Treatment of thin stillage in a high-rate anaerobic fluidized bed bioreactor (AFBR)

被引:42
|
作者
Andalib, Mehran [1 ]
Hafez, Hishann [2 ]
Elbeshbishy, Elsayed [3 ]
Nakhla, George [1 ,3 ]
Zhu, Jesse [1 ]
机构
[1] Univ Western Ontario, Dept Chem & Biochem Engn, London, ON N6A 5B9, Canada
[2] GreenField Ethanol Inc, Chatham, ON N7M 5J4, Canada
[3] Univ Western Ontario, Dept Civil & Environm Engn, London, ON N6A 5B9, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Thin stillage; High rate anaerobic digester; Fluidized bed bioreactor; Suspended solids; TEXTILE WASTE-WATER; BIOLOGICAL TREATMENT; PERFORMANCE EVALUATION; SEQUENTIAL TREATMENT; REACTOR; DIGESTION; INDUSTRY; ACID; REMOVAL; SYSTEM;
D O I
10.1016/j.biortech.2012.07.008
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The primary objective of this work was to investigate the treatability of thin stillage as a by-product of bioethanol production plants using an anaerobic fluidized bed bioreactor (AFBR) employing zeolite with average diameter of (d(m)) of 425-610 mu m and specific surface area (SSA) of 26.5 m(2)/g as the carrier media. Despite the very high strength of thin stillage with chemical oxygen demand of 130,000 mg TCOD/L and suspended solids of 47,000 mg TSS/L, the AFBR showed up to 88% TCOD and 78% TSS removal at very high organic and solids loading rates (OLR and SLR) of 29 kg COD/m(3) d and 10.5 kg TSS/m(3) d respectively and hydraulic retention time (HRT) of 3.5 days. Methane production rates of up to 160 L/d at the steady state equivalent to 40 L-CH4/L-thin stillge d and biogas production rate per reactor volume of 15.8 L-gas/L-reactor d were achieved. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:411 / 418
页数:8
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