Composition and distribution of internal resistance in three types of microbial fuel cells

被引:174
作者
Liang, Peng
Huang, Xia [1 ]
Fan, Ming-Zhi
Cao, Xiao-Xin
Wang, Cheng
机构
[1] Tsinghua Univ, Dept Environm Sci & Engn, Environm Simulat & Pollut Control State Key Lab, Beijing 100084, Peoples R China
[2] Tsinghua Univ, Inst Nucl & New Energy Technol, Beijing 100084, Peoples R China
关键词
microbial fuel cell; internal resistance; flat-type;
D O I
10.1007/s00253-007-1193-4
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
High internal resistance is a key problem limiting the power output of the microbial fuel cell (MFC). Therefore, more knowledge about the internal resistance is essential to enhance the performance of the MFC. However, different methods are used to determine the internal resistance, which makes the comparison difficult. In this study, three different types of MFCs were constructed to study the composition and distribution of internal resistance. The internal resistance (R-i) is partitioned into anodic resistance (R-a), cathodic resistance (R-c), and ohmic resistance (R-ohm) according to their origin and the design of the MFCs. These three resistances were then evaluated by the "current interrupt" method and the "steady discharging" method based on the proposed equivalent circuits for MFCs. In MFC-A, MFC-B, and MFC-C, the R-i values were 3.17, 0.35, and 0.076 ohm m(2), the R-ohm values were 2.65, 0.085, and 0.008 ohm m(2), the R-a values were 0.055, 0.115, and 0.034 ohm m(2), and the R-c values were 0.466, 0.15, and 0.033 ohm m(2), respectively. For MFC-B and MFC-C, the remarkable decrease in R-i compared with the two-chamber MFC was mainly ascribed to the decline in R ohm and R-c. In MFC-C, the membrane electrodes' assembly lowered the ohmic resistance and facilitated the mass transport through the anode and cathode electrodes, resulting in the lowest R-i among the three types.
引用
收藏
页码:551 / 558
页数:8
相关论文
共 29 条
[1]   Continuous electricity generation at high voltages and currents using stacked microbial fuel cells [J].
Aelterman, Peter ;
Rabaey, Korneel ;
Pham, Hai The ;
Boon, Nico ;
Verstraete, Willy .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2006, 40 (10) :3388-3394
[2]   Effects of the cathode gas diffusion layer characteristics on the performance of polymer electrolyte fuel cells [J].
Antolini, E ;
Passos, RR ;
Ticianelli, EA .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 2002, 32 (04) :383-388
[3]   IN-SITU MEMBRANE RESISTANCE MEASUREMENTS IN POLYMER ELECTROLYTE FUEL-CELLS BY FAST AUXILIARY CURRENT PULSES [J].
BUCHI, FN ;
MAREK, A ;
SCHERER, GG .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1995, 142 (06) :1895-1901
[4]   Increased power generation in a continuous flow MFC with advective flow through the porous anode and reduced electrode spacing [J].
Cheng, S ;
Liu, H ;
Logan, BE .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2006, 40 (07) :2426-2432
[5]  
Guo JW, 2003, CHEM J CHINESE U, V24, P1477
[6]   An upflow microbial fuel cell with an interior cathode: Assessment of the internal resistance by impedance Spectroscopy [J].
He, Zhen ;
Wagner, Norbert ;
Minteer, Shelley D. ;
Angenent, Largus T. .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2006, 40 (17) :5212-5217
[7]   The role of potential-dependent electrolyte resistance in the performance, steady-state multiplicities and oscillations of PEM fuel cells: Experimental investigation and macroscopic modelling [J].
Katsaounis, A ;
Balomenou, SP ;
Tsiplakides, D ;
Tsampas, M ;
Vayenas, CG .
ELECTROCHIMICA ACTA, 2005, 50 (25-26) :5132-5143
[8]   Modelling and analysis of electrochemical, thermal, and reactant flow dynamics for a PEM fuel cell system [J].
Khan, MJ ;
Iqbal, MT .
FUEL CELLS, 2005, 5 (04) :463-475
[9]  
LARMINIE J, 2003, CELL SYSTEMS EXPLAIN, P62
[10]  
Liang Peng, 2007, Huanjing Kexue, V28, P1894