A CFD Study with Analytical and Experimental Validation of Laminar and Turbulent Mass-Transfer in Electrochemical Reactors
被引:42
作者:
Colli, A. N.
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机构:
Univ Nacl Litoral, CONICET, Programa Electroquim Aplicada & Ingn Electroquim, Fac Ingn Quim, S3000AOM, Santa Fe, ArgentinaUniv Nacl Litoral, CONICET, Programa Electroquim Aplicada & Ingn Electroquim, Fac Ingn Quim, S3000AOM, Santa Fe, Argentina
Colli, A. N.
[1
]
Bisang, J. M.
论文数: 0引用数: 0
h-index: 0
机构:
Univ Nacl Litoral, CONICET, Programa Electroquim Aplicada & Ingn Electroquim, Fac Ingn Quim, S3000AOM, Santa Fe, ArgentinaUniv Nacl Litoral, CONICET, Programa Electroquim Aplicada & Ingn Electroquim, Fac Ingn Quim, S3000AOM, Santa Fe, Argentina
Bisang, J. M.
[1
]
机构:
[1] Univ Nacl Litoral, CONICET, Programa Electroquim Aplicada & Ingn Electroquim, Fac Ingn Quim, S3000AOM, Santa Fe, Argentina
TERTIARY CURRENT DISTRIBUTION;
PIPE-FLOW;
HIGH SCHMIDT;
TRANSPORT;
MODEL;
SIMULATIONS;
PREDICTION;
OPERATION;
NUMBERS;
CELL;
D O I:
10.1149/2.0971802jes
中图分类号:
O646 [电化学、电解、磁化学];
学科分类号:
081704 ;
摘要:
This work presents numerical simulations, with validation considering analytical expressions and experimental results, of mass-transfer in electrochemical reactors under laminar and turbulent flows in ducts of rectangular and tubular shape. Sudden expansion at the reactor inlet and segmented electrodes are also analyzed. Computational fluid dynamics (CFD) simulations were performed solving the laminar or RANS equations with the Shear Stress Transport (SST) k-omega turbulence model using the open source code OpenFOAMin steady-state. For mass-transfer simulations, the averaged diffusion-convection equation was implemented and solved. A good agreement between mass-transfer simulations with experimental data and analytical results were attained for both laminar and turbulent flow. Discussions about the segmented electrode technique in order to obtain local mass-transfer data in laminar and turbulent flow are also performed. (C) 2018 The Electrochemical Society.
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页码:E81 / E88
页数:8
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