4.8 Article

Hydrogen production with effluent from an ethanol-H2-coproducing fermentation reactor using a single-chamber microbial electrolysis cell

Journal

BIOSENSORS & BIOELECTRONICS
Volume 24, Issue 10, Pages 3055-3060

Publisher

ELSEVIER ADVANCED TECHNOLOGY
DOI: 10.1016/j.bios.2009.03.024

Keywords

Biohydrogen production; Microbial electrolysis cell (MEC); Effluent; Ethanol-type fermentation

Funding

  1. National Natural Science Foundation of China [30870037]
  2. National Renewable Energy Laboratory [RFH-7-77623-01]

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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. (C) 2009 Elsevier B.V. All rights reserved.

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