Corrosion Resistant Fuel Cell Substrates

Best Mode for Carrying on the Invention

A fuel cell electrode substrate was made by dry blending a mixture of 40% by weight powdered phenolic binder and 60% by weight of a carbonized natural fiber for about 10 minutes. The blended mixture was then showered in the air into a porous polytetrafluoroethylene coated fiberglass cloth with a vacuum drawn through the cloth. The mixture was deposited until a loading of approximately 225 g/m.sup.2 was achieved. The deposited web was then pressed to a thickness of about 25 mils at a temperature of 325.degree. F. for three minutes to thermoset the phenolic binder. The resulting composite was then heat treated in a nitrogen atmosphere to a final temperature of 1850.degree. F., at a rate of temperature increase of 8.degree. F. per hour to convert the phenolic binder to carbon. The carbonized body was then heat treated in a graphitizing furnace to a final temperature of 2850.degree. C. to graphitize the carbon fibers.

The resultant substrate was used as an example of a prior art substrate for comparing characteristics with substrates made in accordance with this invention.

A second fuel cell electrode substrate was made by forming a carbon fiber web from a carbonized natural fiber, using a conventional web paper-making process, with a polyvinyl alcohol binder fiber incorporated into the slurry. The web thus formed was dried and then saturated with a 10-15% by weight phenolic resin dispersed in a water carrier so as to add to the fiber web 50% by weight of the phenolic resin. The saturated web was then air dried for ten minutes at a temperature of 230.degree. F. The dried composite was then pressed, thermoset, and heat treated in the same manner as set forth in Example 1.

A third fuel cell electrode substrate was made by preparing a carbon fiber web as in Example 2. A 50% by weight phenolic binder dissolved in an organic solvent was impregnated into the web so as to saturate the latter with the dissolved binder. The saturated web was then dried, pressed, thermoset, and heat treated as in Example 2.

The physical characteristics of the three sample substrates are put forth in Table 1.

From the data set forth in Table 1, it is clear that the substrates of Examples 2 and 3, formed in accordance with this invention are significantly more corrosion resistant then the substrate formed in accordance with the prior art dry forming process.

In particular, the substrate saturated with the dissolved binder exhibits the best corrosion resistance characteristics. Scanning electron micrographs show that a consistent, uniform coating of the phenolic binder is obtained over the carbon fibers using the procedure of this invention. Substantially all of the inter-fiber junctures in the web are coated with the binder using the procedure of this invention. Preferred solvents for the phenolic binder are acetone, and low molecular weight alcohols.

In order to measure the electrical characteristics of a cell using substrates formed in accordance with this invention, a cell assembly was made as follows. Substrates for the 2 inch by 2 inch fuel cell performance test cell were prepared by carbonizing treated cotton fibers and forming these carbon fibers into a web via a wet papermaking process. The web was made to a basis weight of about 150 gm/m.sup.2. The resulting carbon fiber web was then saturated with a 12% by weight solution of phenolic resin dispersed in water to obtain a finished substrate having a 50% by weight resin content. The saturated paper was then dried at 230.degree. F. for 5-10 minutes to evaporate the water from the web, and leave the phenolic resin in place in the web. The dried sheet was then pressed to a constant thickness of 25 mils at 325.degree. F. for 3 minutes to thermoset the phenolic resin. The sheet was then heat treated as described in the aforesaid Example 1. The heat treated sheet was then catalyzed to serve as electrodes in a 2 inch by 2 inch fuel cell. The anode of the cell contained 1/4 mg of platinum /cm.sup.2, a 10% by weight platinum--Vulcan catalyst, a 50% by weight PTFE content, and a 1 mil thick silicon carbide matrix.

The cathode of the cell contained 1/2 mg of platinum /cm.sup.2, a GSB-18 catalyst, a PTFE content of 35% by weight, and a 1 mil thick silicon carbide matrix.

These cathode and anode plates were then paired with electrolyte reservoir plates, the cathode reservoir plate being a ribbed carbon-carbon plate with a mean pore size of 9 microns, and the anode reservior plates being a ribbed carbon-carbon plate with a mean pore size of 21 microns. Performance of the resultant cell was 685 MV at 200 ASF at 370 hrs using 70% H.sub.2 /29% CO.sub.2 /1% CO as the anode reactant, and air as the cathode reactant.

Table 2 is a comparison of the performance of the aforesaid cell with a typical cell whose substrates were formed with the prior art air layering technique.

From Table 1 and Table 2 it is readily apparent that the cell having the resin impregnated substrates in terms of performance is the equal of the prior art cell, and in terms of corrosion resistance, it is vastly superior. In addition to the improved resistance to corrosion, the substrate plates of this invention are stronger than the prior art plates.

It will be readily appreciated that the wet process of this invention could be used in a continuous production line mode to form substrates from a roll of the precursor carbon fiber paper. The paper from the roll could be fed through a bath of the wet binder, then to an evaporation station, and then into a belt press compaction and thermosetter. The sheet would then be cut into the desired plate sizes and heat treated to form the final product.

Since many changes and variations of the disclosed embodiments of the invention may be made without departing from the invention concept, it is not intended to limit the invention otherwise than as required by the appended claims.