Abstract
A tubular Microbial Fuel Cell (MFC) reactor consisting of four modules (total reactor volume of 1 l) was fed with food processing washdown water as a chemical oxygen demand (COD) removal process to decrease effluent pollution levels and discharge costs. Two different operational modes were tested: (A) Under static electrical loads with substrate circulated to and from different storage vessels and (B) employing maximum peak power point tracking (MPPT) whilst re-circulating substrate through a single storage vessel. After 7 cycles through the reactor, notionally equivalent to 28 concatenated tubular MFC modules, 84% of the soluble COD (960 mg l−1) was removed from the effluent in Mode A and 70% (800 mg l−1) in Mode B with MPPT. In the study, acetic acid was consumed first and propionic acid increased initially before depletion after 7 cycles, showing that higher carbohydrates were degraded during the effluent polishing process.
Original language | English |
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Pages (from-to) | 210-217 |
Number of pages | 8 |
Journal | Biochemical Engineering Journal |
Volume | 117 |
Issue number | Part A |
Early online date | 22 Oct 2016 |
DOIs | |
Publication status | Published - 15 Jan 2017 |
Keywords
- Anaerobic processes
- Biodegradation
- COD removal
- Microbial Fuel Cell (MFC)
- Scale-up
- Waste-water treatment
ASJC Scopus subject areas
- Biotechnology
- Bioengineering
- Environmental Engineering
- Biomedical Engineering