High thermal conductivity gas feeder system

Claim 2

A gas ducting system for a plurality of electrochemical cells, said gas ducting system comprising at least one compressible insulating separator disposed between two thermally and electrically conducting manifolding gas means, the manifolding gas means comprising at least one hollow conduit attached to a hollow subheader, both communicating gas therethrough, where the subheader is attached to a manifold segment contacting the separator, and where the two manifolding gas means and insulating separator are compressed together by a compressing means to provide a sealed gas system communicating to the cells.

Claim 3

The gas feeder system of claim 1, where the manifolding gas inlet means are made of metal, and the insulating separator is ceramic material.

Claim 4

The gas feeder system of claim 1, where the conduits have extending exterior metal alloy fins.

Claim 5

The gas feeder system of claim 1, where the conduits have an exterior metal alloy helical wire wrapping.

Claim 6

The gas feeder system of claim 1, where the conduits have a metal alloy twisted ribbon disposed within the interior volume.

Claim 7

The gas feeder system of claim 2, where the conduits are made of an alloy containing nickel and chromium, having a thermal conductivity of over about 13 Btu-ft./sq.ft.-hr.-°F. at 1500° F., and the electrochemical cells are high temperature fuel cells.

Claim 8

The gas feeder system of claim 2, where the electrochemical cells are solid oxide electrolyte fuel cells arranged in a series-parallel electrical connection array, where the conduits contact the inside of the fuel cells providing parallel electrical interconnection.

Claim 9

The gas feeder system of claim 7, where the fuel cells and gas feeder system are disposed within a fuel cell generator operating at a temperature of between about 500° C. and 1100° C. with air being fed through the gas feeder system and into the interior of the fuel cells as oxidant, and fuel gas being fed into the generator to flow about the outside of the fuel cells, where the stoichiometric ratio of air:fuel gas is over 3.5:1, providing an oxidizing environment.

Claim 10

A fuel cell generator comprising a plurality of fuel cells, oxidant manifold feed means comprising alternating metal portions and insulating portions, the metal portions containing a plurality of elongated, metal, oxidant feed conduits, which conduits extend into each of said plurality of fuel cells, and means defining a preheating chamber and a fuel inlet generating chamber where the fuel cells are disposed within the fuel inlet generating chamber, where said oxidant feed conduits comprise a metal resistant to oxidizing gas and pass through the preheating chamber, and where oxidant gas is sealed within the manifold feed means and the oxidant feed conduits so that there is no oxidant entry into the preheating chamber before passage into the fuel cell.

Claim 11

A fuel cell generator comprising a plurality of fuel cells, oxidant manifold feed means comprising alternating metal portions and insulating portions, the metal portions containing a plurality of elongated, metal, oxidant feed conduits, which conduits extend into each of said plurality of fuel cells, and means defining a preheating chamber and a fuel inlet generating chamber where the fuel cells are disposed within the fuel inlet generating chamber, where said oxidant feed conduits comprise a metal resistant to oxidizing gas and pass through the preheating chamber, and where oxidant gas is sealed within the manifold feed means and the oxidant feed conduits so that there is no oxidant entry into the preheating chamber before passage into the fuel cell.

Claim 12

The fuel cell generator of claim 9, where the fuel cells are of elongated tubular construction, comprise an inner electrode, an outer electrode and a solid oxide electrolyte between said electrodes and are arranged in a series-parallel electrical connection array with the metal conduits contacting the inside of the fuel cells providing parallel electrical interconnection, and where metal felts contact the outside of series connected fuel cells providing series electrical interconnection, where the fuel cell generator operates at a temperature of between about 500° C. and about 1100° C., and where the preheating chamber contains a mixture of depleted oxidant and depleted fuel gases.

Claim 13

The fuel cell generator of claim 9, where gaseous fuel enters the fuel inlet generating chamber, contacting the outside of the fuel cells where it is depleted, the oxidant is air which contacts the inside of the fuel cells where it is depleted, where the depleted fuel and air contact each other in the preheating chamber, and where the stoichiometric ratio of air:fuel is over 3.5:1 providing an oxidizing environment.

