Start-Up of an Anaerobic Moving Bed-Biofilm Reactor and Transition to Brewery Wastewater Treatment

被引:13
|
作者
di Biase, A. [1 ]
Devlin, T. R. [1 ]
Oleszkiewicz, J. A. [2 ]
机构
[1] Univ Manitoba, Dept Civil Engn, Winnipeg, MB R3T 5V6, Canada
[2] Univ Manitoba, Dept Civil Engn, Civil Engn, Winnipeg R3T 5V6, MB, Canada
关键词
Anaerobic moving bed-biofilm reactor; Mesophilic; Biogas production; Brewery wastewater; PERFORMANCE; TECHNOLOGY; DIGESTION;
D O I
10.1061/(ASCE)EE.1943-7870.0001146
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Two 4-L anaerobic moving bed-biofilm reactors (AMBBR) with different quantities of cubic media (25 and 35% by volume) were examined. Reactors were fed synthetic protein-based feed and both were shown to be capable of treating up to 20kg/m3day of chemical oxygen demand (COD), achieving 80% COD removal. Beyond that load the performance began to decrease. The maximum biogas production observed was 9.25m3CH4/m3day at an organic loading rate (OLR) of 20kgCOD/m3day. The methane composition varied between 60 and 70%. Averaged methane yields of 0.36 +/- 0.07m3CH4/kgCOD removed and specific removal rates from 0.4 to 20kgCOD/m3day were achieved. At the maximum OLR above 20kgCOD/m3day, the specific surface area activity was calculated as 98 and 75gCOD/m2day in the 25 and 35% reactors, respectively. Kinetic tests performed at the maximum OLR revealed that free-floating suspended biomass contributed to no more than 2.5% of the total removal. The reactors were also capable of treating brewery wastewater, reliably attaining 80% COD removal with methane yields of 0.36 +/- 0.06 and 0.39 +/- 0.03m3CH4/kgCOD from the 35 and 25% reactors, respectively. (C) 2016 American Society of Civil Engineers.
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页数:5
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