Platinum catalyst layers with Pt loadings w = 0.05-0.40 mg/cm 2 were deposited by magnetron sputtering from a variable deposition angle ␣ onto gas diffusion layer ͑GDL͒ substrates and tested as cathode electrodes in proton exchange membrane ͑PEM͒ fuel cells using Nafion 1135 membranes and Teflon-bonded Pt-black electrode ͑TBPBE͒ anodes. Layers deposited at normal incidence ͑␣ = 0°͒ are continuous and approximately replicate the rough surface morphology of the underlying GDL. In contrast, glancing angle deposition ͑GLAD͒ with ␣ = 87°and continuous substrate rotation yields highly porous layers consisting of vertically oriented Pt particles, 100-500 nm high and 100-300 nm wide, that are separated by 20-100 nm. The particle electrodes exhibit a higher ͑lower͒ mass-specific performance than the continuous-layer electrodes for a high ͑low͒ current density i. This is attributed to a higher porosity but lower overall electrochemically active surface area for the particles compared to the continuous layer. Increasing w in particle cells from 0.05 to 0.10 to 0.18 mg/cm 2 yields increasing potentials, but w = 0.40 mg/cm 2 causes a voltage drop at i Ͼ 0.4 A/cm 2 , associated with the reduced pore density at large w. Comparison cells with a TBPBE cathode exhibit comparatively low Tafel slopes but a lower Pt mass specific performance than the sputtered catalysts. Quantitative analyses of kinetic and mass-transport losses in the polarization curves suggest a competing microstructural effect, favoring mass-transport performance and an efficient oxygen reduction reaction for particle and continuous layer electrodes, respectively. The overall results suggest that in addition to the well-known promise of sputter-deposited Pt catalysts as an approach to increase Pt utilization at low loading, GLAD provides the unique ability to control Pt porosity and to achieve efficient reactant flow for high-currentdensity operation.