4.7 Article

Simultaneous coproduction of hydrogen and methane from sugary wastewater by an ACSTRH-UASBMet system

Journal

INTERNATIONAL JOURNAL OF HYDROGEN ENERGY
Volume 38, Issue 19, Pages 7774-7779

Publisher

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.ijhydene.2013.04.065

Keywords

Sugary wastewater; Two-phase anaerobic fermentation process; Hydrogen production rate; Methane production rate; Bioenergy recovery

Funding

  1. Ministry of Environmental Protection, China [200909043]

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A two-phase ACSTR(H)-UASB(Met) system has been investigated at the stepwise decreased HRT for the simultaneous production of hydrogen and methane in this study. Hydrogen could be continuously produced from the two-phase hydrogen fermentation of sugary wastewater in ACSTR and effluents from hydrogen fermentation were converted into methane in UASB reactor. At optimum conditions (HRTH: 5 h, HRTMet: 15 h), the highest hydrogen production rate of 5.69 (+/- 0.06) mmol L-1 h(-1) was obtained from sugary wastewater and methane was continuously produced from effluents of hydrogen fermentation with a production rate of 3.74 (+/- 0.13) mmol L-1 h(-1). The total bioenergy recovery by coproduction of hydrogen and methane from sugary wastewater reached 19.37 W and a total of 92.41% of substrate was converted to the biogas (hydrogen and methane) with twophase anaerobic fermentation. Copyright (C) 2013, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.

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