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公开(公告)号:US06641625B1
公开(公告)日:2003-11-04
申请号:US09563677
申请日:2000-05-02
申请人: Lawrence G. Clawson , Matthew H. Dorson , William L. Mitchell , Brian J. Nowicki , Johannes Thijssen , Robert Davis , Christopher Papile , Jennifer W. Rumsey , Nathan Longo , James C. Cross, III , Vincent Rizzo , Gunther Kleeburg , Michael Rindone , Stephen G. Block , Maria Sun , Brian D. Morriseau , Mark R. Hagan , Brian Bowers
发明人: Lawrence G. Clawson , Matthew H. Dorson , William L. Mitchell , Brian J. Nowicki , Johannes Thijssen , Robert Davis , Christopher Papile , Jennifer W. Rumsey , Nathan Longo , James C. Cross, III , Vincent Rizzo , Gunther Kleeburg , Michael Rindone , Stephen G. Block , Maria Sun , Brian D. Morriseau , Mark R. Hagan , Brian Bowers
IPC分类号: B01J804
CPC分类号: H01M8/0631 , B01J8/0419 , B01J8/0496 , B01J2208/00044 , B01J2208/0007 , B01J2208/00203 , B01J2208/00495 , B01J2208/0061 , B01J2219/00006 , C01B3/36 , C01B3/38 , C01B3/382 , C01B3/386 , C01B3/48 , C01B3/583 , C01B2203/0233 , C01B2203/0244 , C01B2203/0255 , C01B2203/0261 , C01B2203/0288 , C01B2203/04 , C01B2203/044 , C01B2203/045 , C01B2203/0465 , C01B2203/047 , C01B2203/0485 , C01B2203/0495 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/0833 , C01B2203/0844 , C01B2203/0866 , C01B2203/0872 , C01B2203/0883 , C01B2203/0894 , C01B2203/1011 , C01B2203/1023 , C01B2203/1041 , C01B2203/1047 , C01B2203/1052 , C01B2203/1058 , C01B2203/1064 , C01B2203/1076 , C01B2203/1082 , C01B2203/1229 , C01B2203/1241 , C01B2203/1247 , C01B2203/127 , C01B2203/1276 , C01B2203/1282 , C01B2203/1288 , C01B2203/1294 , C01B2203/141 , C01B2203/142 , C01B2203/143 , C01B2203/146 , C01B2203/147 , C01B2203/148 , C01B2203/1604 , C01B2203/1609 , C01B2203/1614 , C01B2203/1619 , C01B2203/1623 , C01B2203/1628 , C01B2203/1633 , C01B2203/1638 , C01B2203/1652 , C01B2203/1661 , C01B2203/1676 , C01B2203/1685 , C01B2203/169 , C01B2203/1695 , C01B2203/80 , C01B2203/82 , H01M8/0612 , Y02P20/128
摘要: A hydrocarbon reformer system including a first reactor configured to generate hydrogen-rich reformate by carrying out at least one of a non-catalytic thermal partial oxidation, a catalytic partial oxidation, a steam reforming, and any combinations thereof, a second reactor in fluid communication with the first reactor to receive the hydrogen-rich reformate, and having a catalyst for promoting a water gas shift reaction in the hydrogen-rich reformate, and a heat exchanger having a first mass of two-phase water therein and configured to exchange heat between the two-phase water and the hydrogen-rich reformate in the second reactor, the heat exchanger being in fluid communication with the first reactor so as to supply steam to the first reactor as a reactant is disclosed. The disclosed reformer includes an auxiliary reactor configured to generate heated water/steam and being in fluid communication with the heat exchanger of the second reactor to supply the heated water/steam to the heat exchanger.
摘要翻译: 一种烃重整器系统,包括通过进行非催化热部分氧化,催化部分氧化,蒸汽重整及其任何组合中的至少一种而产生富氢重整产物的第一反应器,流体连通的第二反应器 其中第一反应器接收富氢重整产物,并且具有用于促进富氢重整产物中的水煤气变换反应的催化剂,以及具有第一质量二相水的热交换器,其被配置为在 所述第二反应器中的所述两相水和富氢重整产物,所述热交换器与所述第一反应器流体连通,以便将作为反应物的蒸汽供应到所述第一反应器。 所公开的重整器包括配置成产生加热的水/蒸汽并与第二反应器的热交换器流体连通的辅助反应器,以将加热的水/蒸汽供应到热交换器。