Development of a submerged anaerobic membrane bioreactor for concurrent extraction of volatile fatty acids and biohydrogen production

被引:48
作者
Trad, Zaineb [1 ,2 ,3 ]
Akimbomi, Julius [4 ]
Vial, Christophe [2 ,3 ]
Larroche, Christian [2 ,3 ]
Taherzadeh, Mohammad J. [4 ]
Fontaine, Jean-Pierre [2 ,3 ]
机构
[1] Univ Clermont Ferrand, Univ Clermont Auvergne, LABEX IMobS3, F-63171 Clermont Ferrand, France
[2] Univ Clermont Ferrand, Univ Clermont Auvergne, Inst Pascal, F-63174 Aubiere, France
[3] CNRS, UMR 6602, F-63178 Aubiere, France
[4] Univ Boras, Swedish Ctr Resource Recovery, S-50190 Boras, Sweden
关键词
Anaerobic membrane bioreactor; Fouling; Submerged membrane; Volatile fatty acids; CONTINUOUS HYDROGEN-PRODUCTION; ORGANIC-ACIDS; ACTIVATED-SLUDGE; WASTE-WATER; FOOD WASTE; FILTRATION; RECOVERY; ELECTRODIALYSIS; MICROFILTRATION; FERMENTATION;
D O I
10.1016/j.biortech.2015.07.095
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The aim of this work was to study an externally-submerged membrane bioreactor for the cyclic extraction of volatile fatty acids (VFAs) during anaerobic fermentation, combining the advantages of submerged and external technologies for enhancing biohydrogen (BioH(2)) production from agrowaste. Mixing and transmembrane pressure (TMP) across a hollow fiber membrane placed in a recirculation loop coupled to a stirred tank were investigated, so that the loop did not significantly modify the hydrodynamic properties in the tank. The fouling mechanism, due to cake layer formation, was reversible. A cleaning procedure based on gas scouring and backwashing with the substrate was defined. Low TMP, 10(4) Pa, was required to achieve a 3 L h(-1) m(-2) critical flux. During fermentation, BioH(2) production was shown to restart after removing VFAs with the permeate, so as to enhance simultaneously BioH(2) production and the recovery of VFAs as platform molecules. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:290 / 300
页数:11
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