Low cost fuel cell diffusion layer configured for optimized anode water management
A fuel cell comprises a cathode gas diffusion layer, a cathode catalyst layer, an anode gas diffusion layer, an anode catalyst layer and an electrolyte. The diffusion resistance of the anode gas diffusion layer when operated with anode fuel is higher than the diffusion resistance of the cathode gas diffusion layer. The anode gas diffusion layer may comprise filler particles having in-plane platelet geometries and be made of lower cost materials and manufacturing processes than currently available commercial carbon fiber substrates. The diffusion resistance difference between the anode gas diffusion layer and the cathode gas diffusion layer may allow for passive water balance control.
1. A fuel cell comprising:
a cathode gas diffusion layer;
a cathode catalyst layer;
an anode gas diffusion layer comprising a carbon fiber substrate comprising filler particles having in-plane platelet geometries;
an anode catalyst layer; and
an electrolyte in contact with the anode catalyst layer and the cathode catalyst layer to facilitate proton flow there between;
wherein the in-plane platelet geometries have an average largest in-plane dimension of at least 1.0 mm and
the diffusion resistance of the anode gas diffusion layer when operated with anode fuel for the anode feed stream is significantly higher than the diffusion resistance of the cathode gas diffusion layer.
2. The fuel cell of claim 1 wherein, the diffusion resistance of the anode gas diffusion layer when operated with anode fuel for the anode feed stream is at least 5 times higher than the diffusion resistance of the cathode gas diffusion layer.
3. The fuel cell of claim 1 wherein, the thermal resistance of the cathode gas diffusion layer and the thermal resistance of the anode gas diffusion layer are within 6 cm 2 K/W of the other.
4. The fuel cell of claim 1 wherein, the thermal resistance of the cathode gas diffusion layer and the thermal resistance of the anode gas diffusion layer are each in the range of approximately 5 cm 2 K/W to approximately 10 cm 2 K/W.
5. The fuel cell of claim 1 wherein, the electrical resistance of the cathode gas diffusion layer and the electrical conductivity of the anode gas diffusion layer are each less than 35 mOhm cm 2 at 0.6 MPa of compression.
6. The fuel cell of claim 1 wherein, the strain of the anode gas diffusion layer and the strain of the cathode gas diffusion layer are within 25% of each other when subjected to a compressive stress of about 2.07 MPa.
7. The fuel cell of claim 1 wherein, a carbonization temperature of the carbon fiber substrate is below 1000° C.
8. The fuel cell of claim 1 wherein, the carbon fiber substrate comprises less than 25% carbon fiber by mass.
9. The fuel cell of claim 1 wherein, the carbon fiber substrate is wet-laid.
10. The fuel cell of claim 1 wherein, the filler particles are graphite platelets and the carbon fiber substrate comprises greater than 50% graphite platelets by mass.
11. The fuel cell of claim 1 wherein, the in-plane platelet geometries have an average shortest in-plane dimension of at least 0.05 mm.
12. The fuel cell of claim 1 wherein, the output voltage at 1.5 A/cm 2 of the fuel cell varies by less than 5% for inlet relative humidity percentages of 40, 60, 80 and 100%.
13. The fuel cell of claim 1 wherein, the fuel cell further comprising an anode outlet and a cathode outlet has a water balance between the anode outlet and the cathode outlet shifted by at least 20% when compared to a comparative fuel cell comprising the cathode gas diffusion layer for both a comparative anode gas diffusion layer and a comparative cathode gas diffusion layer.
14. The fuel cell of claim 1 wherein, the fuel cell is configured for passive water balance.
15. A vehicle comprising the fuel cell of claim 1 , wherein the fuel cell serves as a source of motive power for the vehicle.
16. A fuel cell comprising:
an anode gas flow field having one or more channels for introducing a first gas to the fuel cell;
an anode gas diffusion layer in contact with the anode gas flow field;
an anode catalyst layer in contact with the anode gas diffusion layer;
a polymeric ion conductive membrane in contact with the anode catalyst layer;
a cathode catalyst layer in contact with the polymeric ion conductive membrane;
a cathode gas diffusion layer in contact with the cathode catalyst layer;
a cathode gas flow field having one or more cathode plane channels for introducing a second gas to the fuel cell, the cathode flow field being cooperative with the cathode diffusion layer;
wherein the diffusion resistance of the anode gas diffusion layer when operated with anode fuel for the anode feed stream is substantially higher than the diffusion resistance of the cathode gas diffusion layer, thermal resistance of the cathode gas diffusion layer and the thermal resistance of the anode gas diffusion layer are each in the range of approximately 5 cm 2 K/W to approximately 10 cm 2 K/W, the electrical resistance of the cathode gas diffusion layer and the electrical resistance of the anode gas diffusion layer are each less than 35 mOhm cm 2 at 0.6 MPa of compression, and the anode gas diffusion layer comprises a carbon fiber substrate comprising filler particles having in-plane platelet geometries with an average largest in-plane dimension of at least 1.0 mm.
17. The fuel cell of claim 16 wherein, a carbonization temperature of the carbon fiber substrate is below 1000° C.; the carbon fiber substrate comprises less than 25% carbon fiber by mass; and
an average shortest in-plane dimension of at least 0.05 mm.