Method of producing fuel cell separator, fuel separator, and polymer electrolyte fuel cell
Abstract
Disclosed are a method of producing a fuel cell separator. In this method, dry granules of a composition for a fuel cell separator mainly containing a conductive material, a binder, and an additive are produced by mixing raw materials including at least the conductive material, the binder, and the additive, granulating the resultant mixture to obtain granules, and drying the granules. The dry granules may be further sized. Then, the granules are packed in a mold, and hot-press molded. This method is characterized in that the granules have a residual volatile matter content in a range of 4 wt % or less, and an average particle size in a range of 200 to 700 μm (60 to 160 μm for the sized granules) and a specific particle size distribution. With this method, a fuel cell separator having a high elasticity, an excellent dimensional accuracy, and a high gas non-permeability can be produced with no molding failures, accordingly, with a uniform quality. Further, a solid polymer electrolyte fuel cell having a high gas sealing characteristic and an excellent impact resistance can be produced by using the above high quality fuel cell separators as part or all of separators in the fuel cell.
Claims
exact text as granted — not AI-modified1 . A fuel cell separator having a gas permeability, measured by a method B specified under JIS K7126, in a range of 30 cc/m 2 ·24 hr·atm or less, said fuel cell separator being produced by a method comprising the steps of:
producing dry granules of a composition for a fuel cell separator mainly containing a conductive material, a binder, and an additive by mixing raw materials including at least said conductive material, said binder, and said additive, granulating the resultant mixture to obtain granules, and drying the granules; and
packing said dry granules in a mold, and hot-press molding said dry granules packed in the mold;
wherein a residual volatile matter content of said dry granules is in a range of 4 wt % or less;
an average particle size of said dry granules is in a range of 200 to 700 μm; and
a particle size distribution of said dry granules is as follows:
particle size percentage 5 μm or more and less than 100 μm 5 to 30% 100 μm or more and less than 300 μm 10 to 40% 300 μm or more and less than 500 μm 10 to 50% 500 μm or more and less than 1000 μm balance
2 . A fuel cell separator having a gas permeability, measured by a method B specified under JIS K7126, in a range 30 of 30 cc/m 2 ·24 hr·atm or less, said fuel cell separator being produced by a method comprising the steps of:
producing sized dry granules of a composition for a fuel cell separator mainly containing a conductive material, a binder, and an additive by mixing raw materials including 35 at least said conductive material, said binder, and said additive, granulating the resultant mixture to obtain granules, drying the granules, and sizing the dry granules; and
packing said sized dry granules in a mold, and hot-press molding said sized dry granules packed in the mold:
wherein a residual volatile matter content of said sized dry granules is in a range of 4 wt % or less;
an average particle size of said sized dry granules is in a range of 60 to 160 μm; and
a particle size distribution of said sized dry granules is as follows:
particle size percentage 5 μm or more and less than 100 μm 10 to 80% 100 μm or more and less than 300 μm 10 to 40% 300 μm or more and less than 500 μm balance
3 . A fuel cell separator having a gas permeability, measured by a method B specified under JIS K7126, in a range of 30 cc/m 2 ·24 hr·atm or less, said fuel cell separator
being produced by a method comprising the steps of:
producing dry granules of a composition for a fuel cell separator mainly containing a conductive material, a binder, and an additive by mixing raw materials including at least said conductive material, said binder, and said additive, granulating the resultant mixture to obtain granules, and drying the granules; and
packing said dry granules in a mold, and hot-press molding said dry granules packed in the mold:
wherein said step of mixing raw materials including at least said conductive material, said binder, and said additive comprises the steps of:
adding and mixing said additive to and with said conductive material, to obtain a sub-mixture;
adding said binder to said sub-mixture in an amount of 5 to 30 parts by mass on the basis of 100 parts by mass of said conductive material and simultaneously adding a solvent to said sub-mixture in an amount of 20 parts by mass or less on the basis of 100 parts by mass of said conductive material; and
wet-mixing said sub-mixture with said binder and said solvent.
4 . A fuel cell separator having a gas permeability, measured by a method B specified under JIS K7126, in a range of 30 cc/m 2 ·24 hr·atm or less, said fuel cell separator being produced by a method comprising the steps of:
producing sized dry granules of a composition for a fuel cell separator mainly containing a conductive material, a binder, and an additive by mixing raw materials including at least said conductive material, said binder, and said additive, granulating the resultant mixture to obtain
granules, drying the granules, and sizing the dry granules; and
packing said sized dry granules in a mold, and hot-press molding said sized dry granules packed in the mold; wherein said step of raw materials including at least said conductive material, said binder, and said additive comprises the steps of:
adding and mixing said additive to and with said conductive material, to obtain a sub-mixture:
adding said binder to said sub-mixture in an amount of 5 to 30 parts by mass on the basis of 100 parts by mass of said conductive material and simultaneously adding a solvent to said sub-mixture in an amount of 20 parts by mass or less on the basis of 100 parts by mass of said conductive material, and
wet-mixing said sub-mixture with said binder and said solvent.
5 . A fuel cell separator according to any one of claims 1 to 4 , wherein said step of drying the granules is carried out by a vacuum drying method, a fluid bed drying method, a jet drier method, or an elevated temperature drying method.
6 . A fuel cell separator according to claim 1 , wherein said conductive material is a powder of graphite which has an average particle size ranging from 10 to 80 μm.
