Upflow anaerobic sludge blanket-hollow centered packed bed (UASB-HCPB) reactor for thermophilic palm oil mill effluent (POME) treatment

被引:40
作者
Poh, P. E. [1 ,2 ]
Chong, M. P. [1 ]
机构
[1] Univ Nottingham, Fac Engn, Dept Chem & Environm Engn, Semenyih 43500, Selangor DE, Malaysia
[2] Monash Univ Malaysia, Sch Engn, Chem Engn Discipline, Semenyih 46150, Selangor DE, Malaysia
关键词
Anaerobic digestion; Bioreactors; Wastewater treatment; Bioremediation; Palm oil mill effluent; Biogas; WASTE-WATER TREATMENT; START-UP; TREATMENT SYSTEMS; LOADING RATE; DIGESTION; TEMPERATURE; GRANULATION; BIOREACTORS; METHANE; FILTER;
D O I
10.1016/j.biombioe.2014.05.007
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Upflow anaerobic sludge blanket-hollow centered packed bed (UASB-HCPB) reactor was developed with the aim to minimize operational problems in the anaerobic treatment of Palm Oil Mill Effluent (POME) under thermophilic conditions. The performance of UASB-HCPB reactor on POME treatment was investigated at 55 degrees C. Subsequent to start-up, the performance of the UASB-HCPB reactor was evaluated in terms of i) effect of hydraulic retention time (HRT); effect of organic loading rate (OLR); and effect of mixed liquor volatile suspended solid (MLVSS) concentration on thermophffic POME treatment. Start-up up of the UASB-HCPB reactor was completed in 36 days, removing 88% COD and 90% BOD respectively at an OLR of 28.12 g L-1 d(-1), producing biogas with 52% of methane. Results from the performance study of the UASB-HCPB reactor on thermophilic POME treatment indicated that HRT of 2 days, OLR of 27.65 g L-2 el and MLVSS concentration of 14.7 g was required to remove 90% of COD and BOD, 80% of suspended solid and at the same time produce 60% of methane. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:231 / 242
页数:12
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