Claim 14

The fuel cell generator of claim 9, where the manifold feed means are made of a metal alloy, the insulating portion is a compressible ceramic material separator.

Claim 15

The fuel cell generator of claim 9, where the conduits have extending exterior metal alloy fins.

Claim 16

The fuel cell generator of claim 9, where the conduits have an exterior metal alloy helical wire wrapping.

Claim 17

The fuel cell generator of claim 9, where the conduits have a metal alloy twisted ribbon disposed within the interior volume.

Claim 18

The fuel cell generator of claim 12, where the conduits are made of an alloy containing nickel and chromium, having a thermal conductivity of over about 13 Btu-ft./sq.ft.-hr°F. at 1500° F.

Claim 19

A high temperature solid electrolyte fuel cell generator comprising: (1) a housing means defining a fuel inlet generating chamber and a preheating chamber; (2) a gas porous material separating said fuel inlet generating chamber and preheating chamber; (3) a plurality of elongated tubular fuel cells, each having an electrochemically active length, comprising an inner electrode, an outer electrode and a solid oxide electrolyte between said electrodes, disposed within said fuel inlet generating chamber; (4) oxidant manifold feed means, comprising alternating metal portions and insulating portions, the metal portions communicating with a plurality of metal, elongated, tubular oxidant feed conduits which extend into each of said plurality of fuel cells, providing a means for flowing oxidant gas into said fuel cells and into said preheating chamber, where said oxidant feed conduits are made of a metal alloy resistant to oxidizing gas; and (5) means for flowing a fuel gas into said fuel inlet generating chamber, about said fuel cells, and through said gas porous material into said preheating chamber; where oxidant gas is sealed within the manifold feed means and the oxidant feed conduits so that there is no oxidant entry into the preheating chamber before passage into the fuel cells.

Claim 20

A high temperature solid electrolyte fuel cell generator comprising: (1) a housing means defining a fuel inlet generating chamber and a preheating chamber; (2) a gas porous material separating said fuel inlet generating chamber and preheating chamber; (3) a plurality of elongated tubular fuel cells, each having an electrochemically active length, comprising an inner electrode, an outer electrode and a solid oxide electrolyte between said electrodes, disposed within said fuel inlet generating chamber; (4) oxidant manifold feed means, comprising alternating metal portions and insulating portions, the metal portions communicating with a plurality of metal, elongated, tubular oxidant feed conduits which extend into each of said plurality of fuel cells, providing a means for flowing oxidant gas into said fuel cells and into said preheating chamber, where said oxidant feed conduits are made of a metal alloy resistant to oxidizing gas; and (5) means for flowing a fuel gas into said fuel inlet generating chamber, about said fuel cells, and through said gas porous material into said preheating chamber; where oxidant gas is sealed within the manifold feed means and the oxidant feed conduits so that there is no oxidant entry into the preheating chamber before passage into the fuel cells.

Claim 21

The fuel cell generator of claim 17, where the fuel cell generator operates at a temperature of between about 500° C. and about 1100° C., the oxidant is air, the stoichiometric ratio of air:fuel is over 3.5:1 providing an oxidizing environment, the fuel and air are depleted by contact with the fuel cell and the depleted fuel and air contact and mix with each other in the preheating chamber.

Claim 22

The fuel cell generator of claim 17, where the conduits are made of an alloy containing nickel and chromium alloy having a thermal conductivity of over about 13 Btu-ft./sq.ft.-hr.-°F. at 1500° F.

Claim 23

The fuel cell generator of claim 17, where the conduits have extending exterior metal alloy fins.

Claim 24

The fuel cell generator of claim 17, where the conduits have an exterior metal alloy helical wire wrapping.

Claim 25

The fuel cell generator of claim 17, where the conduits have a metal alloy twisted ribbon disposed within the interior volume.

Claim 26

The fuel cell generator of claim 17, where the fuel cells are arranged in a series-parallel electrical connection array with the metal conduits contacting the inside of the fuel cells providing parallel electrical interconnection and metal felts contacting the outside of series connected fuel cells providing series electrical interconnection.