DIRECT OXIDATION FUEL CELL AND METHOD FOR PRODUCING CATALYST-COATED MEMBRANE USED THEREFOR
A direct oxidation fuel cell with high catalyst utilization efficiency and excellent power generation characteristics. The unit cell includes: a membrane-electrode assembly including an anode, a cathode, and an electrolyte membrane interposed therebetween; and anode-side and cathode-side separators being in contact with the anode and cathode, respectively. The anode and cathode each includes a catalyst layer disposed on one principal surface of the electrolyte membrane. At least one of the anode and cathode catalyst layers has a center portion and a peripheral portion surrounding the center portion. The catalyst amounts C 2b and C 2c per unit projected area of regions facing the midstream and downstream of the flow channel of the separator within the peripheral portion are each smaller than the catalyst amount C 1 per unit projected area of the center portion.
1 . A direct oxidation fuel cell having at least one unit cell, the unit cell comprising: a membrane-electrode assembly including an anode, a cathode, and an electrolyte membrane interposed between the anode and the cathode; an anode-side separator being in contact with the anode; and a cathode-side separator being in contact with the cathode,
the anode-side separator having a supply port for supplying fuel therethrough, and a fuel flow channel extending from the supply port,
the cathode-side separator having a supply port for supplying oxidant therethrough, and an oxidant flow channel extending from the supply port,
the fuel flow channel and the oxidant flow channel each having an upstream portion continued from the supply port, a midstream portion continued from the upstream portion, and a downstream portion continued from the midstream portion,
the anode including an anode catalyst layer disposed on one principal surface of the electrolyte membrane, and an anode diffusion layer being laminated on the anode catalyst layer and being in contact with the anode-side separator,
the cathode including a cathode catalyst layer disposed on the other principal surface of the electrolyte membrane, and a cathode diffusion layer being laminated on the cathode catalyst layer and being in contact with the cathode-side separator,
the anode catalyst layer and the cathode catalyst layer each including a catalyst and a polymer electrolyte,
the anode catalyst layer facing the upstream portion, the midstream portion, and the downstream portion of the fuel flow channel,
the cathode catalyst layer facing the upstream portion, the midstream portion, and the downstream portion of the oxidant flow channel,
at least one of the anode catalyst layer and the cathode catalyst layer having a center portion and a peripheral portion surrounding the center portion, and
a catalyst amount C 2b per unit projected area of a region facing the midstream portion within the peripheral portion and a catalyst amount C 2c per unit projected area of a region facing the downstream portion within the peripheral portion each being smaller than a catalyst amount C 1 per unit projected area of the center portion.
2 . The direct oxidation fuel cell according to claim 1 , wherein ratios C 2b /C 1 and C 2c /C 1 of the catalyst amount C 2b and the catalyst amount C 2c to the catalyst amount C 1 are each 0.2 or more and 0.8 or less.
3 . The direct oxidation fuel cell according to claim 1 , wherein a ratio C 2a /C 1 of a catalyst amount C 2a per unit projected area of a region facing the upstream portion within the peripheral portion to the catalyst amount C 1 is 0.95 or more and 1.05 or less.
4 . The direct oxidation fuel cell according to claim 1 , wherein the catalyst amount C 2a per unit projected area of a region facing the upstream portion within the peripheral portion, the catalyst amount C 2b , and the catalyst amount C 2c satisfy the following relationship:
C 2a >C 2b ≧C 2c .
5 . The direct oxidation fuel cell according to claim 1 , wherein a ratio of a total projected area of the regions facing the midstream portion and the downstream portion within the peripheral portion to a total projected area of the center portion and the peripheral portion is 0.1 or more and 0.51 or less.
6 . The direct oxidation fuel cell according to claim 1 , wherein:
the anode catalyst layer has the center portion and the peripheral portion, and includes electrically conductive carbon particles, an anode catalyst supported on the conductive carbon particles, and a polymer electrolyte; and
the catalyst amount C 1 is 1 mg/cm 2 or more and 4 mg/cm 2 or less.
7 . The direct oxidation fuel cell according to claim 1 , wherein:
the cathode catalyst layer has the center portion and the peripheral portion, and includes electrically conductive carbon particles, a cathode catalyst supported on the conductive carbon particles, and a polymer electrolyte; and
the catalyst amount C 1 is 0.8 mg/cm 2 or more and 2 mg/cm 2 or less.
8 - 10 . (canceled)