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The optimum cp for the maximum cell performance was around 0.1 0.2 M.
It was found that there existed optimal values of electrode pore size and porosity for maximum cell performance.
For maximum cell performance, we found that the pore volume in the 3D cathode needs to be larger to have better oxygen diffusion but overly porous cathodes have less effective electrical conductivity, resulting in lower power generation.
At high Pt loading, the cell performance is not as sensitive to the Pt loading, and the ordered structures must be carefully optimized to obtain the maximum cell performance.
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Maximum fuel cell performance was obtained utilizing a microporous layer with carbon loading of 1.0 mg cm−2 when air was used as an oxidant.
The optimum temperature for attaining the maximum fuel cell performance was at 75 °C while it reduced by decreasing the temperature to 50 °C or increasing it to 85 °C.
The cell performance maximum through increasing electron density at counter electrode surface to enhance its catalytic ability is still a challenging problem.
Since the mixing and depletion widths are major factors that determine the cell performance, maximum Reynolds and Péclet numbers as well as fuel utilization are considered as variables of comparison.
The cell performance is maximum at 2 M of electrolyte concentration obtained at 9.24 W/cm2, and lowest at 0.5 M was 6.48 W/cm2.
Single cell tests have shown that the membrane has a moderate fuel cell performance with maximum power density of 300 mW/cm−2 at 40 °C and 80% RH, 400 mW/cm−2 at 60 °C and 80% RH.
Given design ranges, results show that the cell performance is maximum when the two top metal layers and the bottom metal electrode become thinner while the bottom metal contact becomes thicker.
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