TY - JOUR
T1 - 3D non-isothermal dynamic simulation of high temperature proton exchange membrane fuel cell in the start-up process
AU - Zhang, Jun
AU - Zhang, Caizhi
AU - Hao, Dong
AU - Ni, Meng
AU - Huang, Shulong
AU - Liu, Deman
AU - Zheng, Yifeng
N1 - Funding Information:
This work is supported in part by the National Nature Science Foundation of China ( 51806024 ), the Technological Innovation and Application Demonstration in Chongqing (Major Themes of Industry: cstc2018jszx-cyztzxX0005 , cstc2019jscx-zdztzxX0033 ), Tianjin Municipal Science and Technology Commission Program (Project No. 17ZXFWGX00040 ) and the Fundamental Research Funds for the Central Universities (No.: 2019CDXYQC0003 , 244005202014 , and No.: 2018CDXYTW0031 ). This work is also supported by Beijing Computing Centre for providing the cloud computing services. M. Ni thanks the grants (Project Number: PolyU 152214/17E and PolyU 152064/18E) from Research Grant Council, University Grants Committee, Hong Kong SAR.
Publisher Copyright:
© 2020 Hydrogen Energy Publications LLC
Copyright:
Copyright 2020 Elsevier B.V., All rights reserved.
PY - 2021/1/6
Y1 - 2021/1/6
N2 - High temperature proton exchange membrane fuel cell (HT-PEMFC) with phosphoric acid doped polybenzimidazole (PBI) electrolyte shows multiple advantages over conventional PEMFC working at below 373 K, such as faster electrochemical kinetics, simpler water management, higher carbon monoxide tolerance. However, starting HT-PEMFC from room temperature to the optimal operating temperature range (433.15 K–453.15 K) is still a serious challenge. In present work, the start-up strategy is proposed and evaluated and a three-dimensional non-isothermal dynamic model is developed to investigate start-up time and temperature distribution during the start-up process. The HT-PEMFC is preheated by gas to 393.15 K, followed by discharging a current from the cell for electrochemical heat generation. Firstly, different current loads are applied when the average temperature of membrane reaches 393.15 K. Then, the start-up time and temperature distribution of co-flow and counter-flow are compared at different current loads. Finally, the effect of inlet velocity and temperature on the start-up process are explored in the case of counter-flow. Numerical results clearly show that applied current load is necessary to reduce start-up time and just 0.1 A/cm2 current load can reduce startup time by 45%. It is also found that co-flow takes 18.8% less time than counter-flow to heat membrane temperature to 393.15 K, but the maximum temperature difference of membrane is 39% higher than the counter-flow. Increasing the inlet gas flow velocity and temperature can shorten the start-up time but increases the temperature difference of the membrane.
AB - High temperature proton exchange membrane fuel cell (HT-PEMFC) with phosphoric acid doped polybenzimidazole (PBI) electrolyte shows multiple advantages over conventional PEMFC working at below 373 K, such as faster electrochemical kinetics, simpler water management, higher carbon monoxide tolerance. However, starting HT-PEMFC from room temperature to the optimal operating temperature range (433.15 K–453.15 K) is still a serious challenge. In present work, the start-up strategy is proposed and evaluated and a three-dimensional non-isothermal dynamic model is developed to investigate start-up time and temperature distribution during the start-up process. The HT-PEMFC is preheated by gas to 393.15 K, followed by discharging a current from the cell for electrochemical heat generation. Firstly, different current loads are applied when the average temperature of membrane reaches 393.15 K. Then, the start-up time and temperature distribution of co-flow and counter-flow are compared at different current loads. Finally, the effect of inlet velocity and temperature on the start-up process are explored in the case of counter-flow. Numerical results clearly show that applied current load is necessary to reduce start-up time and just 0.1 A/cm2 current load can reduce startup time by 45%. It is also found that co-flow takes 18.8% less time than counter-flow to heat membrane temperature to 393.15 K, but the maximum temperature difference of membrane is 39% higher than the counter-flow. Increasing the inlet gas flow velocity and temperature can shorten the start-up time but increases the temperature difference of the membrane.
KW - Counter-flow
KW - HT-PEMFC
KW - Start-up process
KW - Temperature distribution
UR - http://www.scopus.com/inward/record.url?scp=85095811184&partnerID=8YFLogxK
U2 - 10.1016/j.ijhydene.2020.10.116
DO - 10.1016/j.ijhydene.2020.10.116
M3 - Journal article
AN - SCOPUS:85095811184
SN - 0360-3199
VL - 46
SP - 2577
EP - 2593
JO - International Journal of Hydrogen Energy
JF - International Journal of Hydrogen Energy
IS - 2
ER -