7 . A polymer electrolyte fuel cell comprising:
a plurality of unit cells juxtaposed, each of which has a pair of electrodes disposed with a polymer electrolyte membrem put therebetween, and a pair of separators disposed with said electrodes put therebetween and shaped to form gas supply/discharge passages between said separators and said electrodes; wherein part or all of said separators in said fuel cell are composed of fuel cell separators each of which has a gas permeability, measured by a method B specified under JIS K7126, in a range of 30 cc/m 2 ·24 hr·atm or less, and which is produced by a method comprising the steps of: producing dry granules of a composition for a fuel cell separator mainly containing a conductive material, a binder, and an additive by mixing raw materials including at least said conductive material, said binder, and said additive, granulating the resultant mixture to obtain granules, and drying the granules; and packing said dry granules in a mold, and hot-press molding said dry granules packed in the mold; wherein a residual volatile matter content of said dry granules is in a range of 4 wt % or less: an average particle size of said dry granules is in a range of 200 to 700 μm; and a particle size distribution of said dry granules is as follows: particle size percentage 5 μm or more and less than 100 μm 5 to 30% 100 μm or more and less than 300 μm 10 to 40% 300 μm or more and less than 500 μm 10 to 50% 500 μm or more and less than 1000 μm balance
8 . A polymer electrolyte fuel cell comprising:
a plurality of unit cells juxtaposed, each of which has a pair of electrodes disposed with a polymer electrolyte membrem put therebetween, and a pair of separators disposed with said electrodes put therebetween and shaped to form gas supply/discharge passages between said separators and said electrodes: wherein part or all of said separators in said fuel cell are composed of fuel cell separators each of which has a gas permeability, measured by a method B specified under JIS K7126, in a range of 30 cc/m 2 ·24 hr·atm or less, and which is produced by a method comprising the steps of: producing sized dry granules of a composition for a fuel cell separator mainly containing a conductive material, a binder, and an additive by mixing raw materials including at least said conductive material, said binder, and said additive, granulating the resultant mixture to obtain granules, drying the granules, and sizing the dry granules; and packing said sized dry granules in a mold, and hot-press molding said sized dry granules packed in the mold; wherein a residual volatile matter content of said sized dry granules is in a range of 4 wt % or less; an average particle size of said sized dry granules is in a range of 60 to 160 μm; and a particle size distribution of said sized dry granules is as follows: particle size percentage 5 μm or more and less than 100 μm 10 to 80% 100 μm or more and less than 300 μm 10 to 40% 300 μm or more and less than 500 μm balance
9 . A polymer electrolyte fuel cell comprising:
a plurality of unit cells juxtaposed, each of which has a pair of electrodes disposed with a polymer electrolyte membrem put therebetween, and a pair of separators disposed with said electrodes put therebetween and shaped to form gas supply/discharge passages between said separators and said electrodes; wherein part or all of said separators in said fuel cell are composed of fuel cell separators each of which has a gas permeability, measured by a method B specified under JIS K7126, in a range of 30 cc/m 2 ·24 hr·atm or less, and which is produced by a method comprising the steps of: producing dry granules of a composition for a fuel cell separator mainly containing a conductive material, a binder, and an additive by mixing raw materials including at least said conductive material, said binder, and said additive, granulating the resultant mixture to obtain granules, and drying the granules; and
packing said dry granules in a mold, and hot-press molding said dry granules packed in the mold:
wherein said step of mixing raw materials including at least said conductive material, said binder, and said additive comprises the steps of:
adding and mixing said additive to and with said conductive material, to obtain a sub-mixture;
adding said binder to said sub-mixture in an amount of 5 to 30 parts by mass on the basis of 100 parts by mass of said conductive material and simultaneously adding a solvent to said sub-mixture in an amount of 20 parts by mass or less on the basis of 100 parts by mass of said conductive material; and
wet-mixing said sub-mixture with said binder and said solvent.
10 . A polymer electrolyte fuel cell comprising:
a plurality of unit cells juxtaposed, each of which has a pair of electrodes disposed with a polymer electrolyte membrem put therebetween, and a pair of separators disposed with said electrodes put therebetween and shaped to form gas supply/discharge passages between said separators and said electrodes:
wherein part or all of said separators in said fuel cell are composed of fuel cell separators each of which has
a gas permeability, measured by a method B specified under JIS K7126, in a range of 30 cc/m 2 ·24 hr·atm or less, and which is produced by a method comprising the steps of:
producing sized dry granules of a composition for a fuel cell separator mainly containing a conductive material, a binder, and an additive by mixing raw materials including at least said conductive material, said binder, and said additive, granulating the resultant mixture to obtain granules, drying the granules, and sizing the dry granules; and packing said sized dry granules in a mold, and hot-press molding said sized dry granules packed in the mold; wherein said step of raw materials including at least said conductive material, said binder, and said additive comprises the steps of: adding and mixing said additive to and with said conductive material, to obtain a sub-mixture; adding said binder to said sub-mixture in an amount of 5 to 30 parts by mass on the basis of 100 parts by mass of said conductive material and simultaneously adding a solvent to said sub-mixture in an amount of 20 parts by mass or less on the basis of 100 parts by mass of said conductive material; and wet-mixing said sub-mixture with said binder and said solvent.
11 . A polymer electrolyte fuel cell according to any one of claims 7 to 10 , wherein said step of drying the granules is carried out by a vacuum drying method, a fluid bed drying method, a jet drier method, or an elevated temperature drying method.
12 . A polymer electrolyte fuel cell according to claim 7 , wherein said conductive material is a powder of graphite which has an average particle size ranging from 10 to 80 μm.Join the waitlist — get patent alerts
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