TY - JOUR
T1 - Unveiling lifespan bottlenecks in high-power fuel cell stacks
T2 - Flow maldistribution, end-cell degradation, and GDL/CL interactions under accelerated degradation testing
AU - Xiao, Chenguang
AU - Xia, Qi
AU - Pei, Houchang
AU - Xing, Lu
AU - Chang, Huawei
AU - Tu, Zhengkai
PY - 2025/11/30
Y1 - 2025/11/30
N2 - To address the durability challenges in commercial vehicle fuel cell stacks, this study systematically investigated degradation mechanisms in an 80 kW stack via accelerated testing. A variable-spacing flow distribution zone with dynamic resistance adjustment capability was introduced to balance flow resistance, reducing the stoichiometric ratio range from 2.88/1.83 to 2.23/1.88 and significantly improving gas distribution uniformity. After 2000-h testing at 1.8 A cm−2, the voltage decay rate stabilized at 9.07 mV/h. Critically, the gas distribution end cell(GDE) emerged as the primary lifespan bottleneck, exhibiting a 43.2 % voltage loss (vs. 7.8 % in central cells) due to severe anode flooding (accumulating 80 % of inlet liquid water), which accelerated carbon corrosion and concentration polarization. Long-term operation degraded the gas diffusion layer by reducing porosity and small-pore proportions (<105 nm), impairing water management and increasing concentration polarization. Regional disparities in membrane electrode assembly degradation were observed, with outlet regions and middle channels degrading faster due to flow field-induced uneven gas distribution. Notably, catalyst layer thickness attenuation strongly correlated with Pt particle growth driven by carbon corrosion. These findings provide a universal framework for targeted flow field optimization and PEMFC durability enhancement through integrated water/gas management strategies.
AB - To address the durability challenges in commercial vehicle fuel cell stacks, this study systematically investigated degradation mechanisms in an 80 kW stack via accelerated testing. A variable-spacing flow distribution zone with dynamic resistance adjustment capability was introduced to balance flow resistance, reducing the stoichiometric ratio range from 2.88/1.83 to 2.23/1.88 and significantly improving gas distribution uniformity. After 2000-h testing at 1.8 A cm−2, the voltage decay rate stabilized at 9.07 mV/h. Critically, the gas distribution end cell(GDE) emerged as the primary lifespan bottleneck, exhibiting a 43.2 % voltage loss (vs. 7.8 % in central cells) due to severe anode flooding (accumulating 80 % of inlet liquid water), which accelerated carbon corrosion and concentration polarization. Long-term operation degraded the gas diffusion layer by reducing porosity and small-pore proportions (<105 nm), impairing water management and increasing concentration polarization. Regional disparities in membrane electrode assembly degradation were observed, with outlet regions and middle channels degrading faster due to flow field-induced uneven gas distribution. Notably, catalyst layer thickness attenuation strongly correlated with Pt particle growth driven by carbon corrosion. These findings provide a universal framework for targeted flow field optimization and PEMFC durability enhancement through integrated water/gas management strategies.
KW - 80 kW commercial fuel cell stack
KW - Degradation
KW - End cell effects
KW - Lifetime
KW - Voltage decay rate
UR - https://www.scopus.com/pages/publications/105018172413
U2 - 10.1016/j.energy.2025.138869
DO - 10.1016/j.energy.2025.138869
M3 - Article
AN - SCOPUS:105018172413
SN - 0360-5442
VL - 338
SP - 1
EP - 15
JO - Energy
JF - Energy
M1 - 138869
ER -