Use of silicone membranes to enhance gas transfer during microbial fuel cell operation on carbon monoxide

被引:10
作者
Hussain, A. [1 ,2 ]
Tartakovsky, B. [2 ]
Guiot, S. R. [2 ]
Raghavan, V. [1 ]
机构
[1] McGill Univ, Dept Bioresource Engn, Ste Anne De Bellevue, PQ H9X 3V9, Canada
[2] Natl Res Council Canada, Biotechnol Res Inst, Montreal, PQ H2P 2R2, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Microbial fuel cell; Carbon monoxide; Silicone membrane; Gas transfer; SYNGAS FERMENTATION; MASS-TRANSFER; ELECTRICITY; REACTOR; OPPORTUNITIES; TECHNOLOGY; CHALLENGES; CONVERSION; AERATION; BIOMASS;
D O I
10.1016/j.biortech.2011.09.057
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Electricity generation in a microbial fuel cell (MFC) using carbon monoxide (CO) or synthesis gas (syngas) as a carbon source has been demonstrated recently. A major challenge associated with CO or syngas utilization is the mass transfer limitation of these sparingly soluble gases in the aqueous phase. This study evaluated the applicability of a dense polymer silicone membrane and thin wall silicone tubing for CO mass transfer in MFCs. Replacing the sparger used in our previous study with the membrane systems for CO delivery resulted in improved MFC performance and CO transformation efficiency. A power output and CO transformation efficiency of up to 18 mW L-R(-1) (normalized to anode compartment volume) and 98%, respectively, was obtained. The use of membrane systems offers the advantage of improved mass transfer and reduced reactor volume, thus increasing the volumetric power output of MFCs operating on a gaseous substrate such as (C). 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:10898 / 10906
页数:9
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