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Transport in PEMFC Stacks - DOE Hydrogen and Fuel Cells ...

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Achievements: Design of Gas Diffusion Media<br />

Comparison of Mercury pore size distributions of new design GDLs<br />

Cumulative Intrusion Volume (mL/g)<br />

Incremental Intrusion Volume (mL/g)<br />

4.5<br />

4<br />

3.5<br />

3<br />

2.5<br />

2<br />

1.5<br />

1<br />

0.5<br />

0<br />

0.001 0.01 0.1 1 10 100 1000<br />

Pore Size Diameter (µm)<br />

1.4<br />

1.2<br />

1<br />

0.8<br />

0.6<br />

0.4<br />

0.2<br />

Basel<strong>in</strong>e Substrates<br />

EP40T<br />

P50T<br />

P75T<br />

EP40T<br />

P50T<br />

P75T<br />

0<br />

0.001 0.01 0.1 1 10 100 1000<br />

Pore Size Diameter (µm)<br />

Cumulative Intrusion Volume (mL/g)<br />

Incremental Intrusion Volume (mL/g)<br />

2.5<br />

2<br />

1.5<br />

Cumulative pore volume<br />

1<br />

0.5<br />

0<br />

0.001 0.01 0.1 1 10 100 1000<br />

Pore Size Diameter (µm)<br />

0.7<br />

0.6<br />

0.5<br />

0.4<br />

0.3<br />

0.2<br />

0.1<br />

P50T_basel<strong>in</strong>e<br />

P50_Low<br />

P50_High<br />

Differential pore volume<br />

Modified Substrates<br />

P50T_basel<strong>in</strong>e<br />

P50_Low<br />

P50_High<br />

0<br />

0.001 0.01 0.1 1 10 100 1000<br />

Pore Size Diameter (µm)<br />

This presentation does not conta<strong>in</strong> any proprietary, confidential,<br />

or otherwise restricted <strong>in</strong>formation<br />

EP40T has largest<br />

pore volume,<br />

concentrated at 50<br />

µm<br />

Modification greatly<br />

reduces volume of<br />

large pores<br />

14

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