TY - JOUR
T1 - Temperature effects on the methanogenesis enhancement and sulfidogenesis suppression in the UASB treatment of sulfate-rich methanol wastewater
AU - Wu, Jiang
AU - Liu, Quanli
AU - Feng, Bo
AU - Kong, Zhe
AU - Jiang, Bo
AU - Li, Yu You
N1 - Funding Information:
This study is acknowledged to financially supported by the Japan Society for the Promotion of Science (JSPS), File No. 17J00995 . The first author wants to thank the China Scholarship Council (CSC , No. 201608050003 ) for financial support.
Publisher Copyright:
© 2019
PY - 2019/8
Y1 - 2019/8
N2 - This study aims at investigating that the temperature effects on the overall organics removal capability and the reaction kinetic properties of methanogenesis/sulfidogenesis in anaerobic treatment of sulfate-rich methanol wastewater. A lab-scale upflow anaerobic sludge blanket (UASB) reactor was operated for 285 days treating sulfate-rich methanol wastewater at a temperature range of 17.5–50 °C. The COD/SO4 2− ratio of synthetic wastewater is 0.5. Experimental results indicate that both methanogens and sulfidogens showed lower metabolic activities at 17.5–25 °C. The average chemical oxygen demand (COD) removal efficiencies were higher than 90% at 40–50 °C. During these experimental periods, larger than 85% of influent COD was confirmed to be utilized for methanogenesis, revealing that methanogens prevailed over sulfidogens and dominated significantly in the COD utilization. In contrast, the sulfidogenesis-based COD utilization was effectively limited under the temperature range of 40–50 °C.
AB - This study aims at investigating that the temperature effects on the overall organics removal capability and the reaction kinetic properties of methanogenesis/sulfidogenesis in anaerobic treatment of sulfate-rich methanol wastewater. A lab-scale upflow anaerobic sludge blanket (UASB) reactor was operated for 285 days treating sulfate-rich methanol wastewater at a temperature range of 17.5–50 °C. The COD/SO4 2− ratio of synthetic wastewater is 0.5. Experimental results indicate that both methanogens and sulfidogens showed lower metabolic activities at 17.5–25 °C. The average chemical oxygen demand (COD) removal efficiencies were higher than 90% at 40–50 °C. During these experimental periods, larger than 85% of influent COD was confirmed to be utilized for methanogenesis, revealing that methanogens prevailed over sulfidogens and dominated significantly in the COD utilization. In contrast, the sulfidogenesis-based COD utilization was effectively limited under the temperature range of 40–50 °C.
KW - Methanogenesis enhancement
KW - Sulfate-rich methanol wastewater
KW - Sulfidogenesis suppression
KW - Temperature
KW - UASB reactor
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U2 - 10.1016/j.ibiod.2019.05.013
DO - 10.1016/j.ibiod.2019.05.013
M3 - Article
AN - SCOPUS:85066158271
SN - 0964-8305
VL - 142
SP - 182
EP - 190
JO - International Biodeterioration and Biodegradation
JF - International Biodeterioration and Biodegradation
ER -