Pressure Drop through Platinized Titanium Porous Electrodes for Cerium-Based Redox Flow Batteries

被引:37
作者
Arenas, Luis F. [1 ]
de Leon, Carlos Ponce [1 ]
Walsh, Frank C. [1 ]
机构
[1] Univ Southampton, Dept Mech Engn, Energy Technol Grp, Electrochem Engn Lab, Southampton SO17 1BJ, Hants, England
关键词
cerium; electrochemical flow reactor; platinized titanium; porous electrode; pressure drop; redox flow battery; RETICULATED VITREOUS CARBON; ENERGY-STORAGE; MASS-TRANSPORT; RECTANGULAR CHANNEL; NICKEL FOAM; ELECTROCHEMICAL REACTOR; PERFORMANCE; DESIGN; CELL; ELECTROLYZER;
D O I
10.1002/aic.16000
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The pressure drop, Delta P, across a redox flow battery is linked to pumping costs and energy efficiency, making fluid properties of the electrolyte important in scale-up operations. The Delta P at diverse platinized titanium electrodes in Ce-based redox flow batteries is reported as a function of mean linear electrolyte velocity measured in a rectangular channel flow cell. Darcy's friction factor and permeability vs. Reynolds number are calculated. Average permeability values are: 7.10 x 10(-4) cm(2) for Pt/Ti mesh, 4.45 x 10(-40) cm(2) for Pt/Ti plate + turbulence promoters, 1.67 x 10(-5) cm(2) for Pt/Ti micromesh, and 1.31 x 10(-6) cm(2) for Pt/Ti felt. The electrochemical volumetric mass transport coefficient, k(m)A(e), is provided as a function of Delta P. In the flow-by configuration, Pt/Ti felt combines high k(m)A(e) values with a relatively high Delta P, followed by Pt/Ti micromesh. Pt/Ti mesh and Pt/Ti plate gave a lower Delta P but poorer electrochemical performance. Implications for cell design are discussed. (c) 2017 American Institute of Chemical Engineers
引用
收藏
页码:1135 / 1146
页数:12
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