Article ID Journal Published Year Pages File Type
7718974 International Journal of Hydrogen Energy 2014 12 Pages PDF
Abstract
The aim of this study was to promote biohydrogen production in an thermophilic anaerobic fluidized bed reactor (AFBR) at 55 °C using a mixture of sugar cane stillage and glucose at approximately 5000-5300 mg COD L−1. During a reduction in the hydraulic retention time (HRT) from 8, 6, 4, 2 and 1 h, H2 yields of 5.73 mmol g CODadded−1 were achieved (at HRT of 4 h, with organic loading rate of 52.7 kg COD m−3 d−1). The maximum volumetric H2 production of 0.78 L H2 h−1 L−1 was achieved using stillage as carbon source. In all operational phases, the H2 average content in the biogas was between 31.4 and 52.0%. Butyric fermentation was the predominant metabolic pathway. The microbial community in accordance with the DGGE bands profile was found similarity coefficient between 91 and 95% without significant changes in bacterial populations after co-substrate removal. Bacteria like Thermoanaerobacterium sp. and Clostridium sp. were identified.
Related Topics
Physical Sciences and Engineering Chemistry Electrochemistry
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