Method and apparatus for converting hydrocarbon fuel into...

C - Chemistry – Metallurgy – 01 – B

Patent

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Details

C01B 3/36 (2006.01) B01J 8/02 (2006.01) B01J 8/04 (2006.01) C01B 3/38 (2006.01) C01B 3/48 (2006.01) H01M 8/06 (2006.01)

Patent

CA 2265468

An apparatus and a method are disclosed for converting hydrocarbon fuel or an alcohol into hydrogen gas and carbon dioxide. The apparatus includes a first vessel (18) having a partial oxidation reaction zone (24) and a separate steam reforming reaction zone (26) that is distinct from the partial oxidation reaction zone. The first vessel has a first vessel inlet (20) at the partial oxidation reaction zone and a first vessel outlet (22) at the steam reforming zone. The reformer also includes a helical tube (32) extending about the first vessel. The helical tube has a first end connected to an oxygen-containing source (42) and a second end connected to the first vessel at the partial oxidation reaction zone. Oxygen gas from an oxygen-containing source can be directed through the helical tube to the first vessel. A second vessel (58) having a second vessel inlet (60) and second vessel outlet (22) is annularly disposed about the first vessel. The helical tube is disposed between the first vessel and the second vessel and gases from the first vessel can be directed through second vessel.

L'invention concerne un appareil et un procédé pour convertir u n carburant ou un alcool hydrocarbure en gaz hydrogène et en dioxyde de carbone. L'appareil comprend un premier récipient ayant une zone de réaction d'oxydation partielle et une zone de réaction de reformation de vapeur, qui est distincte de la zone de réaction d'oxydation partielle. Le premier récipient a un premier orifice d'entrée situé dans la zone de réaction d'oxydation partielle et un premier orifice de sortie situé dans la zone de reformation de vapeur. Le reformeur comprend également un tube hélicoïdal enroulé autour du premier récipient. Ledit tube a une première extrémité reliée à une source d'oxygène et une seconde extrémité reliée au premier récipient dans la zone de réaction d'oxydation partielle. Le gaz oxygène provenant de la source d'oxygène est dirigé au travers du tube hélicoïdal jusque dans le premier récipient. Un second récipient ayant un second orifice d'entrée et un second orifice de sortie est disposé en anneau autour du premier récipient. Le tube hélicoïdal est disposé entre le premier récipient et le second récipient et les gaz provenant du premier récipient peuvent être envoyés dans le second récipient.

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