Hydrogen production with effluent from an ethanol–H 2-coproducing fermentation reactor using a single-chamber microbial electrolysis cell

Abstract

Hydrogen can be produced by bacterial fermentation of sugars, but substrate conversion to hydrogen is incomplete. Using a single-chamber microbial electrolysis cell (MEC), we show that additional hydrogen can be produced from the effluent of an ethanol-type dark-fermentation reactor. An overall hydrogen recovery of 83 ± 4% was obtained using a buffered effluent (pH 6.7–7.0), with a hydrogen production rate of 1.41 ± 0.08 m 3 H 2/m 3 reactor/d, at an applied voltage of E ap = 0.6 V. When the MEC was combined with the fermentation system, the overall hydrogen recovery was 96%, with a production rate of 2.11 m 3 H 2/m 3/d, corresponding to an electrical energy efficiency of 287%. High cathodic hydrogen recoveries (70 ± 5% to 94 ± 4%) were obtained at applied voltages of 0.5–0.8 V due to shorter cycle times, and repression of methanogen growth through exposure of the cathode to air after each cycle. Addition of a buffer to the fermentation effluent was critical to MEC performance as there was little hydrogen production using unbuffered effluent (0.0372 m 3 H 2/m 3/d at E ap = 0.6 V, pH 4.5–4.6). These results demonstrate that hydrogen yields from fermentation can be substantially increased by using MECs.