Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
5746169 | Chemosphere | 2017 | 10 Pages |
â¢Potential of MEC to upgrade methanolic wastewater treatment in UASB reactor was evaluated.â¢Use of MEC improved methane production by around 10.1%.â¢Bioelectrochemical process reinforced EPS secretion and formation of [-Fe-EPS-]n matrix.â¢Bioelectrochemical process diversified microbial compositions and recycled wasted CO2.
The dispersion of granules in upflow anaerobic sludge blanket (UASB) reactor represents a critical technical issue in methanolic wastewater treatment. In this study, the potentials of coupling a microbial electrolysis cell (MEC) into an UASB reactor for improving methanolic wastewater biodegradation, long-term process stability and biomethane recovery were evaluated. The results indicated that coupling a MEC system was capable of improving the overall performance of UASB reactor for methanolic wastewater treatment. The combined system maintained the comparatively higher methane yield and COD removal efficiency over the single UASB process through the entire process, with the methane production at the steady-state conditions approaching 1504.7 ± 92.2 mL-CH4 Lâ1-reactor dâ1, around 10.1% higher than the control UASB (i.e. 1366.4 ± 71.0 mL-CH4 Lâ1-reactor dâ1). The further characterizations verified that the input of external power source could stimulate the metabolic activity of microbes and reinforced the EPS secretion. The produced EPS interacted with Fe2+/3+ liberated during anodic corrosion of iron electrode to create a gel-like three-dimensional [-Fe-EPS-]n matrix, which promoted cell-cell cohesion and maintained the structural integrity of granules. Further observations via SEM and FISH analysis demonstrated that the use of bioelectrochemical stimulation promoted the growth and proliferation of microorganisms, which diversified the degradation routes of methanol, convert the wasted CO2 into methane and accordingly increased the process stability and methane productivity.
Graphical abstractDownload high-res image (247KB)Download full-size image