Fuel cell power generation system

Claim 2

A fuel cell power generation system comprising: a reforming reactor for reacting fuel and water in a reforming reaction to produce a reformed gas containing hydrogen and carbon monoxide; CO shift reactor for subjecting said reformed gas to a CO shift reaction to decrease concentration of carbon monoxide in said reformed gas; CO removal means for oxidizing carbon monoxide in said reformed gas, exiting said CO shift reactor, to carbon dioxide; a fuel cell for generating electric power by reaction of a gaseous oxidizing agent and said reformed gas having been subjected to the shift reaction and the oxidizing reaction; power output determining means for determining an output power value required from said fuel cell to meet a load demand; space velocity determining means for determining a space velocity for feed of said reformed gas to said CO removal means, in accordance with the determined output value; and regulating means for regulating the feed of reformed gas to the CO removal means responsive to the determined space velocity.

Claim 3

The fuel cell power generation system according to claim 1, wherein said reforming reactor contains a supported reforming catalyst.

Claim 4

The fuel cell power generation system according to claim 1, wherein said CO removal means has plural reaction chambers separated by partition plates which are gas barriers and which are heat conductive.

Claim 5

The fuel cell power generation system according to claim 3, wherein said each reaction chamber is composed of a reaction section containing a selective-oxidizing catalyst and a cooling section for receiving cooling water to maintain the temperature of said selective-oxidizing catalyst within a predetermined temperature range.

Claim 6

The fuel cell power generation system according to claim 4, wherein said reaction section is L-shaped in cross-section.

Claim 7

The fuel cell power generation system according to claim 4, wherein said regulating means includes a plurality of valves, each valve opening or closing one reaction section whereby said regulating means regulates the number of reaction sections receiving the reformed gas.

Claim 8

A fuel cell power generating process comprising: reacting a fuel with water in gas phase in a reforming reaction to produce a reformed gas including carbon monoxide at a first concentration and hydrogen; feeding said reformed gas to a shift reactor for a CO shift reaction therein to decrease the concentration of carbon monoxide in said reformed gas to a second concentration lower than said first concentration; feeding said reformed gas to a CO reactor, having a plurality of sections, for an oxidation reaction therein to decrease the concentration of carbon monoxide in said reformed gas to a third concentration lower than said second concentration; feeding said reformed gas, containing carbon monoxide at said third concentration, and a gaseous oxidizing agent to a fuel cell for reaction to generate electric power; determining an output value for power required from said fuel cell as a function of a load demand; determining a space velocity value for said reformed gas entering said CO reactor based on input values for the feed rate of said reformed gas to said CO reactor and said determined output value; and controlling the number of said plurality of sections of said CO reactor receiving said reformed gas in accordance with the determined space velocity value.

Claim 9

A fuel cell power generating process comprising: reacting a fuel with water in gas phase in a reforming reaction to produce a reformed gas including carbon monoxide at a first concentration and hydrogen; feeding said reformed gas to a shift reactor for a CO shift reaction therein to decrease the concentration of carbon monoxide in said reformed gas to a second concentration lower than said first concentration; feeding said reformed gas to a CO reactor, having a plurality of sections, for an oxidation reaction therein to decrease the concentration of carbon monoxide in said reformed gas to a third concentration lower than said second concentration; feeding said reformed gas, containing carbon monoxide at said third concentration, and a gaseous oxidizing agent to a fuel cell for reaction to generate electric power; determining an output value for power required from said fuel cell as a function of a load demand; determining a space velocity value for said reformed gas entering said CO reactor based on input values for the feed rate of said reformed gas to said CO reactor and said determined output value; and controlling the number of said plurality of sections of said CO reactor receiving said reformed gas in accordance with the determined space velocity value.

Claim 10

The fuel cell power generating process according to claim 7, wherein said fuel is methanol.

Claim 11

The fuel cell power generating process according to claim 7, wherein said reforming reaction is promoted by a reforming catalyst and is conducted at a catalytic active temperature of 250° C. to 300° C.

Claim 12

The fuel cell power generation process according to claim 7, wherein said shift reactor contains a bed of a shift catalyst and wherein said shift reaction reduces the carbon monoxide first concentration in said reformed gas to a second concentration of 1,000 ppm or less at a temperature of 150° C. to 200° C.

Claim 13

The fuel cell power generating process according to claim 7, wherein each section of said CO reactor includes at least one reaction subsection containing a bed of selective-oxidizing catalyst and at least one cooling subsection and further comprising circulating water through said cooling subsection to maintain the temperature of said selective-oxidizing catalyst in a predetermined temperature range.

Claim 14

The fuel cell power generating process according to claim 11, wherein said predetermined temperature range is 90° C. to 140° C.

Claim 15

The fuel cell power generating process according to claim 11, wherein said selective-oxidizing catalyst is supported on a particulate carrier in a first density at the upstream side of said bed and a second density at the downstream side of said bed, relative to the flow of the reformed gas through said CO reactor, said second density being higher than said first density.

Claim 16

The fuel cell power generating process according to claim 7, wherein said space velocity is controlled at 1,000 hr -1 to 2,000 hr -1 .

Claim 17

The fuel cell power generating process according to claim 7, wherein said third carbon monoxide concentration in said reformed gas is 10 ppm or less.