TY - JOUR
T1 - Linking Structure to Performance: Characterization of Porous Transport Layers for High-Pressure Water Electrolysis
T2 - Article No. 150924
AU - P. M. Duarte, Ricardo
AU - Kowal, Andrea
AU - Young, James
AU - Lang, Jack
AU - Zenyuk, Iryna
AU - Wrubel, Jacob
AU - Bender, Guido
PY - 2025
Y1 - 2025
N2 - Proton exchange membrane (PEM) water electrolysis is a promising technology to produce cost-efficient hydrogen. PEM electrolyzers offer a large current density range and the ability to operate at differential pressure which can be used to minimize both capital and operational expenditures. However, directly producing pressurized hydrogen at the cathode results in pushing the membrane against the anode porous transport layer (PTL). This can lead to detrimental effects, such as membrane deformation or ruptures, which depend on membrane properties as well as PTL material properties such as pore size, structure, and morphology. In this work, a range of sinter and felt-based commercial PTLs are evaluated for their contributions to the cell's electrochemical and H2 crossover performance at cathode pressures up to 30 bar. X-ray tomography and post-operando optical microscopy are used to assess the morphology of the PTLs, and the PTL induced deformation experienced by the catalyst coated membrane (CCM), respectively. PTL samples with lower porosity were found to reduce both the cell voltage and the amount of H2 permeating from the cathode to the anode exhaust, which was ascribed to improved catalyst layer contact and reduced membrane deformation, respectively. The best performing PTLs improved electrolyzer efficiency by ~1.5 kWh/kgH2. Specifically, 1 kWh/kgH2 was gained due to reducing membrane deformation and decreasing H2 crossover. The remainder 0.5 kWh/kgH2 were achieved by improving the electrical contact at the electrode/PTL interface which decreased cell voltage.
AB - Proton exchange membrane (PEM) water electrolysis is a promising technology to produce cost-efficient hydrogen. PEM electrolyzers offer a large current density range and the ability to operate at differential pressure which can be used to minimize both capital and operational expenditures. However, directly producing pressurized hydrogen at the cathode results in pushing the membrane against the anode porous transport layer (PTL). This can lead to detrimental effects, such as membrane deformation or ruptures, which depend on membrane properties as well as PTL material properties such as pore size, structure, and morphology. In this work, a range of sinter and felt-based commercial PTLs are evaluated for their contributions to the cell's electrochemical and H2 crossover performance at cathode pressures up to 30 bar. X-ray tomography and post-operando optical microscopy are used to assess the morphology of the PTLs, and the PTL induced deformation experienced by the catalyst coated membrane (CCM), respectively. PTL samples with lower porosity were found to reduce both the cell voltage and the amount of H2 permeating from the cathode to the anode exhaust, which was ascribed to improved catalyst layer contact and reduced membrane deformation, respectively. The best performing PTLs improved electrolyzer efficiency by ~1.5 kWh/kgH2. Specifically, 1 kWh/kgH2 was gained due to reducing membrane deformation and decreasing H2 crossover. The remainder 0.5 kWh/kgH2 were achieved by improving the electrical contact at the electrode/PTL interface which decreased cell voltage.
KW - high pressure operation
KW - hydrogen crossover
KW - low temperature water electrolysis
KW - porous transport layer
U2 - 10.1016/j.ijhydene.2025.150924
DO - 10.1016/j.ijhydene.2025.150924
M3 - Article
SN - 0360-3199
VL - 165
JO - International Journal of Hydrogen Energy
JF - International Journal of Hydrogen Energy
ER -