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Updated: Jun 23, 2026

Evaluation of Integrated Anaerobic Digestion and Hydrothermal Carbonization for Bioenergy Production
Published on: June 15, 2014
Continuous H2 and CH4 production from high-solid food waste in the two-stage thermophilic fermentation process with
Dong-Yeol Lee1, Yoshitaka Ebie, Kai-Qin Xu
1Research Center for Material Cycles and Waste Management, National Institute for Environmental Studies, 16-2 Onogawa, Tsukuba, Japan. lee.dongyeol@nies.go.jp
Abstract:
A thermophilic two-stage fermentation process using 10% total solids (TS) food waste was tested at varying organic loading rates (OLRs). The system was configured to produce H(2) and CH(4) in conjugation with the chemical oxygen demand (COD), nitrogen removal, and adjustment of the pH by returning sludge as an alkali buffer from the sludge storage tank for denitrification. The pH in the H(2) fermentation reactor was maintained in the range of 5.4-5.7 using sludge recirculation (Q(r)/Q(i) ratio 1). The average H(2) (11.1l-H(2) l(-1)-fed d(-1)) and CH(4) (47.4l-CH(4) l(-1)-fed d(-1)) production rates were achieved at OLRs of 39 (H(2) fermentation reactor) and 4.16 gCOD l(-1)d(-1) (CH(4) fermentation reactor), respectively. These results suggest that long-term stability of the continuous two-stage process can be successfully achieved by recirculation of high-alkalinity sludge of 6.7-7.5 g l(-1) as CaCO(3), without any added external chemical buffer.
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