| Literature DB >> 24871275 |
Jung-Yeol Lee1, Jeonghee Yun, Tae Gwan Kim, Daehyun Wee, Kyung-Suk Cho.
Abstract
We evaluated the feasibility of co-digesting molasses wastewater and sewage sludge in a two-stage hydrogen- and methane-producing system. The highest energy was recovered at the 21-h hydraulic retention time (HRT) of the first hydrogenic reactor and at 56-h HRT of the secondary methanogenic reactor. Hence, the two-stage system recovered 1,822 kJ from 1 L of the mixed wastes (19.7: hydrogenic reactor plus, 1,802 kJ L(-1): methanogenic reactor). Despite the overloaded VFA-run with a short HRT of 56 h, the GAC-CH4 reactor increased methane production rate and yields due to enhanced pH buffer capacity. An RNA-based community analysis showed that the Ethanoligenens and Methanosaeta dominated the hydrogen and methane bioreactor, respectively. The two-stage system of co-digesting molasses and sewage sludge is particularly cost-effective due to non-pretreatment of sewage sludge.Entities:
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Year: 2014 PMID: 24871275 DOI: 10.1007/s00449-014-1217-2
Source DB: PubMed Journal: Bioprocess Biosyst Eng ISSN: 1615-7591 Impact factor: 3.210