Dynamic Behavior of a Solid Oxide Steam Electrolyzer System Using Transient Photovoltaic Generated Power for Renewable Hydrogen Production

被引:17
作者
Saeedmanesh, Alireza [1 ]
Colombo, Paolo [2 ]
McLarty, Dustin [3 ]
Brouwer, Jack [1 ]
机构
[1] Univ Calif Irvine, Dept Mech & Aerosp Engn, Irvine, CA 92697 USA
[2] Politecn Torino, Dept Energy, I-10129 Turin, Italy
[3] Washington State Univ, Sch Mech & Mat Engn, Pullman, WA 99164 USA
基金
美国国家科学基金会;
关键词
CO-ELECTROLYSIS; CARBON-DIOXIDE; CELL; ENERGY; PERFORMANCE; OPERATION;
D O I
10.1115/1.4043340
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
This study investigates the dynamic behavior of a solid oxide steam electrolyzer (SOSE) system without an external heat source that uses transient photovoltaic (PV) generated power as an input to produce compressed (to 3 MPa) renewable hydrogen to be injected directly into the natural gas network. A cathode-supported crossflow planar solid oxide electrolysis (SOE) cell is modeled in a quasi-three-dimensional thermo-electrochemical model that spatially and temporally simulates the performance of a unit cell operating dynamically. The stack is composed of 2500 unit cells that are assumed to be assembled into identically operating stacks, creating a 300 kW electrolyzer stack module. For the designed 300 kW SOSE stack (thermoneutral voltage achieved at design steady-state conditions), powered by the dynamic 0-450 kW output of PV systems, thermal management and balancing of all heat supply and cooling demands is required based upon the operating voltage to enable efficient operation and prevent degradation of the SOSE stacks. Dynamic system simulation results show that the SOSE system is capable of following the dynamic PV generated power for a sunny day (maximum PV generated power) and a cloudy day (highly dynamic PV generated power) while the SOSE stack temperature gradient is always maintained below a maximum set point along the stack for both days. The system efficiency based upon lower heating value of the generated hydrogen is between 0-75% and 0-78% with daily hydrogen production of 94 kg and 55 kg for sunny and cloudy days, respectively.
引用
收藏
页数:14
相关论文
共 27 条
[1]   Optimal control strategies for hydrogen production when coupling solid oxide electrolysers with intermittent renewable energies [J].
Cai, Qiong ;
Adjiman, Claire S. ;
Brandon, Nigel P. .
JOURNAL OF POWER SOURCES, 2014, 268 :212-224
[2]  
California Energy Commission, 2017, CAL EN COMM TRACK PR
[3]   A comparative assessment on hydrogen production from low- and high-temperature electrolysis [J].
Ferrero, Domenico ;
Lanzini, Andrea ;
Santarelli, Massimo ;
Leone, Pierluigi .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2013, 38 (09) :3523-3536
[4]   Synthetic natural gas via integrated high-temperature electrolysis and methanation: Part I-Energy performance [J].
Giglio, Emanuele ;
Lanzini, Andrea ;
Santarelli, Massimo ;
Leone, Pierluigi .
JOURNAL OF ENERGY STORAGE, 2015, 1 (01) :22-37
[5]   Co-electrolysis of CO2 and H2O in solid oxide cells: Performance and durability [J].
Graves, Christopher ;
Ebbesen, Sune D. ;
Mogensen, Mogens .
SOLID STATE IONICS, 2011, 192 (01) :398-403
[6]   Solid oxide electrolysis cell 3D simulation using artificial neural network for cathodic process description [J].
Grondin, D. ;
Deseure, J. ;
Ozil, P. ;
Chabriat, J. -P. ;
Grondin-Perez, B. ;
Brisse, A. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2013, 91 (01) :134-140
[7]  
Grondin D., 2008, P COMSOL C HANN GERM
[8]   Performance and methane production characteristics of H2O-CO2 co-electrolysis in solid oxide electrolysis cells [J].
Li, Wenying ;
Wang, Hongjian ;
Shi, Yixiang ;
Cai, Ningsheng .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2013, 38 (25) :11104-11109
[9]   Dynamic electro-thermal modeling of co-electrolysis of steam and carbon dioxide in a tubular solid oxide electrolysis cell [J].
Luo, Yu ;
Shi, Yixiang ;
Li, Wenying ;
Cai, Ningsheng .
ENERGY, 2015, 89 :637-647
[10]  
McLarty D., 2010, P ASME FUEL CELL SCI