Performance of submerged anaerobic membrane bioreactor for thermomechanical pulping wastewater treatment

被引:19
|
作者
Gao, W. J. [1 ]
Han, M. N. [1 ]
Xu, Chunbao [2 ]
Liao, B. Q. [1 ]
Hong, Y. [3 ]
Cumin, J. [3 ]
Dagnew, M. [3 ]
机构
[1] Lakehead Univ, Dept Chem Engn, 955 Oliver Rd, Thunder Bay, ON P7B 5E1, Canada
[2] Univ Western Ontario, Dept Chem & Biochem Engn, London, ON N6A 5B9, Canada
[3] GE Water & Proc Technol, Oakville, ON L6M 4B2, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Anaerobic membrane bioreactor; Hollow fiber membrane; Membrane fouling; Biogas sparging rate; Pulp and paper effluent;
D O I
10.1016/j.jwpe.2016.05.004
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A hollow fiber submerged anaerobic membrane bioreactor (SAnMBR) was operated for 160 days for thermo-mechanicalal pulping pressate treatment. A COD removal efficiency of 83 +/- 4% was achieved under all tested conditions, although the residual COD in permeate increased slightly with an increase in influent COD. The biogas yield slightly decreased with a higher feed concentration. The EPS production increased with an increase in organic loading rate. Membrane performance was affected by both the influent COD concentration and biogas sparging rate. The fouling layer samples were characterized using various analytical tools. The results suggest that it is feasible and attractive to treat thermomechanical pulping wastewater by a hollow fiber SAnMBR. Cake layer formation was the dominant mechanism of membrane fouling. An increase in biogas sparging rate actively mitigated the accumulation and deposition of sludge on/in membrane module, thus favored the enhancement of membrane flux and an efficient long-term operation. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:70 / 78
页数:9
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