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Béatrice Fischer, Lyon FR

Béatrice Fischer, Lyon FR

Patent application numberDescriptionPublished
20090274593INTERNAL COMBUSTION EXCHANGER-REACTOR FOR FIXED BED ENDOTHERMIC REACTION - The invention concerns an exchanger-reactor (11-05-2009
20100080754PROCESS FOR PRODUCING HYDROGEN WITH COMPLETE CAPTURE OF CO2 AND RECYCLING UNCONVERTED METHANE - The present invention concerns a process for producing hydrogen from a hydrocarbon feed and steam, comprising: 04-01-2010
20100126908NOVEL STEAM REFORMING FURNACE USING POROUS BURNERS - The present invention describes a steam reforming furnace for the production of hydrogen, which employs a set of porous burners interposed between the tubes to be heated, improving compactness of the furnace.05-27-2010
20100189638COMPACT EXCHANGER-REACTOR USING A PLURALITY OF POROUS BURNERS - The present invention describes a novel exchanger-reactor intended to implement highly endothermic reactions such as natural gas or naphtha steam reforming, using in situ porous burners.07-29-2010
20100199682PROCESS FOR THE PRODUCTION OF HYDROGEN WITH TOTAL RECOVERY OF CO2 AND REDUCTION OF UNCONVERTED METHANE - This invention relates to a process for the production of hydrogen from a hydrocarbon feedstock and water vapor comprising: 08-12-2010
20100252482REACTOR AND PROCESS FOR ENDOTHERMIC GAS PHASE REACTIONS ON A SOLID CATALYST - The invention concerns a reactor for catalytic reforming or for hydrocarbon dehydrogenation, having a cylindrical shape along a vertical axis, an upper head and a lower bottom comprising at least two annular zones centred on the vertical axis, said two annular zones being a zone termed a catalytic zone and a zone termed the exchange zone. Vertical hermetic panels divide the reactor into sectors, said sectors each comprising at least one exchange section and at least one catalytic section, the ensemble of said exchange sections forming the exchange zone and the ensemble of said catalytic sections forming the catalytic zone.10-07-2010
20100263532DRY NATURAL GAS LIQUEFACTION METHOD - The method allows liquefaction of a dry natural gas comprising water and heavy hydrocarbons containing more than five carbon atoms. The following stages are carried out: 10-21-2010
20100276336REACTOR AND PROCESS FOR ENDOTHERMIC GAS PHASE REACTIONS - The invention concerns a reactor for carrying out an endothermic gas phase reaction having a cylindrical shape along a vertical axis and comprising at least four annular zones, centred on the vertical axis and in succession from the edge towards the centre of the reactor, namely a first zone 11-04-2010
20110048067NATURAL GAS LIQUEFACTION METHOD WITH HIGH-PRESSURE FRACTIONATION - The method provides liquefaction of a natural gas by carrying out the following stages: 03-03-2011

Patent applications by Béatrice Fischer, Lyon FR