Fermentative hydrogen production in an up-flow anaerobic biofilm reactor inoculated with a co-culture of Clostridium acetobutylicum and Desulfovibrio vulgaris

被引:36
作者
Barca, Cristian [1 ]
Ranava, David [2 ]
Bauzan, Marielle [3 ]
Ferrasse, Jean-Henry [1 ]
Giudici-Orticoni, Marie-Therese [2 ]
Soric, Audrey [1 ,2 ]
机构
[1] Aix Marseille Univ, CNRS, Cent Marseille, M2P2, Marseille, France
[2] Aix Marseille Univ, CNRS, BIP, Marseille, France
[3] Aix Marseille Univ, CNRS, IMM, Marseille, France
关键词
Anaerobic metabolism; Scale-up; Packed bed bioreactors; Microbial consortium; Bioprocess design; Biogas; PACKED-BED BIOREACTORS; BIOHYDROGEN PRODUCTION; FLUIDIZED-BED; DOMINANT BACTERIA; DARK FERMENTATION; H-2; PRODUCTION; GLUCOSE; SLUDGE; COMMUNITIES;
D O I
10.1016/j.biortech.2016.09.072
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Dark fermentation systems often show low H-2 yields and unstable H-2 production, as the result of the variability of microbial dynamics and metabolic pathways. Recent batch investigations have demonstrated that an artificial consortium of two anaerobic bacteria, Clostridium acetobutylicum and Desulfovibrio vulgaris Hildenborough, may redirect metabolic fluxes and improve H-2 yields. This study aimed at evaluating the scale-up from batch to continuous H-2 production in an up-flow anaerobic packed-bed reactor (APBR) continuously fed with a glucose-medium. The effects of various parameters, including void hydraulic retention time (HRTv), pH, and alkalinity, on H-2 production performances and metabolic pathways were investigated. The results demonstrated that a stable H-2 production was reached after 3-4 days of operation. H-2 production rates increased significantly with decreasing HRTv from 4 to 2 h. Instead, H-2 yields remained almost stable despite the change in HRTv, indicating that the decrease in HRTv did not affect the global metabolism. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:526 / 533
页数:8
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