Fuel cell electrode substrate incorporating separator as an intercooler and process for preparation thereof

Claim 2

An electrode substrate for fuel cells comprising: (1) two porous carbonaceous layers, each having a number of elongated holes for feeding reactant gases into a fuel cell, which holes are defined near the center of the thickness thereof, and (2) a gas impermeable, carbonaceous separator interposed between said layers, having a number of elongated holes for flowing coolant, which holes are defined near the center of the thickness thereof; said two porous layers and said separator being integrated as a whole body by calcination, said separator excluding the elongated holes for flowing coolant having an average bulk density of about 1.2 g/cm 3 or more, a gas permeability of about 1×10 -4 cm 2 /hr.mmAq. or less, a thermal conductivity of about 1 kcal/m.hr.°C. or more and a specific resistance of about 10×10 -3 Ωcm or less; each said porous layer being a uniform monolayer and having an average bulk density in the range of about 0.4 to 0.8 g/cm 3 , a porosity in the range of about 50 to 80%, a gas permeability of about 20 ml/cm.hr. mmAq. or more and a thermal conductivity of about 0.7 kcal/m.hr.°C. or more, about 60% or more of the open pores of said porous layer having a diameter of about 100 microns or less.

Claim 3

The electrode substrate of claim 1, wherein said elongated holes for flowing coolant are parallel to each other, to an end face of the electrode, and to a side surface of the electrode, are continuously elongated in said separator from one side surface of the electrode to another side surface opposite thereto, and have the cross-sectional area as a circle having a diameter of about 2 to 10 mm.

Claim 4

The electrode substrate of claim 1, wherein said elongated holes for feeding reactant gases are parallel to each other, to an end face of the electrode, and to a side surface of the electrode, are continuously elongated in said porous layer from one side surface of the electrode to another side surface opposite thereto, and have the same cross-sectional area as a circle having a diameter of about 0.5 to 3 mm; said elongated holes in said porous layer on one side of said separator and those in said porous layer on the other side of said separator being disposed perpendicular to each other.

Claim 5

The electrode substrate of claim 1, wherein said calcination is carried out under an inert environment at a temperature in the range of about 800° to 3,000° C.

Claim 6

An electrode substrate for fuel cells comprising (1) two porous carbonaceous layers and (2) a gas impermeable, carbonaceous separator interposed between said layers, having a number of elongated holes for flowing coolant, which holes are defined near the center of the thickness of said separator; said two porous layers and said separator being integrated as a whole body by calcination; said separator excluding said elongated holes for flowing coolant having an average bulk density of about 1.2 g/cm 3 or more, a gas permeability of about 1×10 -4 cm 2 /hr.mmAq. or less, a thermal conductivity of about 1 kcal/m.hr.°C. or more and a specific resistance of about 10×10 -3 Ωcm or less; each of said porous layers having a two layer structure, said two layer structure comprising a first porous layer and a second porous layer and elongated holes for feeding reactant gases defined between said first porous layer and said second porous layer, said second porous layer having a bulk density larger than that of said first porous layer and being adjacent to said separator; said first porous layer having an average bulk density of about 0.4 to 0.8 g/cm 3 , a porosity of about 50 to 80%, a gas permeability of about 20 ml/cm.hr.mmAq. or more and a thermal conductivity of about 0.7 kcal/m.hr.°C. or more, about 60% or more of the open pores of said first porous layer having a diameter of about 100 microns or less, and said second porous layer having an average bulk density of about 0.5 to 1.0 g/cm 3 and a thermal conductivity of about 0.9 kcal/m.hr.°C. or more.

Claim 7

An electrode substrate for fuel cells comprising (1) two porous carbonaceous layers and (2) a gas impermeable, carbonaceous separator interposed between said layers, having a number of elongated holes for flowing coolant, which holes are defined near the center of the thickness of said separator; said two porous layers and said separator being integrated as a whole body by calcination; said separator excluding said elongated holes for flowing coolant having an average bulk density of about 1.2 g/cm 3 or more, a gas permeability of about 1×10 -4 cm 2 /hr.mmAq. or less, a thermal conductivity of about 1 kcal/m.hr.°C. or more and a specific resistance of about 10×10 -3 Ωcm or less; each of said porous layers having a two layer structure, said two layer structure comprising a first porous layer and a second porous layer and elongated holes for feeding reactant gases defined between said first porous layer and said second porous layer, said second porous layer having a bulk density larger than that of said first porous layer and being adjacent to said separator; said first porous layer having an average bulk density of about 0.4 to 0.8 g/cm 3 , a porosity of about 50 to 80%, a gas permeability of about 20 ml/cm.hr.mmAq. or more and a thermal conductivity of about 0.7 kcal/m.hr.°C. or more, about 60% or more of the open pores of said first porous layer having a diameter of about 100 microns or less, and said second porous layer having an average bulk density of about 0.5 to 1.0 g/cm 3 and a thermal conductivity of about 0.9 kcal/m.hr.°C. or more.

