Extensive analysis of an SOC stack for mobile application in reversible mode under various operating conditions

被引:12
作者
Preininger, Michael [1 ]
Stoeckl, Bernhard [1 ]
Subotic, Vanja [1 ]
Hochenauer, Christoph [1 ]
机构
[1] Graz Univ Technol, Inst Thermal Engn, Inffeldgasse 25b, A-8010 Graz, Austria
关键词
solid oxide cell (SOC); Anode-supported cell (ASC); High temperature electrolysis (HTE); Lightweight SOC stack; OXIDE FUEL-CELLS; HIGH-TEMPERATURE ELECTROLYSIS; CO-ELECTROLYSIS; HYDROGEN-PRODUCTION; ELECTROCHEMICAL CHARACTERIZATION; SYNGAS PRODUCTION; H2O ELECTROLYSIS; SYNTHETIC FUELS; CARBON-DIOXIDE; SOFC STACK;
D O I
10.1016/j.electacta.2018.12.141
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
The reversible solid oxide cell (rSOC) is a key technology that is capable of generating electricity, heat, and valuable fuels in a highly efficient manner. By integrating an rSOC module and all of the necessary components into a compact unit, it is possible to realize an autonomous reversible system. In order to learn more about the durability and reliability of a ten-cell rSOC stack, originally developed for mobile applications, was operated in both fuel cell and electrolysis modes under realistic operating conditions. The stack was fed with gas mixtures of H-2, H2O, CO2 and CO. The stack examined in the course of these experiments consists of large, planar, anode-supported cells (ASC). Compared to stacks with conventionally produced interconnects, the concept used for this stack was based on stamped metal sheet plates of CroFer22 APU, which means that they are lightweight and easy to assemble. The present study includes a detailed characterization of the stack's performance during reversible operation and evaluates its applicability for real operation. To this end, a comprehensive stack analysis including electrochemical impedance spectroscopy (EIS), chronopotentiometry, a gas analysis, polarization curves, and temperature measurements. In consideration of system integrations, the stack was operated in galvanostatic mode under system-relevant, steady-state conditions: at a fuel utilization of 80% in fuel cell mode, and at a reactant utilization of 70% in electrolysis mode. The feasibility of this SOC stack's long-term operation has thus been proven for an operating time of >2000 h. Finally, degradation analyses of both the stack and the individual cells were performed, whereby the stack was observed to have a degradation rate of 3.7%/kh. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页码:692 / 707
页数:16
相关论文
共 72 条
[1]   Operating maps of high temperature H2O electrolysis and H2O+CO2 co-electrolysis in solid oxide cells [J].
Aicart, J. ;
Usseglio-Viretta, F. ;
Laurencin, J. ;
Petitjean, M. ;
Delette, G. ;
Dessemond, L. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (39) :17233-17246
[2]   Accurate predictions of H2O and CO2 co-electrolysis outlet compositions in operation [J].
Aicart, J. ;
Petitjean, M. ;
Laurencin, J. ;
Tallobre, L. ;
Dessemond, L. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2015, 40 (08) :3134-3148
[3]   Production of synthesis gas (H2 and CO) by high-temperature Co-electrolysis of H2O and CO2 [J].
Alenazey, Feraih ;
Alyousef, Yousef ;
Almisned, Omar ;
Almutairi, Ghzzai ;
Ghouse, Mohammad ;
Montinaro, Dario ;
Ghigliazza, Francesco .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2015, 40 (32) :10274-10280
[4]   Hierarchical modeling of solid oxide cells and stacks producing syngas via H2O/CO2 Co-electrolysis for industrial applications [J].
Banerjee, A. ;
Wang, Y. ;
Diercks, J. ;
Deutschmann, O. .
APPLIED ENERGY, 2018, 230 :996-1013
[5]  
Bienert C., 2015, ECS Transactions, V68, P2159, DOI 10.1149/06801.2159ecst
[6]   A NONLINEAR LEAST-SQUARES FIT PROCEDURE FOR ANALYSIS OF IMMITTANCE DATA OF ELECTROCHEMICAL SYSTEMS [J].
BOUKAMP, BA .
SOLID STATE IONICS, 1986, 20 (01) :31-44
[7]   High temperature water electrolysis in solid oxide cells [J].
Brisse, Annabelle ;
Schefold, Josef ;
Zahid, Mohsine .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (20) :5375-5382
[8]   High Temperature Electrolysis at EIFER, main achievements at cell and stack level [J].
Brisse, Annabelle ;
Schefold, Josef .
WHEC 2012 CONFERENCE PROCEEDINGS - 19TH WORLD HYDROGEN ENERGY CONFERENCE, 2012, 29 :53-63
[9]   Syngas production by high temperature steam/CO2 coelectrolysis using solid oxide electrolysis cells [J].
Chen, Xinbing ;
Guan, Chengzhi ;
Xiao, Guoping ;
Du, Xianlong ;
Wang, Jian-Qiang .
FARADAY DISCUSSIONS, 2015, 182 :341-351
[10]   An experimental investigation of fuel assisted electrolysis as a function of fuel and reactant utilization [J].
Cinti, G. ;
Bidini, G. ;
Hemmes, K. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (28) :11857-11867