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Advanced methanogenic performance and fouling mechanism investigation of a high-solid anaerobic membrane bioreactor (AnMBR) for the co-digestion of food waste and sewage sludge
被引:57
作者:
Cheng, Hui
[1
]
Li, Yemei
[1
]
Guo, Guangze
[2
]
Zhang, Tao
[1
]
Qin, Yu
[1
]
Hao, Tianwei
[3
]
Li, Yu-You
[1
,2
]
机构:
[1] Tohoku Univ, Grad Sch Engn, Dept Civil & Environm Engn, 6-6-06 Aoba, Sendai, Miyagi 9808579, Japan
[2] Tohoku Univ, Grad Sch Environm Studies, Dept Frontier Sci Adv Environm, 6-6-20 Aoba, Sendai, Miyagi 9808579, Japan
[3] Univ Macau, Fac Sci & Technol, Dept Civil & Environm Engn, Macau, Peoples R China
来源:
基金:
日本学术振兴会;
关键词:
Sewage sludge;
Food waste;
Anaerobic co-digestion;
High-solid AnMBR;
Fouling mechanism;
BIOGAS PRODUCTION;
ACTIVATED-SLUDGE;
ENERGY-BALANCE;
PRETREATMENT;
WATER;
COSUBSTRATE;
EFFICIENCY;
D O I:
10.1016/j.watres.2020.116436
中图分类号:
X [环境科学、安全科学];
学科分类号:
08 ;
0830 ;
摘要:
Disposal of the increasingly huge amounts of sewage sludge (SeS) has become an impending problem worldwide. To solve this problem, a high-solid anaerobic membrane bioreactor (AnMBR) was used for the anaerobic co-digestion (AcoD) of SeS and food waste (FW). This study investigated the effects of SeS ratio on the methanogenic performance of the AcoD with a gradual increase value from 0 to 25%, 50%, 75% and 100% (total solids based). The results showed that the highest methanogenic performance was achieved at mono FW digestion. As for the co-digestion, the optimal FW/SeS ratio for methanogenic performance was 75%:25% among all the mixing ratios. The COD based biogas yield and methane yield were 0.498 L-biogas/g-CODfed and 0.295 L-CH4/g-CODfed at this optimal mixing ratio, which were 67.7% and 67.6% higher than those of the mono SeS digestion, respectively. The upgraded values were attributed to the improved hydrolysis ratio (by 8.14%) and the balanced carbon-to-nitrogen (C/N) ratio by co-digestion with FW, which synergistically stimulated methanogenesis ratio by 81.0%. The continuous membrane filtration property was investigated and four typical trans-membrane pressure (TMP) variation curves at different fouling degrees were determined. The membrane could sustainably operate at a flux of 6 L/m(2)/h (LMH) at the mixed liquor total solids (MLTS) concentration of 25 30 g/L. The combination of continuous membrane filtration property, particle size distribution of the mixed liquor and the external forces analysis was firstly applied to unravel the membrane fouling mechanism of a high-solid AnMBR. The result of this study will contribute to the establishment of an efficient FW and SeS treatment strategy. (c) 2020 Elsevier Ltd. All rights reserved.
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