An improved cathode structure on a membrane/electrode assembly has been developed for a direct methanol fuel cell, in a continuing effort to realize practical power systems containing such fuel cells. This cathode structure is intended particularly to afford better cell performance at a low airflow rate.
A membrane/electrode assembly of the type for which the improved cathode structure was developed (see Figure 1) is fabricated in a process that includes brush painting and spray coating of catalyst layers onto a polymer-electrolyte membrane and onto gas-diffusion backings that also act as current collectors. The aforementioned layers are then dried and hotpressed together. When completed, the membrane/electrode assembly contains (1) an anode containing a fine metal black of Pt/Ru alloy, (2) a membrane made of Nafion 117® or equivalent (a perfluorosulfonic acid-based hydrophilic, proton-conducting ion-exchange polymer), (3) a cathode structure (in the present case, the improved cathode structure described below), and (4) the electrically conductive gas-diffusion backing layers, which are made of Toray 060™ (or equivalent) carbon paper containing between 5 and 6 weight percent of poly(tetrafluoroethylene).
The need for an improved cathode structure arises for the following reasons: In the design and operation of a fuel-cell power system, the airflow rate is a critical parameter that determines the overall efficiency, cell voltage, and power density. It is desirable to operate at a low airflow rate in order to obtain thermal and water balance and to minimize the size and mass of the system. The performances of membrane/electrode assemblies of prior design are limited at low airflow rates. Methanol crossover increases the required airflow rate. Hence, one way to reduce the required airflow rate is to reduce the effect of methanol crossover. Improvement of the cathode structure — in particular, addition of hydrophobic particles to the cathode — has been demonstrated to mitigate the effects of crossover and decrease the airflow required.
The present improved cathode structure and the membrane/electrode assembly of which it is a part differ from prior such structures in the manner in which hydrophobic particles are distributed in the various layers and in the pretreatment of the membrane. The improved cathode is fabricated in a variant of the fabrication process summarized above. The major steps of this variant of the process as they affect the cathode are the following:
- The polymer-electrolyte membrane is roughened by use of a 600-grit-abrasive- coated paper.For a membrane area of 25 cm2, an ink comprising 0.18 g of Pt catalyst, 0.72 g of Nafion® (5 percent ionomer solution), and 0.40 g of water is applied to the abraded membrane surface by a paintbrush.
- Air is blown over the painted membrane surface to dry the ink.
- The gas-diffusion/ current-collecting carbon paper is brush-coated with an ink that contains the ingredients described for step 2, plus 0.035 g of poly(tetrafluoroethylene) particles.
- The membrane coated with catalyst layer is bonded to the gas-diffusion/ current-collecting carbon paper by use of heat and pressure.
The performance of membrane electrode assemblies prepared by the new process is compared with those prepared by the state-of-art (SOA) process in Figure 2. The current density at 0.49 V has been raised from 70 mA/cm2 to 100 mA/cm2. This results in an increase in power density of 43 percent. At an applied current density of 100 mA/cm2, the cell voltage for the SOA cell and improved cell are 0.43 and 0.49, respectively. The increase in cell voltage between the SOA and improved cell resulted in an increase in cell efficiency of 8 percent when the effects of crossover are included.
This work was done by Thomas Valdez and Sekharipuram Narayanan of Caltech for NASA’s Jet Propulsion Laboratory. For further information, access the Technical Support Package (TSP) free on-line at www.techbriefs.com/tsp under the Electronics/ Computers category.
In accordance with Public Law 96-517, the contractor has elected to retain title to this invention. Inquiries concerning rights for its commercial use should be addressed to:
Innovative Technology Assets Management
Mail Stop 202-233
4800 Oak Grove Drive
Pasadena, CA 91109-8099
Refer to NPO-30829, volume and number of this NASA Tech Briefs issue, and the page number.
This Brief includes a Technical Support Package (TSP).
Improved Cathode Structure for a Direct Methanol Fuel Cell
(reference NPO-30829) is currently available for download from the TSP library.
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