Abstract
Practical application of microbial electrolysis cells (MECs) for hydrogen production requires scalable reactors with low internal resistance, high current density, and high hydrogen recovery. This work reports a liter scale tubular MEC approaching these requirements. The tubular cell components (a platinum-coated titanium mesh cathode, an anion exchange membrane, and a pleated stainless steel felt anode) were arranged in a concentric configuration. The reactor had a low internal resistance (0.325 Ω, 19.5 mΩ m2) due to the high conductivity of the electrodes, a compact reactor configuration, and proper mixing. With acetate as electron donor, the MEC achieved a volumetric current density of 654 ± 22 mA L−1 (projected current density, 1.09 ± 0.04 mA cm−2) and a volumetric hydrogen production rate of 7.10 ± 0.01 L L−1 d−1 at an applied voltage of 1 V. The reactor also showed high hydrogen recovery (∼100%), high hydrogen purity (>98%), and excellent operational stability during the 3 weeks of operation. These results demonstrated that high hydrogen production rate could be achieved on larger scale MEC and this tubular MEC holds great potential for scaling up.
| Original language | English |
|---|---|
| Pages (from-to) | 484-490 |
| Number of pages | 7 |
| Journal | Journal of Power Sources |
| Volume | 356 |
| DOIs | |
| State | Published - 2017 |
| Externally published | Yes |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
Keywords
- Hydrogen production
- Microbial electrolysis cells
- Reactor design
- Stainless steel felt
- Tubular reactor
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