TY - JOUR
T1 - Electricity production from xylose in fed-batch and continuous-flow microbial fuel cells
AU - Huang, Liping
AU - Logan, Bruce E.
N1 - Funding Information:
Acknowledgments The authors would like to acknowledge David Jones and Elodie Lalaurette for sample analysis assistance. This research was supported by SRF for ROCS, SEM of China, Key Laboratory of Industrial Ecology and Environmental Engineering, Ministry of China Education, the National Renewable Energy Laboratory, and the Paul L. Busch Award administered by the Water Environment Research Foundation.
Copyright:
Copyright 2008 Elsevier B.V., All rights reserved.
PY - 2008/9
Y1 - 2008/9
N2 - A medium-scale (0.77 l) air-cathode, brush-anode microbial fuel cell (MFC) operated in fed-batch mode using xylose (20 mM) generated a maximum power density of 13±1 W/m3 (673±43 mW/m2). Xylose was rapidly removed (83.5%) within 8 h of a 60-h cycle, with 42.1% of electrons in intermediates (8.5±0.2 mM acetate, 5.9±0.01 mM ethanol, 4.3±0.1 mM formate, and 1.3±0.03 mM propionate), 9.1% captured as electricity, 16.1% in the remaining xylose, and 32.7% lost to cell storage, biomass, and other processes. The final Coulombic efficiency was 50%. At a higher initial xylose concentration (54 mM), xylose was again rapidly removed (86.9% within 24 h of a 116-h cycle), intermediates increased in concentration (18.4±0.4 mM acetate, 7.8±0.4 mM ethanol and 2.1±0.2 mM propionate), but power was lower (5.2±0.4 W/m3). Power was increased by operating the reactor in continuous flow mode at a hydraulic retention time of 20 h (20±1 W/m3), with 66±1% chemical oxygen demand removal. These results demonstrate that electricity generation is sustained over a cycle primarily by stored substrate and intermediates formed by fermentation and that the intermediates produced vary with xylose loading.
AB - A medium-scale (0.77 l) air-cathode, brush-anode microbial fuel cell (MFC) operated in fed-batch mode using xylose (20 mM) generated a maximum power density of 13±1 W/m3 (673±43 mW/m2). Xylose was rapidly removed (83.5%) within 8 h of a 60-h cycle, with 42.1% of electrons in intermediates (8.5±0.2 mM acetate, 5.9±0.01 mM ethanol, 4.3±0.1 mM formate, and 1.3±0.03 mM propionate), 9.1% captured as electricity, 16.1% in the remaining xylose, and 32.7% lost to cell storage, biomass, and other processes. The final Coulombic efficiency was 50%. At a higher initial xylose concentration (54 mM), xylose was again rapidly removed (86.9% within 24 h of a 116-h cycle), intermediates increased in concentration (18.4±0.4 mM acetate, 7.8±0.4 mM ethanol and 2.1±0.2 mM propionate), but power was lower (5.2±0.4 W/m3). Power was increased by operating the reactor in continuous flow mode at a hydraulic retention time of 20 h (20±1 W/m3), with 66±1% chemical oxygen demand removal. These results demonstrate that electricity generation is sustained over a cycle primarily by stored substrate and intermediates formed by fermentation and that the intermediates produced vary with xylose loading.
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U2 - 10.1007/s00253-008-1588-x
DO - 10.1007/s00253-008-1588-x
M3 - Article
C2 - 18626640
AN - SCOPUS:50849085152
SN - 0175-7598
VL - 80
SP - 655
EP - 664
JO - Applied Microbiology and Biotechnology
JF - Applied Microbiology and Biotechnology
IS - 4
ER -