Dynamic modelling of hydrogen evolution effects in the all-vanadium redox flow battery

被引:251
作者
Shah, A. A. [1 ]
Al-Fetlawi, H. [1 ]
Walsh, F. C. [1 ]
机构
[1] Univ Southampton, Sch Engn Sci, Energy Technol Res Grp, Electrochem Engn Lab, Southampton SO17 1BJ, Hants, England
关键词
Bubble formation; Flow battery; Hydrogen evolution; Mathematical model; Numerical simulation; ION-EXCHANGE MEMBRANES; MASS-TRANSFER; 2-PHASE FLOW; MATHEMATICAL-MODEL; GAS-BUBBLES; SIMULATION; DIFFUSION; CONVECTION; ELECTRODES; TRANSPORT;
D O I
10.1016/j.electacta.2009.10.022
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
A model for hydrogen evolution in an all-vanadium redox flow battery is developed, coupling the dynamic conservation equations for charge, mass and momentum with a detailed description of the electrochemical reactions. Bubble formation at the negative electrode is included in the model, taking into account the attendant reduction in the liquid volume and the transfer of momentum between the gas and liquid phases, using a modified multiphase-mixture approach. Numerical simulations are compared to experimental data for different vanadium concentrations and mean linear electrolyte flow rates, demonstrating good agreement. Comparisons to simulations with negligible hydrogen evolution demonstrate the effect of gas evolution on the efficiency of the battery. The effects of reactant concentration, flow rate, applied current density and gas bubble diameter on hydrogen evolution are investigated. Significant variations in the gas volume fraction and the bubble velocity are predicted, depending on the operating conditions. (C) 2009 Elsevier Ltd. All rights reserved
引用
收藏
页码:1125 / 1139
页数:15
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