REGISTER now for FREE 
|
FREE patent keyword monitoring and additional FREE benefits. REGISTER now for FREE
|
|
|
Chemistry Of Inorganic Compounds > Hydrogen Or Compound Thereof > Elemental Hydrogen > By Decomposing Hydrocarbon By Decomposing HydrocarbonBy Decomposing Hydrocarbon patent applications listed are from June 2005 to current and include Date, Patent Application Number, Patent Title, Patent Abstract summary and are linked to the corresponding patent application page.06/21/07 - 20070140954 - Process for the preparation hydrogen and a mixture of hydrogen and carbon monoxide Process for the preparation hydrogen and a mixture of hydrogen and carbon monoxide containing gas from a carbonaceous feedstock by performing the following steps: (a) preparing a mixture of hydrogen and carbon monoxide having a temperature of above 700° C. (51); (b) catalytic steam reforming a carbonaceous feedstock in a ... 05/03/07 - 20070098627 - Steam generation apparatus and method Provided herein is a process for generating steam comprising supplying a first stream to a steam reformer to produce a second stream comprising essentially 100% steam such that the molecular composition of the first stream is identical to the molecular composition of second stream, wherein the steam reformer comprises a ... 03/15/07 - 20070059235 - Rapid activation catalyst systemin a non-thermal plasma catalytic reactor A rapid start reactor is provided that can be used, for example, in a water gas shift reactor of a fuel processor. A reactor has a catalyst support structure with one or more surfaces overlaid with an active coating that includes a catalyst. The active coating heats upon exposure to ... 02/22/07 - 20070041894 - Synthesis gas and carbon dioxide generation method A method of generating a synthesis gas product stream and carbon dioxide in which a fuel is combusted in an oxygen transport membrane combustor to produce a flue gas stream containing the carbon dioxide and water. Reforming duty is divided between a combined reforming process and a gas heated reformer ... 01/25/07 - 20070020173 - Hydrogen distribution networks and related methods A hydrogen distribution network comprising a hydrocarbon feedstock distribution system; a hydrogen distribution system; and (c) two or more hydrogen production facilities wherein (1) the hydrogen production facilities produce minimal or no net excess steam for export and comprise at least one hydrogen production module interconnected to a purification system, ... 01/04/07 - 20070003477 - Purification of a mixture of h<sb>2</sb>/co by catalysis of the impurities The invention relates to a method for purifying a gaseous flow containing at least hydrogen (H2), carbon monoxide (CO), a metal carbonyl, and at least one impurity selected from oxygen (O2) and unsaturated hydrocarbons. According to said method, the gaseous flow is brought into contact with a first catalytic bed ... 07/06/06 - 20060147370 - Multi-stream microchannel device The invention is a process and device for exchanging heat energy between three or more streams in a microchannel heat exchanger which can be integrated with a microchannel reactor to form an integrated microchannel processing unit. The invention enables the combining of a plurality of integrated microchannel devices to provide ... 06/15/06 - 20060127305 - Series of hydroconversion and steam reforming processes to optimize hydrogen production on production fields The invention concerns a process for treating a hydrocarbon feed comprising a series of a first upstream process for hydrocarbon hydroconversion comprising at least one reaction chamber, the reaction or reactions occurring inside said chambers and employing at least one solid phase, at least one liquid phase and at least ... 06/01/06 - 20060115413 - Microsystem process networks Various aspects and applications of microsystem process networks are described. The design of many types of microsystems can be improved by ortho-cascading mass, heat, or other unit process operations. Microsystems having exergetically efficient microchannel heat exchangers are also described. Detailed descriptions of numerous design features in microcomponent systems are also ... 02/16/06 - 20060034755 - Microsystem process networks Various aspects and applications or microsystem process networks are described. The design of many types of microsystems can be improved by ortho-cascading mass, heat, or other unit process operations. Microsystems having energetically efficient microchannel heat exchangers are also described. Detailed descriptions of numerous design features in microcomponent systems are also ... 02/16/06 - 20060034754 - Microsystem process networks Various aspects and applications of microsystem process networks are described. The design of many types of Microsystems can be improved by ortho-cascading mass, heat, or other unit process operations. Microsystems having energetically efficient microchannel heat exchangers are also described. Detailed descriptions of numerous design features in microcomponent systems are also ... 02/09/06 - 20060029538 - Method for removal of contaminants from a hydrogen processor feed stream, as in a fuel cell power plant Method and apparatus are provided for removing contaminants from a hydrogen processor feed stream, as in a fuel cell power plant (110). Inlet oxidant (38), typically air, required by a catalytic hydrogen processor (34) in a fuel processor (14) for a fuel cell stack assembly (12) in the power plant ... 10/20/05 - 20050232855 - Reactor with carbon dioxide fixing material Apparatus and methods for converting hydrocarbon fuels to hydrogen-rich reformate that incorporate a carbon dioxide fixing mechanism into the initial hydrocarbon conversion process. The mechanism utilizes a carbon dioxide fixing material within the reforming catalyst bed to remove carbon dioxide from the reformate product. The removal of carbon dioxide from ... 10/20/05 - 20050232854 - Method and installation for separating a mixture of hydrogen and carbon monoxide The invention relates to a method for simultaneously producing hydrogen and carbon monoxide, whereby the synthesis gas is subjected to decarbonatation in a decarbonatation unit (2), and to desiccation in a desiccation unit (5). The remaining constituents are cryogenically separated and a hydrogen-enriched gas (7, 19, 21) is recycled upstream ... ### FreshPatents.com Support |