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公开(公告)号：EP1381453A4
公开(公告)日：2008-02-13
申请号：EP02734044
申请日：2002-04-26
IPC分类号： B01J8/04 , C01B3/36 , B01D53/86 , B01D53/88 , B01J8/00 , B01J8/06 , B01J19/24 , C01B3/38 , C01B3/48 , F28D7/00 , H01M8/06
CPC分类号： B01J8/009 , B01D53/864 , B01D53/885 , B01J8/0453 , B01J8/0492 , B01J8/0496 , B01J8/067 , B01J19/243 , B01J2208/00132 , B01J2208/00141 , B01J2208/00203 , B01J2208/0053 , B01J2208/025 , B01J2219/00006 , B01J2219/0002 , C01B3/382 , C01B3/48 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/044 , C01B2203/045 , C01B2203/0455 , C01B2203/047 , C01B2203/0485 , C01B2203/066 , C01B2203/0811 , C01B2203/0833 , C01B2203/0838 , C01B2203/0844 , C01B2203/0883 , C01B2203/142 , C01B2203/143 , C01B2203/82 , F28D7/0066 , F28D7/0091 , H01M8/0618 , H01M8/0668 , H01M8/0675
摘要： An apparatus (20) for carrying out a multi-step process of converting hydrocarbon fuel (F) to a substantially pure hydrogen gas feed (H) includes a plurality of reaction zones (202, 204, 206, 208, 210) arranged in a common reaction chamber (212). The multi-step process includes providing a fuel (F) to the fuel processor (226) so that as the fuel (F) reacts and forms the hydrogen rich gas (H), the intermediate gas products pass through each reaction zone as arranged in the reactor to produce the hydrogen rich gas (H).
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公开(公告)号：EP1611399A4
公开(公告)日：2015-05-20
申请号：EP04758616
申请日：2004-03-30
发明人： DESHPANDE VIJAY A , KRAUSE CURTIS L , MARTIN PAUL F , NGUYEN KEVIN H , STEVENS JAMES F , WHEAT WILLIAMS S
CPC分类号： F23C13/02 , C01B3/34 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/1258 , F23C13/00 , F23C2900/03002 , F23D14/66 , F23L2900/07009 , H01M8/0631 , Y02E20/348 , Y02P20/128 , Y02P70/56 , Y10T29/49348
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公开(公告)号：EP1620636A4
公开(公告)日：2007-06-13
申请号：EP04758610
申请日：2004-03-30
IPC分类号： B01J8/04 , B01J20060101 , B01J8/02 , B01J10/00 , C01B3/38 , C01B3/48 , C01B3/56 , F01P20060101 , F16F1/34 , F28F19/00 , H01M8/00 , H01M8/04 , H01M8/06 , H01M8/10 , H01M8/12 , H01M8/18
CPC分类号： B01J8/0285 , B01J8/0496 , B01J2208/00141 , B01J2208/00168 , B01J2208/0053 , B01J2219/00083 , B01J2219/00087 , C01B3/382 , C01B3/48 , C01B3/56 , C01B2203/0244 , C01B2203/0283 , C01B2203/042 , C01B2203/044 , C01B2203/047 , C01B2203/0485 , C01B2203/066 , C01B2203/0844 , C01B2203/0883 , C01B2203/146 , H01M8/0612 , H01M8/0668 , H01M2008/1095 , Y02P20/129
摘要： A coolant subsystem for use in a fuel processor and a method for its operation are disclosed. In accordance with a first aspect, the coolant subsystem is separate from the feed to the processor reactor and is capable of circulating a coolant through the processor reactor. In accordance with a second aspect, the constituent elements of the fuel processor are housed in a cabinet, and the coolant subsystem is capable of cooling both the processor reactor and the interior of the cabinet. In various alternatives, the fuel processor can be employed to reform a fuel for a fuel cell power plant and/or may be used to provide thermal control for unrelated mechanical systems.
