reflecting stable microbial functionality under scale-up conditions. Overall, the results demonstrate that with proper operational optimization, MES can be scaled up effectively without compromising energy efficiency or microbial–electrochemical synergy, offering a viable pathway for CO2-to-methane conversion in up-scaled systems.
| Original language | English (US) |
|---|---|
| Article number | 125723 |
| Journal | Water Research |
| Volume | 297 |
| DOIs | |
| State | Published - Jun 1 2026 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
All Science Journal Classification (ASJC) codes
- Environmental Engineering
- Civil and Structural Engineering
- Ecological Modeling
- Water Science and Technology
- Waste Management and Disposal
- Pollution
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