Numerical investigation of solid oxide electrolysis cells for hydrogen production applied with different continuity expressions

被引:18
作者
Zhang, Ji-Hao [1 ,2 ,3 ]
Lei, Li-Bin [4 ]
Liu, Di [5 ]
Zhao, Fu-Yun [1 ,2 ,3 ]
Chen, Fanglin [4 ]
Wang, Han-Qing [6 ]
机构
[1] Wuhan Univ, Minist Educ, Key Lab Hydraul Machinery Transients, Wuhan, Hubei, Peoples R China
[2] Wuhan Univ, Hubei Key Lab Waterjet Theory & New Technol, Wuhan, Hubei, Peoples R China
[3] Wuhan Univ, Sch Power & Mech Engn, Wuhan 430072, Hubei, Peoples R China
[4] Univ South Carolina, Dept Mech Engn, Columbia, SC 29208 USA
[5] China Univ Petr, Coll Pipeline & Civil Engn, Qingdao, Shandong, Peoples R China
[6] Univ South China, Sch Civil Engn, Hengyang, Hunan, Peoples R China
关键词
SOECs modeling; Source imbalance; Current densities; Computational fluid dynamics (CFD); MEMBRANE FUEL-CELL; STEAM ELECTROLYSIS; MATHEMATICAL-MODEL; BOUNDARY-CONDITIONS; FLOW-FIELD; CFD MODEL; PERFORMANCE; SIMULATION; SOFC; STATE;
D O I
10.1016/j.enconman.2017.07.013
中图分类号
O414.1 [热力学];
学科分类号
摘要
A dynamic SOEC (Solid Oxide Electrolysis Cell) model is proposed to investigate the transient response and steady performance of a planar SOEC. Three representative types of continuity equation expressions are systematically compared for the simulation of source terms introduced by electrochemical reactions. For the conservative form of continuity equation (Type A), reasonable predictions at both sides of cathode and anode cannot be achieved, as the diffusion effect is neglected. The non-conservative form of continuity equation (Type B) can obtain reasonable prediction for the cathode side but poor prediction for the anode side. The Type C of continuity equation, newly proposed by the authors for modeling the SOECs, is based on the law of volume conservation. It could achieve the volume increment (oxygen produced) at the anode compartment and good agreements with the analytical ones. It is also found that continuity equations significantly influence the fluid flow and mass transport, whereas their effects on the electrical characteristics are negligible when the global current density is not high. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:646 / 659
页数:14
相关论文
共 49 条
[1]   Experimental Validation of Two-Dimensional H2O and CO2 Co-Electrolysis Modeling [J].
Aicart, J. ;
Laurencin, J. ;
Petitjean, M. ;
Dessemond, L. .
FUEL CELLS, 2014, 14 (03) :430-447
[2]   Modeling optimizes PEM fuel cell performance using three-dimensional multi-phase computational fluid dynamics model [J].
Al-Baghdadi, Maher A. R. Sadiq ;
Al-Janabi, Haroun A. K. Shahad .
ENERGY CONVERSION AND MANAGEMENT, 2007, 48 (12) :3102-3119
[3]   SOFC modeling considering electrochemical reactions at the active three phase boundaries [J].
Andersson, Martin ;
Yuan, Jinliang ;
Sunden, Bengt .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2012, 55 (04) :773-788
[4]   Modelling and simulation of the steady-state and dynamic behaviour of a PEM fuel cell [J].
Asl, S. M. Sharifi ;
Rowshanzamir, S. ;
Eikani, M. H. .
ENERGY, 2010, 35 (04) :1633-1646
[5]   Double diffusive natural convection in an enclosure filled with a step type porous layer: Non-Darcy flow [J].
Baytas, A. C. ;
Baytas, A. F. ;
Ingham, D. B. ;
Pop, I. .
INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2009, 48 (04) :665-673
[6]   BOUNDARY CONDITIONS AT A NATURALLY PERMEABLE WALL [J].
BEAVERS, GS ;
JOSEPH, DD .
JOURNAL OF FLUID MECHANICS, 1967, 30 :197-&
[7]   A nonequilibrium finite-volume model for conjugate fluid/porous/solid domains [J].
Betchen, L ;
Straatman, AG ;
Thompson, BE .
NUMERICAL HEAT TRANSFER PART A-APPLICATIONS, 2006, 49 (06) :543-565
[8]   Thermal stress and thermo-electrochemical analysis of a planar anode-supported solid oxide fuel cell: Effects of anode porosity [J].
Chiang, Lieh-Kwang ;
Liu, Hui-Chung ;
Shiu, Yao-Hua ;
Lee, Chien-Hsiung ;
Lee, Ruey-Yi .
JOURNAL OF POWER SOURCES, 2010, 195 (07) :1895-1904
[9]   Simulation of coupled flows in adjacent porous and open domains using a control-volume finite-element method [J].
Costa, VAF ;
Oliveira, LA ;
Baliga, BR ;
Sousa, ACM .
NUMERICAL HEAT TRANSFER PART A-APPLICATIONS, 2004, 45 (07) :675-697
[10]   Modeling at solid oxide heat exchanger integrated stacks and simulation at high fuel utilization [J].
Costamagna, P ;
Honegger, K .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1998, 145 (11) :3995-4007