Claim 8

The electrode substrate of claim 5, wherein the thickness of said first porous layer is in the range of about a fiftieth to a half of the total thickness of said porous carbonation layer.

Claim 9

The electrode substrate of claim 5, wherein said elongated holes for flowing coolant are parallel to each other, to an end face of the electrode, and to a side surface of the electrode, are continuously elongated in said separator from one side surface of the electrode to another side surface opposite thereto, and have the same cross-section area as a circle having a diameter of about 2 to 10 mm.

Claim 10

The electrode substrate of claim 5, wherein said elongated holes for feeding reactant gases are parallel to each other, to an end face of the electrode, and to a side surface of the electrode, are continuously elongated in said porous layer from one side surface of the electrode to another side surface opposite thereto, and have the same cross-sectional area as a circle having a diameter of about 0.5 to 3 mm; said elongated holes in said porous layer on one side of said separator and those in said porous layer on the other side of said separator being disposed perpendicular to each other.

Claim 11

An electrode substrate for fuel cells comprising (1) two porous carbonaceous layers, each having a number of elongated holes for feeding reactant gases into a fuel cell, which holes are defined near the center of the thickness thereof, and (2) a separator; said two porous layers and said separator being integrated as a whole body by calcination; each said porous layer being a uniform monolayer and having an average bulk density in the range of from about 0.4 to 0.8 g/cm 3 , a porosity in the range of about 50 to 80%, a gas permeability of about 20 ml/cm.hr.mmAq. or more and a thermal conductivity of about 0.7 kcal/m.hr.°C. or more, about 60% or more of the open pores of said porous layer having a diameter of about 100 microns or less, said separator comprising a gas impermeable, carbonaceous separator plate and two pairs of gas impermeable, carbonaceous peripheral sealing members, a number of elongated holes for flowing coolant being provided near the center of the thickness of said separator plate, each pair of said members being on either side of said separator plate, the longitudinal direction of one pair of said members being perpendicular to that of the other pair of said members; said separator excluding said elongated holes having a gas permeability in the direction of the thickness of about 10 -4 cm 2 /hr.mmAq. or lower, bending strength of about 500 kg/cm 2 or higher, a thermal conductivity of about 4 kcal/m.hr.°C. or higher and an electric resistance of about 100 mΩ.cm or lower, said peripheral sealing member having a gas permeability in the direction towards a side surface of said separator of 10 -2 cm 2 /hr.mmAq. or less.

Claim 12

An electrode substrate for fuel cells comprising (1) two porous carbonaceous layers, each having a number of elongated holes for feeding reactant gases into a fuel cell, which holes are defined near the center of the thickness thereof, and (2) a separator; said two porous layers and said separator being integrated as a whole body by calcination; each said porous layer being a uniform monolayer and having an average bulk density in the range of from about 0.4 to 0.8 g/cm 3 , a porosity in the range of about 50 to 80%, a gas permeability of about 20 ml/cm.hr.mmAq. or more and a thermal conductivity of about 0.7 kcal/m.hr.°C. or more, about 60% or more of the open pores of said porous layer having a diameter of about 100 microns or less, said separator comprising a gas impermeable, carbonaceous separator plate and two pairs of gas impermeable, carbonaceous peripheral sealing members, a number of elongated holes for flowing coolant being provided near the center of the thickness of said separator plate, each pair of said members being on either side of said separator plate, the longitudinal direction of one pair of said members being perpendicular to that of the other pair of said members; said separator excluding said elongated holes having a gas permeability in the direction of the thickness of about 10 -4 cm 2 /hr.mmAq. or lower, bending strength of about 500 kg/cm 2 or higher, a thermal conductivity of about 4 kcal/m.hr.°C. or higher and an electric resistance of about 100 mΩ.cm or lower, said peripheral sealing member having a gas permeability in the direction towards a side surface of said separator of 10 -2 cm 2 /hr.mmAq. or less.

Claim 13

The electrode substrate of claim 9, wherein said peripheral sealing member has a height of about 2.5 mm or less.

Claim 14

The electrode substrate of claim 9, wherein said separator has been calcinated at about 100° C. or more.

Claim 15

The electrode substrate of claim 9, wherein said elongated holes for flowing coolant are parallel to each other to an end face of the electrode, and to a side surface of the electrode, are continuously elongated in said separator from one side surface of the electrode to another side surface opposite thereto. and have the same cross-sectional area as a circle having a diameter of about 2 to 10 mm.

Claim 16

The electrode substrate of claim 9, wherein said elongated holes for feeding reactant gases are parallel to each other, to an end face of the electrode, and to a side surface of the electrode, are continuously elongated in said porous layer from one side surface of the electrode to another side surface opposite thereto, and have the same cross-sectional area as a circle having a diameter of about 0.5 to 3 mm; said elongated holes in said porous layer on on one side of said separator and those in said porous layer on the other side of said separator being disposed perpendicular to each other.