| Literature DB >> 23360705 |
Takashi Onodera1, Shinya Sase, Pairaya Choeisai, Wilasinee Yoochatchaval, Haruhiko Sumino, Takashi Yamaguchi, Yoshitaka Ebie, Kaiqin Xu, Noriko Tomioka, Motoyuki Mizuochi, Kazuaki Syutsubo.
Abstract
This study evaluated the process performance of a novel treatment system consisting of an acidification reactor, an upflow staged sludge bed (USSB) reactor, an upflow anaerobic sludge blanket reactor, and an aerobic trickling filter for the treatment of a high-strength molasses wastewater with a chemical oxygen demand (COD) of up to 120,000mg/L. The USSB operating at 35°C was capable of achieving an organic loading rate of 11kgCOD/m(3) day with a methane recovery of 62.4% at an influent COD of 120,000mg/L. The final effluent COD was 4520mg/L. The system was effective with regard to nitrification and sulfur removal. Fifty percent inhibition of the bacterial activity of the retained sludge by the cations was determined at 8gK/L for sucrose degradation, 16gK/L for sulfate reduction, and 12gK/L or 9gNa/L for acetoclastic methane production. Cation inhibition of anaerobic degradation reduced the process performance of the USSB.Entities:
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Year: 2013 PMID: 23360705 DOI: 10.1016/j.biortech.2012.12.126
Source DB: PubMed Journal: Bioresour Technol ISSN: 0960-8524 Impact factor: 9.642