Abstract
A combined anaerobic digestion (AD) and microbial electrolysis cell (MEC) system, named here as ADMEC, was investigated to evaluate the energy recovery from pretreated wastewater solids. Alkaline and thermal hydrolysis pretreatment methods increased the solubility of organic compounds present in the raw solids by 25% and 20%, respectively. The soluble phase from pretreatment was separated and used for microbial electrolysis, whereas the insoluble fraction was fed into semi-continuous digesters. The digester effluent was also later fed into the MECs separately. The pretreatment had variable effects on AD and MEC performance. The methane content in AD biogas was higher in pretreated groups, 78.29 ± 2.89% and 73.2 ± 1.79%, for alkaline and thermal, than the control, 50.26 ± 0.53%, but the overall biogas production rates were lower than the control, 20 and 30 mL CH4/gCOD*d for alkaline and thermal compared to 80 mL CH4/gCOD*d. The effluent streams from thermally pretreated digesters were the best substrate for microbial electrolysis, in terms of hydrogen production and efficiency. These MECs produced 1.7 ± 0.2 L- H2/L-day, 0.3 ± 0.1 L- H2/L-day, and 0.29 ± 0.1 L- H2//L-day, for thermal, alkaline, and control reactors. The productivity was lower compared to acetate and propionate controls, which yielded 5.79 ± 0.03 L- H2/L-day and 3.49 ± 0.10 L- H2/L-day, respectively. The PT solubilized fractions were not ideal substrates for microbial electrolysis. A chemical oxygen demand (COD) mass balance showed that pretreatment shifts the electron flux away from methane and biomass sinks towards hydrogen production.