3D non-isothermal dynamic simulation of high temperature proton exchange membrane fuel cell in the start-up process

• Published in: International journal of hydrogen energy 2021-01, Vol.46 (2), p.2577-2593
• Main Authors: Zhang, Jun, Zhang, Caizhi, Hao, Dong, Ni, Meng, Huang, Shulong, Liu, Deman, Zheng, Yifeng
• Format: Article
• Language: English
• Subjects: Counter-flow; HT-PEMFC; Start-up process; Temperature distribution
• ISSN: 0360-3199; 1879-3487
• DOI: 10.1016/j.ijhydene.2020.10.116

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. •Applying a current load can significantly shorten start-up time.•Start-up time and temperature distribution are compared for co-flow and counter-flow.•Counter-flow needs more time to start, but temperature distribution is more evenly.•The effect of inlet gas temperature and velocity on start-up process are investigated.