TY - JOUR
T1 - Glycerol-assisted co-electrolysis in solid oxide electrolyzer cell (SOEC) for green syngas production
T2 - A 2D modelling study
AU - Wang, Chen
AU - Li, Zheng
AU - Guan, Daqin
AU - Zhu, Meng
AU - Bello, Idris Temitope
AU - Han, Minfang
AU - Ni, Meng
N1 - Funding Information:
M. NI thanks the grants (Project Number: N_PolyU552/20) from Research Grants Council, University Grants Committee , Hong Kong SAR.
Publisher Copyright:
© 2023 Elsevier Ltd
PY - 2023/12/1
Y1 - 2023/12/1
N2 - A 2D multi-physics model is developed to study the glycerol-assisted SOEC co-electrolysis process, with a novel in-tube reformer to improve the fuel utilization and reduce the temperature difference. After model validation, the effects of key operating parameters on the electrochemical performance and temperature distribution of the system are investigated. It is found that glycerol assistance can significantly reduce the operating voltage of the SOEC co-electrolysis system, thus saving over 55 % of electrical energy at 1073 K. Besides, increasing operating voltage, operating temperature and cathode H2O molar fraction promote the co-electrolysis process, leading to an increase in cathode H2O/CO2 conversion. Optimal values of the anode/cathode flow rates (Qan = 70–110 SCCM and Qca = 125–175 SCCM) and the anode glycerol molar fraction (Xan,GL = 0.05–0.15) are obtained to achieve both good electrochemical performance and uniform temperature distribution. Meanwhile, the proposed in-tube reformer can greatly reduce the temperature difference inside the cell, and by precisely controlling the structure and operating parameters of the system, a more uniform internal temperature distribution can be obtained, even allowing the system to be operated at homogeneous temperature conditions. This study provides a reference for the commercialization of efficient green syngas production and CO2 recycling by using renewable electricity.
AB - A 2D multi-physics model is developed to study the glycerol-assisted SOEC co-electrolysis process, with a novel in-tube reformer to improve the fuel utilization and reduce the temperature difference. After model validation, the effects of key operating parameters on the electrochemical performance and temperature distribution of the system are investigated. It is found that glycerol assistance can significantly reduce the operating voltage of the SOEC co-electrolysis system, thus saving over 55 % of electrical energy at 1073 K. Besides, increasing operating voltage, operating temperature and cathode H2O molar fraction promote the co-electrolysis process, leading to an increase in cathode H2O/CO2 conversion. Optimal values of the anode/cathode flow rates (Qan = 70–110 SCCM and Qca = 125–175 SCCM) and the anode glycerol molar fraction (Xan,GL = 0.05–0.15) are obtained to achieve both good electrochemical performance and uniform temperature distribution. Meanwhile, the proposed in-tube reformer can greatly reduce the temperature difference inside the cell, and by precisely controlling the structure and operating parameters of the system, a more uniform internal temperature distribution can be obtained, even allowing the system to be operated at homogeneous temperature conditions. This study provides a reference for the commercialization of efficient green syngas production and CO2 recycling by using renewable electricity.
KW - CO recycling
KW - Fuel assisted co-electrolysis
KW - Numerical modeling
KW - Solid oxide electrolyzer cell
KW - Thermal effect
UR - http://www.scopus.com/inward/record.url?scp=85165487923&partnerID=8YFLogxK
U2 - 10.1016/j.fuel.2023.129227
DO - 10.1016/j.fuel.2023.129227
M3 - Journal article
AN - SCOPUS:85165487923
SN - 0016-2361
VL - 353
JO - Fuel
JF - Fuel
M1 - 129227
ER -