Sulfides generated from sulfate reduction commonly act as inhibitors in anaerobic digestion (AD). This study examined the performance of three configurations of microbial electrolysis cell-assisted anaerobic digestion (MEC-AD) systems: single-chamber, dual-chamber with an anion exchange membrane (AEM), and dual-chamber with a cation exchange membrane (CEM), operated under sulfate-reducing conditions. In general, the single-chamber MEC-AD reactors exhibited significantly higher methane yields (74.5–75.0%) than the control (64.4%). Upon converting a single-chamber MEC-AD to a dual-chamber configuration using an AEM, methane yield further increased up to 80.6%. The membrane facilitated the transfer of buffer anions to the anode and sulfate to the cathode, which substantially reduced un-ionized sulfide concentrations in the anode chamber. The MEC-AD with an AEM also demonstrated increased specific methanogenic activities, current densities, and microbial diversity with the enrichment of electroactive bacteria (e.g., Geobacter, Aeromonas) and hydrogenotrophic Methanobacterium. However, the MEC-AD reactor with a CEM experienced a significant reduction in methane yield (63.2%), mainly due to anolyte acidification, which increased the un-ionized sulfide concentrations.
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Huang et al. (2024) studied this question.
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