Experiments and modeling of solid oxide co-electrolysis: Occurrence of CO2 electrolysis and safe operating conditions

被引:0
|
作者
Liang, Jingjing [1 ,2 ]
Liu, Yaodong [1 ]
Zhao, Yi [2 ]
Marechal, Francois [2 ]
Han, Minfang [1 ]
Sun, Kaihua [3 ]
机构
[1] Tsinghua Univ, Fuel Cell & Energy Storage Ctr, Dept Energy & Power Engn, State Key Lab Power Syst Operat & Control, Beijing 100084, Peoples R China
[2] Ecole Polytech Fed Lausanne, Ind Proc & Energy Syst Engn, CH-1950 Sion, Switzerland
[3] Xuzhou Huatsing Jingkun Energy Co Ltd, Xuzhou 221001, Jiangsu, Peoples R China
基金
中国国家自然科学基金;
关键词
SOEC; Co-electrolysis; Reaction mechanism; Carbon deposition; OXYGEN-ELECTRODE; ELECTROCHEMICAL PERFORMANCE; NI/YSZ ELECTRODES; CARBON DEPOSITION; SYNGAS PRODUCTION; FISCHER-TROPSCH; CELLS SOECS; HYDROGEN; H2O; DEGRADATION;
D O I
10.1016/j.cej.2024.154647
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Solid Oxide Electrolysis Cell (SOEC) has attracted considerable attention for its potential scalability and high energy conversion efficiency. It is capable of electrolyzing both H2O and CO2 simultaneously, generating syngas that can be further synthesized into carbon-based fuels, which are good energy carriers for long-term energy storage. However, despite its promise, the understanding of the reaction mechanism crucial for extending cell longevity remains incomplete, and concerns persist regarding carbon deposition during co-electrolysis. A dual approach, combining experiments and Multiphysics simulations was adopted to explore the reaction mechanism and carbon deposition risk across a wide range of operating conditions on industrial-size cells. Both experimental observations and simulation results indicate that CO2 electrolysis and carbon deposition are significantly influenced by the inlet water content and flow rates at the fuel electrode. Increasing the inlet H2O concentration and fuel electrode flow rates lead to CO2 electrolysis occurring at higher current densities. Also, carbon deposition, which was found at the interface of fuel electrode and electrolyte, can be mitigated by controlling the conversion rate relative to the inlet H2O content and by increasing the flow rate at the fuel electrode. Additionally, the current density distribution of H2O electrolysis and CO2 electrolysis across the cell were also investigated. The obtained insights hold significance for the practical operation of SOEC co-electrolysis.
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页数:16
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