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4.发明公开
公开(公告)号：EP1349647A4
公开(公告)日：2006-11-08
申请号：EP01991282
申请日：2001-12-12
发明人： DESHPANDE VIJAY A
IPC分类号： B01J7/00 , B01J8/00 , B01J8/04 , C01B3/16 , C01B3/32 , C01B3/38 , C01B3/48 , C01B3/58 , H01M8/06
CPC分类号： C01B3/16 , B01J8/0465 , B01J8/0496 , B01J2208/00203 , B01J2208/00309 , B01J2208/0053 , B01J2219/0002 , C01B3/323 , C01B3/382 , C01B3/48 , C01B3/583 , C01B2203/0244 , C01B2203/0283 , C01B2203/044 , C01B2203/0455 , C01B2203/047 , C01B2203/0485 , C01B2203/066 , C01B2203/0811 , C01B2203/0844 , C01B2203/085 , C01B2203/0866 , C01B2203/0877 , C01B2203/0883 , C01B2203/0888 , C01B2203/0894 , C01B2203/1011 , C01B2203/1017 , C01B2203/1023 , C01B2203/1035 , C01B2203/1041 , C01B2203/1082 , C01B2203/1205 , C01B2203/1235 , C01B2203/127 , C01B2203/1276 , C01B2203/142 , C01B2203/146 , C01B2203/1604 , C01B2203/82 , H01M8/0612 , H01M8/0668 , H01M8/0675
摘要： An apparatus (10) for carrying out a multi-step process of converting hydrocarbon fuel (100) to a substantially pure hydrogen gas feed (150) includes a plurality of modules (128, 132, 136, 144) each module being in fluid communication with adjacent modules. The modules may be arranged axially along a common axis of flow or alternatively the modules are arranged along a common axis so that they are nested one within the other. The multi-step process includes: providing a fuel processor having a plurality of modules; and feeding the hydrocarbon fuel (100) successively through each of the modules (128, 132, 136, 144) in the reactor to produce the hydrogen rich gas (150).
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公开(公告)号：EP1345679A4
公开(公告)日：2006-05-03
申请号：EP01986119
申请日：2001-12-05
发明人： DESHPANDE VIJAY A
IPC分类号： B01J8/00 , B01J8/02 , B01J8/04 , B01J8/06 , B01J19/00 , B01J19/24 , C01B3/16 , C01B3/38 , C01B3/48 , C01B3/58 , C10J1/207 , H01M8/04 , H01M8/06 , C10J3/68
CPC分类号： B01J8/0488 , B01J8/009 , B01J8/0278 , B01J8/0285 , B01J8/0423 , B01J8/0453 , B01J8/048 , B01J8/0492 , B01J8/0496 , B01J8/067 , B01J19/0013 , B01J19/2475 , B01J19/2485 , B01J2208/00141 , B01J2208/00176 , B01J2208/00194 , B01J2208/00203 , B01J2208/00407 , B01J2208/00415 , B01J2208/00716 , B01J2208/00814 , B01J2208/025 , B01J2219/0002 , B01J2219/00083 , B01J2219/00135 , B01J2219/182 , B01J2219/185 , B01J2219/1944 , C01B3/16 , C01B3/38 , C01B3/382 , C01B3/384 , C01B3/386 , C01B3/48 , C01B3/583 , C01B2203/0244 , C01B2203/0283 , C01B2203/0288 , C01B2203/044 , C01B2203/0455 , C01B2203/0465 , C01B2203/047 , C01B2203/0485 , C01B2203/0495 , C01B2203/066 , C01B2203/0805 , C01B2203/0844 , C01B2203/085 , C01B2203/0866 , C01B2203/0877 , C01B2203/0883 , C01B2203/0894 , C01B2203/1011 , C01B2203/1017 , C01B2203/1023 , C01B2203/1035 , C01B2203/1041 , C01B2203/1082 , C01B2203/1205 , C01B2203/1235 , C01B2203/1276 , C01B2203/142 , C01B2203/146 , C01B2203/147 , C01B2203/1604 , C01B2203/80 , C01B2203/82 , H01M8/04022 , H01M8/04037 , H01M8/04059 , H01M8/0612 , H01M8/0631 , H01M8/0668 , Y02P20/52
摘要： A reactor module (300) for use in a compact fuel processor having a module inlet (320) for receiving a feed stream, a module outlet (390) for producing an effluent stream, a reactor having a reactor inlet, a reactor outlet, and catalyst, an inlet spiral passage (330) in fluid communication with the module inlet to the reactor inlet, and an outlet spiral passage (340) in fluid communication with the reactor outlet to the module outlet. Such a design provides for the feed stream to be introduced to the module inlet, where it then passes through the inlet spiral passage, and is heated by hot reactor product passing through the outlet spiral passage. The reactor may be any type of fixed bed exothermic containing supported catalyst particles or the reactor bed may be a monolith with catalytic material coated on to the surface of the structural members.
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