Increasing power recovery and organic removal efficiency using extended longitudinal tubular microbial fuel cell (MFC) reactors

被引:47
作者
Kim, Jung Rae [1 ]
Rodriguez, Jorge [2 ,3 ]
Hawkes, Freda R. [2 ]
Dinsdale, Richard M. [2 ]
Guwy, Alan J. [2 ]
Premier, Giuliano C. [1 ]
机构
[1] Univ Glamorgan, SERC, Fac Adv Technol, Pontypridd CF37 1DL, M Glam, Wales
[2] Univ Glamorgan, SERC, Fac Hlth Sport & Sci, Pontypridd CF37 1DL, M Glam, Wales
[3] Univ Santiago de Compostela, Dept Chem Engn, Santiago De Compostela 15782, Spain
基金
英国工程与自然科学研究理事会;
关键词
ELECTRICITY-GENERATION; STACK; CATHODE;
D O I
10.1039/c0ee00073f
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The power recovery and COD removal efficiency, which depend on organic influent loading rate, have been studied in a high aspect ratio longitudinal tubular MFC reactor (liquid volume, 1 L). The power output from four anode/cathode pairs (modules) along the MFC's length was compared in two different modes of electrical connection (i.e. independently connected and connected in parallel to the loads). Independent connection to resistive loads for each of the four modules produced higher total maximum power generation than parallel connection (6% higher at 0.8 g l(-1)/d and 36% higher at 0.08 g l(-1)/d). The cumulative power production lengthwise along the reactor modules increased to 2.6 mW in the two higher OLRs tested (0.8 and 0.38 g l(-1)/d). However, at lower OLRs, the power tended to saturate at a lower level due to reduced organic concentrations in the later modules. Step perturbation of organic influent concentration from 960 to 22 mg sucrose l(-1) resulted in a delayed voltage decrease, probably due to storage effects in the biofilm on the anode electrode. The power recovery and organic removal could be maximized by extending the number of modules in the longitudinal tubular reactor, which could control effluent quality and power yield, thus facilitating scale-up.
引用
收藏
页码:459 / 465
页数:7
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