Honda Giken Kogyo Kabushiki Kaisha

Symyx Technologies, Inc.

Honda Giken Koygo Kabushiki Kaisha

Freeslate, Inc.

University of Michigan

Cory Bernard Phillips

Alfred Gerhard Hagemeyer

Karin Yaccato

Christopher James Brooks

Raymond E Carhart

Robert K Grasselli

Peter Strasser

Michael Herrmann

Andreas Lesik

Jeremy J Patt

Levi T Thompson

Dong Ju Moon

A method and catalysts for producing a hydrogen-rich syngas are disclosed. According to the method a CO-containing gas contacts a water gas shift (WGS) catalyst, optionally in the presence of water, preferably at a temperature of less than about 450&#xb0; C. to produce a hydrogen-rich gas, such as a hydrogen-rich syngas. Also disclosed is a water gas shift catalyst formulated from:

Platinum-ruthenium containing catalyst formulations for hydrogen generation

A method and catalysts and fuel processing apparatus for producing a hydrogen-rich gas, such as a hydrogen-rich syngas are disclosed. According to the method a CO-containing gas, such as a syngas, contacts a water gas shift catalyst in the presence of water, preferably at a temperature of less than about 450&#xb0; C. to produce a hydrogen-rich gas, such as a hydrogen-rich syngas. Also disclosed is a water gas shift catalyst comprising: The WGS catalyst may be supported on a carrier, such as any one member or a combination of alumina, zirconia, titania, ceria, magnesia, lanthania, niobia, yttria and iron oxide. Fuel processors containing such water gas shift catalysts are also disclosed.

Platinum-alkali/alkaline-earth catalyst formulations for hydrogen generation

A method and catalysts for producing a hydrogen-rich syngas are disclosed. According to the method a CO-containing gas contacts a water gas shift (WGS) catalyst, in the presence of water, preferably at a temperature of less than about 450&#xb0; C. to produce a hydrogen-rich syngas. Also disclosed is a water gas shift catalyst formulated from:

Platinum and rhodium and/or iron containing catalyst formulations for hydrogen generation

A method and catalysts and fuel processing apparatus for producing a hydrogen-rich gas, such as a hydrogen-rich syngas are disclosed. According to the method, a CO-containing gas, such as a syngas, contacts a platinum-free ruthenium-cobalt water gas shift ('WGS') catalyst, in the presence of water and preferably at a temperature of less than about 450&#xb0; C., to produce a hydrogen-rich gas, such as a hydrogen-rich syngas. Also disclosed is a platinum-free ruthenium-cobalt water gas shift catalyst formulated from:

Platinum-free ruthenium-cobalt catalyst formulations for hydrogen generation

A method and catalysts and fuel processing apparatus for producing a hydrogen-rich gas, such as a hydrogen-rich syngas are disclosed. According to the method a CO-containing gas, such as a syngas, contacts a water gas shift ('WGS') catalyst, in the presence of water, preferably at a temperature of less than about 450&#xb0; C. to produce a hydrogen-rich gas, such as a hydrogen-rich syngas. Also disclosed is a water gas shift catalyst formulated from:

Catalyst formulations containing Group 11 metals for hydrogen generation

A reactor module having one or more than one heat exchanger, a chamber block capable of being charged with a catalyst, and a platform are assembled in a unit in which separate fluid flows of reactants and heat media are directed by manifolds and ducts intrinsically formed in the module. Multiple reactor modules may be interconnected to form a further reactor module unit and the interconnected reactor units may in turn be configured for a large system with a high power rating.

Compact reactor capable of being charged with catalytic material for use in a hydrogen generation/fuel cell system

Mono- and bimetallic transition metal carbides, nitrides and borides, and their oxygen containing analogs (e.g. oxycarbides) for use as water gas shift catalysts are described. In a preferred embodiment, the catalysts have the general formula of M1 M2 Z O , wherein M1 is selected from the group consisting of Mo, W, and combinations thereof; M2 is selected from the group consisting of Fe, Ni, Cu, Co, and combinations thereof; Z is selected from the group consisting of carbon, nitrogen, boron, and combinations thereof; A is an integer; B is 0 or an integer greater than 0; C is an integer; O is oxygen; and D is 0 or an integer greater than 0. The catalysts exhibit good reactivity, stability, and sulfur tolerance, as compared to conventional water shift gas catalysts. These catalysts hold promise for use in conjunction with proton exchange membrane fuel cell powered systems.

Growing community of inventors

Detroit, MI, United States of America

Cory Bernard Phillips