The Relationship between Shunt Currents and Edge Corrosion in Flow Batteries

被引:42
作者
Darling, Robert M. [1 ,2 ]
Shiau, Huai-Suen [3 ]
Weber, Adam Z. [3 ]
Perry, Mike L. [2 ]
机构
[1] Joint Ctr Energy Storage Res, Argonne, IL 60439 USA
[2] United Technol Res Ctr, E Hartford, CT 06108 USA
[3] Lawrence Berkeley Natl Lab, Berkeley, CA 94720 USA
关键词
CELL; MODEL; ELECTRODE; LEAKAGE; STACKS; SYSTEM; PERFORMANCE; EFFICIENCY;
D O I
10.1149/2.0081711jes
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
Shunt currents occur in electrochemical reactors like flow batteries, electrolyzers, and fuel cells where many bipolar cells that are connected in series electrically contact a mobile electrolyte through one or more common fluid distribution manifolds. Shunt currents reduce energy efficiency, and can cause unwanted side reactions including corrosion and gas generation. Equivalent-circuit models have been widely used to examine shunt currents in multi-cell electrochemical reactors. However, a detailed investigation of the interesting electrochemical processes occurring at the edges of the active areas has not been presented. In this work, the generation of shunt currents and their tendency to drive corrosion at the edges of positive electrodes in the most positive cells in a reactor stack are investigated with a comprehensive numerical model. An analytical model based on the penetration of current into a semi-infinite electrode, that can be used in conjunction with traditional equivalent-circuit models to assess the tendency for shunt currents to drive corrosion, is developed and compared to the numerical model. The models provided here can be used to set requirements on maximum allowable port currents in order to achieve a particular durability goal. (C) The Author(s) 2017. Published by ECS. All rights reserved.
引用
收藏
页码:E3081 / E3091
页数:11
相关论文
共 30 条
[1]   Analysis of shunt currents and associated corrosion of bipolar plates in PEM fuel cells [J].
Bennett, William R. ;
Hoberecht, Mark A. ;
Lvovich, Vadim F. .
JOURNAL OF ELECTROANALYTICAL CHEMISTRY, 2015, 737 :162-173
[2]   Comparative analysis for various redox flow batteries chemistries using a cost performance model [J].
Crawford, Alasdair ;
Viswanathan, Vilayanur ;
Stephenson, David ;
Wang, Wei ;
Thomsen, Edwin ;
Reed, David ;
Li, Bin ;
Balducci, Patrick ;
Kintner-Meyer, Michael ;
Sprenkle, Vincent .
JOURNAL OF POWER SOURCES, 2015, 293 :388-399
[3]   The Influence of Electrode and Channel Configurations on Flow Battery Performance [J].
Darling, Robert M. ;
Perry, Mike L. .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2014, 161 (09) :A1381-A1387
[4]  
DELTOMBE E, 1974, ATLAS ELECTROCHEMICA, P234
[5]  
Dimoault-Darcy E. C., 1988, J ELECTROCHEM SOC, V135, P656
[6]   POTENTIAL DISTRIBUTION AND ELECTRODE STABILITY IN A BIPOLAR ELECTROLYSIS CELL [J].
DIVISEK, J ;
JUNG, R ;
BRITZ, D .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 1990, 20 (02) :186-195
[7]   Simplified model to predict the effect of the leakage current on primary and secondary current distributions in electrochemical reactors with a bipolar electrode [J].
Henquín, ER ;
Bisang, JM .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 2005, 35 (12) :1183-1190
[8]   A TECHNIQUE FOR CALCULATING SHUNT LEAKAGE AND CELL CURRENTS IN BIPOLAR STACKS HAVING DIVIDED OR UNDIVIDED CELLS [J].
KAMINSKI, EA ;
SAVINELL, RF .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1983, 130 (05) :1103-1107
[10]  
Kinoshita K., 1988, CARBON ELECTROCHEMIC, P372