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Computational fluid dynamics modeling of a solid oxide electrolyzer cell for hydrogen production
被引:103
作者:
Ni, Meng
[1
]
机构:
[1] Hong Kong Polytech Univ, Dept Bldg & Real Estate, Kowloon, Hong Kong, Peoples R China
关键词:
Heat and mass transfer;
Solid oxide fuel cell (SOFC);
High temperature steam electrolysis;
Electrochemistry;
Porous media;
Transport phenomena;
HIGH-TEMPERATURE ELECTROLYSIS;
FUEL-CELL;
STEAM ELECTROLYSIS;
WATER-VAPOR;
TRANSPORT PHENOMENA;
HEAT/MASS TRANSFER;
COUPLED TRANSPORT;
DUCTS RELEVANT;
ENERGY;
ANODE;
D O I:
10.1016/j.ijhydene.2009.07.080
中图分类号:
O64 [物理化学(理论化学)、化学物理学];
学科分类号:
070304 ;
081704 ;
摘要:
A 2D computational fluid dynamics (CFD) model was developed to study the performance of a planar solid oxide electrolyzer cell (SOEC) for hydrogen production. The governing equations for mass continuity, momentum conservation, energy conservation and species conservation were discretized with the finite volume method (FVM). The coupling of velocity and pressure was treated with the SIMPLEC (Semi-Implicit Method for Pressure Linked Equations - Consistent) algorithm. Simulations were performed to investigate the effects of operating/structural parameters on heat/mass transfer and the electric characteristics of a planar SOEC. It is found that the gas velocity at the cathode increases significantly along the main flow channel, as the increase in H-2 molar fraction decreases the density and viscosity of the gas mixture at the cathode. It is also found that increasing the inlet gas velocity can enhance the SOEC performance. Another important finding is that the electrode porosity has small effect on SOEC performance. The results of this paper provide better understanding on the coupled heat/mass transfer and electrochemical reaction phenomena in an SOEC. The model developed can serve as a useful tool for SOEC design optimization. (C) 2009 Professor T. Nejat Veziroglu. Published by Elsevier Ltd. All rights reserved.
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页码:7795 / 7806
页数:12
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