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Disclosed is a hydrogen generation process for use with fuel cells which includes a preferential oxidation step to reduce the concentration of carbon monoxide. The preferential oxidation step includes contacting a fuel stream comprising hydrogen and carbon monoxide in the presence of an oxygen at a

Disclosed is a hydrogen generation process for use with fuel cells which includes a preferential oxidation step to reduce the concentration of carbon monoxide. The preferential oxidation step includes contacting a fuel stream comprising hydrogen and carbon monoxide in the presence of an oxygen at a preferential oxidation temperature of between about 70° and about 160° C. with preferential oxidation catalyst for reducing the concentration of carbon monoxide to produce a treated fuel gas stream comprising less than about 50 ppm-vol carbon monoxide. The preferential oxidation catalyst comprises ruthenium metal disposed on an alumina carrier having a low density and a high porosity. Superior performance at low preferential oxidation temperatures below 130° C. was observed when the alumina carrier contained a bimodal pore distribution with an average pore distribution of from about 20 to about 3000 angstroms. The preferential oxidation catalyst may be employed to reduce carbon monoxide in fuel gas streams supplied to fuel cells wherein carbon monoxide will poison the active noble metal membrane and higher preferential oxidation temperatures may reduce the hydrogen content of the gas stream.

대표청구항 ▼

1. A method for preparing a preferential oxidation catalyst comprising: a) impregnating an alumina carrier having an apparent bulk density of about 0.3 to about 0.7 gm/cc, a surface area of about 25 to about 500 m2/g, and an average pore diameter of from about 20 to about 3000 angstroms with a so

1. A method for preparing a preferential oxidation catalyst comprising: a) impregnating an alumina carrier having an apparent bulk density of about 0.3 to about 0.7 gm/cc, a surface area of about 25 to about 500 m2/g, and an average pore diameter of from about 20 to about 3000 angstroms with a source of ruthenium metal to provide a ruthenium-containing composition having a ruthenium content of between about 0.5 and about 5 wt-%; and b) reducing the ruthenium containing composition. 2. The method of claim 1 wherein the reducing of the ruthenium composition comprises contacting the ruthenium composition with a reducing gas at a reducing temperature of between about 300° and about 500° C. 3. The method of claim 1 wherein the alumina carrier comprises a bimodal pore size distribution. 4. The method of claim 1 further comprising an oxidation step at an oxidizing temperature less than about 500° C. after the impregnating of step (a) and prior to the reducing of step (b). 5. The method of claim 1 further comprising an oxidation step at an oxidizing temperature less than about 300° C. after the impregnating of step (a) and prior to the reducing of step (b). 6. The method of claim 1 wherein the alumina carrier comprises a pore distribution comprising at least one peak having an average pore diameter between about 800 and 1500 angstroms. 7. A preferential oxidation catalyst comprising an alumina carrier having an apparent bulk density of about 0.3 to about 0.7 gm/cc, an average pore diameter of from about 20 to 3000 angstroms wherein the alumina has a pore distribution with at least one peak having an average pore diameter between 70 and 100 angstroms and a second peak distribution having an average pore diameter of between 800 and 1500 angstroms, a pore volume of about 0.1 to about 2.5 milliliters per gram and a surface area of about 100 to about 500 square meters per gram, having between about 0.5 and about 5 weight percent ruthenium dispersed thereon. 8. The catalyst of claim 7 wherein essentially no crystallites of ruthenium are detectable by X-ray diffraction having a resolution minimum of 40 angstroms. 9. A preferential oxidation catalyst comprising an alumina carrier having an apparent bulk density of about 0.3 to about 0.7 gm/cc, an average pore diameter of from about 20 to 3000 angstroms wherein the alumina has a bimodal pore distribution with one peak distribution having an average pore diameter of between 1000 and 1500 angstroms, a pore volume of about 0.1 to about 2.5 milliliters per gram and a surface area of about 100 to about 500 square meters per gram, having between about 0.5 and about 5 weight percent ruthenium dispersed thereon wherein essentially no crystallites of ruthenium are detectable by X-ray diffraction having a resolution minimum of 40 angstroms. 10. The catalyst of claim 9 wherein the alumina comprises at least one member selected from the group consisting of gamma and eta alumina.