3D CFD model of a multi-cell high-temperature electrolysis stack

被引:66
作者
Hawkes, Grant [1 ]
O'Brien, James [1 ]
Stoots, Carl [1 ]
Hawkes, Brian [1 ]
机构
[1] Idaho Natl Lab, Idaho Falls, ID 83415 USA
关键词
CFD high-temperature steam electrolysis; Hydrogen production; HYDROGEN-PRODUCTION; NUCLEAR-ENERGY; PERFORMANCE;
D O I
10.1016/j.ijhydene.2008.11.068
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 three-dimensional (3D) computational fluid dynamics (CFDs) electrochemical model has been created to model high-temperature electrolysis stack performance and steam electrolysis in the Idaho National Laboratory (INL) Integrated Lab Scale (ILS) experiment. The model is made of 60 planar cells stacked on top of each other operated as solid oxide electrolysis cells (SOECs). Details of the model geometry are specific to a stack that was fabricated by Ceramatec, Inc. [References herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or other-wise, does not necessarily constitute or imply its endorsement, recommendation, or favoring by the U.S. Government, any agency thereof, or any company affiliated with the Idaho National Laboratory]. and tested at INL. Inlet and outlet plenum flow and distribution are considered. Mass, momentum, energy, and species conservation and transport are provided via the core features of the commercial CFD code FLUENT. [References herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or otherwise, does not necessarily constitute or imply its endorsement, recommendation, or favoring by the U.S. Government, any agency thereof, or any company affiliated with the Idaho National Laboratory]. A solid oxide fuel cell (SOFC) model adds the electrochemical reactions and loss mechanisms and computation of the electric field throughout the cell. The FLUENT SOFC user-defined subroutine was modified for this work to allow for operation in the SOEC mode. Model results provide detailed profiles of temperature, Nernst potential, operating potential, activation over potential, anode-side gas composition, cathode-side gas composition, current density, and hydrogen production over a range of stack operating conditions. Variations in flow distribution and species concentration are discussed. End effects of flow and per-cell voltage are also considered. (C) 2008 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:4189 / 4197
页数:9
相关论文
共 13 条
[1]   HYDROGEN-PRODUCTION BY HIGH-TEMPERATURE ELECTROLYSIS OF WATER-VAPOR [J].
DOENITZ, W ;
SCHMIDBERGER, R ;
STEINHEIL, E ;
STREICHER, R .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1980, 5 (01) :55-63
[2]  
Doenitz W, 1985, INT J HYDROGEN ENERG, V10, P291
[3]  
DOENITZ W, 1982, INT J HYDROGEN ENERG, V3, P29
[4]  
*FLUENT INC, FLUENT 6 3 FUEL CELL
[5]  
Forsberg CW, 2003, INT J HYDROGEN ENERG, V28, P1073
[6]  
HAWKES GL, 2007, 2007 ASME JSME THERM
[7]   Computational fluid dynamics model of a planar solid-oxide electrolysis cell for hydrogen production from nuclear energy [J].
Hawkes, Grant L. ;
O'Brien, James E. ;
Stoots, Carl M. ;
Herring, J. Stephen ;
Shahnam, Mehrdad .
NUCLEAR TECHNOLOGY, 2007, 158 (02) :132-144
[8]  
HENDERSON DA, 2005 ANN DOE HYDROGE
[9]   Progress in high-temperature electrolysis for hydrogen production using planar SOFC technology [J].
Herring, J. Stephen ;
O'Brien, James E. ;
Stoots, Carl M. ;
Hawkes, G. L. ;
Hartvigsen, Joseph J. ;
Shahnam, Mehrdad .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2007, 32 (04) :440-450
[10]  
JENSEN M, DK4000 RIS NAT LAB M