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1. 发明授权

US07371361B2 Maximum reaction rate converter system for exothermic reactions 有权
标题翻译：用于放热反应的最大反应速率转换器系统
公开(公告)号：US07371361B2
公开(公告)日：2008-05-13
申请号：US10904315
申请日：2004-11-03
申请人： Shashi P. Singh , David P. Mann , Anant Pisut
发明人： Shashi P. Singh , David P. Mann , Anant Pisut
IPC分类号： C01C1/04 , C01B3/16
CPC分类号： C01C1/0423 , B01J8/008 , B01J8/067 , B01J23/462 , B01J2208/00212 , B01J2208/00221 , B01J2208/00513 , B01J2208/00548 , B01J2219/00238 , C01C1/0441 , C01C1/0482 , Y02E60/364 , Y02P20/52
摘要： An ammonia converter system and method are disclosed. The reactor can alter the conversion of ammonia by controlling the reaction temperature of the exothermic reaction along the length of the reactor to parallel the equilibrium curve for the desired product. The reactor 100 can comprise a shell 101 and internal catalyst tubes 109. The feed gas stream enters the reactor, flows through the shell 101, and is heated by indirect heat exchange with the catalyst tubes 109. The catalyst tubes 109 comprise reactive zones 122 having catalyst and reaction limited zones 124 that can comprise inert devices that function to both separate the reactive zones, increase heat transfer area, and reduce the temperature of the reaction mixture as the effluent passes through the catalyst tube 109.
摘要翻译：公开了一种氨转化器系统和方法。反应器可以通过控制沿着反应器长度的放热反应的反应温度平行所需产物的平衡曲线来改变氨的转化率。反应器100可以包括壳体101和内部催化剂管109。进料气流进入反应器，流过壳体101，并通过与催化剂管109的间接热交换加热。催化剂管109包括具有催化剂和反应限制区124的反应区122，其可以包含用于分离反应区的惰性装置，增加传热面积，并且当流出物通过催化剂管时降低反应混合物的温度 109。

2. 发明授权

US07846417B2 Maximum reaction rate converter process for exothermic reactions 有权
标题翻译：最大反应速率转换器放热反应过程
公开(公告)号：US07846417B2
公开(公告)日：2010-12-07
申请号：US11932019
申请日：2007-10-31
申请人： Shashi P. Singh , David P. Mann , Anant Pisut
发明人： Shashi P. Singh , David P. Mann , Anant Pisut
IPC分类号： C01C1/04 , C07C27/06 , C07C53/08 , C07C45/00 , C07C1/20 , C07D307/89
CPC分类号： C01C1/0423 , B01J8/008 , B01J8/067 , B01J23/462 , B01J2208/00212 , B01J2208/00221 , B01J2208/00513 , B01J2208/00548 , B01J2219/00238 , C01C1/0441 , C01C1/0482 , Y02E60/364 , Y02P20/52
摘要： An ammonia converter and method are disclosed. The reactor can alter the conversion of ammonia by controlling the reaction temperature of the exothermic reaction along the length of the reactor to parallel the equilibrium curve for the desired product. The reactor 100 can comprise a shell 101 and internal catalyst tubes 109. The feed gas stream enters the reactor, flows through the shell 101, and is heated by indirect heat exchange with the catalyst tubes 109. The catalyst tubes 109 comprise reactive zones 122 having catalyst and reaction limited zones 124 that can comprise inert devices that function to both separate the reactive zones, increase heat transfer area, and reduce the temperature of the reaction mixture as the effluent passes through the catalyst tube 109.
摘要翻译：公开了氨转化器和方法。反应器可以通过控制沿着反应器长度的放热反应的反应温度来平行所需产物的平衡曲线来改变氨的转化率。反应器100可以包括壳体101和内部催化剂管109.进料气体流进入反应器，流过壳体101，并通过与催化剂管109的间接热交换而被加热。催化剂管109包括反应区域122，反应区域122具有催化剂和反应限制区124，其可以包括用于分离反应区的惰性装置，增加传热面积，并且当流出物通过催化剂管109时降低反应混合物的温度。

3. 发明授权

US07842254B2 Maximum reaction rate converter for exothermic reactions 有权
标题翻译：用于放热反应的最大反应速率转化器
公开(公告)号：US07842254B2
公开(公告)日：2010-11-30
申请号：US11932140
申请日：2007-10-31
申请人： Shashi P. Singh , David P. Mann , Anant Pisut
发明人： Shashi P. Singh , David P. Mann , Anant Pisut
IPC分类号： B01J8/04
CPC分类号： C01C1/0423 , B01J8/008 , B01J8/067 , B01J23/462 , B01J2208/00212 , B01J2208/00221 , B01J2208/00513 , B01J2208/00548 , B01J2219/00238 , C01C1/0441 , C01C1/0482 , Y02E60/364 , Y02P20/52
摘要： An ammonia converter is disclosed. The converter can alter the conversion of ammonia by controlling the reaction temperature of the exothermic reaction along the length of the reactor to parallel the equilibrium curve for the desired product. The converter can comprise a shell 101 and internal catalyst tubes 109. The feed gas stream enters the reactor, flows through the shell 101, and is heated by indirect heat exchange with the catalyst tubes 109. The catalyst tubes 109 comprise reactive zones 122 having catalyst and reaction limited zones 124 that can comprise inert devices that function to both separate the reactive zones, increase heat transfer area, and reduce the temperature of the reaction mixture as the effluent passes through the catalyst tube 109.
摘要翻译：公开了一种氨转化器。转化器可以通过控制沿着反应器长度的放热反应的反应温度来平行所需产物的平衡曲线来改变氨的转化率。转化器可以包括壳体101和内部催化剂管109.进料气体流进入反应器，流过壳体101，并通过与催化剂管109的间接热交换而加热。催化剂管109包含具有催化剂的反应区域122 和反应限制区124，其可以包括用于分离反应区的惰性装置，增加传热面积，并且当流出物通过催化剂管109时降低反应混合物的温度。

4. 发明授权

US07867460B2 Efficiency of ammonia processes 有权
标题翻译：氨工艺的效率
公开(公告)号：US07867460B2
公开(公告)日：2011-01-11
申请号：US12107506
申请日：2008-04-22
申请人： Shashi P. Singh , Yue Jing
发明人： Shashi P. Singh , Yue Jing
IPC分类号： B01J8/00 , B01J10/00 , B01J8/04 , C01C1/00 , F28D7/00
CPC分类号： C01C1/0423 , B01J8/0469 , B01J2208/00212 , B01J2208/0053 , C01C1/0405 , F27D17/004 , Y02P20/52
摘要： Systems and methods for producing ammonia. The system can include a first shell having two or more discrete catalyst beds disposed therein, a second shell disposed about the first shell, a first heat exchanger disposed external to the first shell and in fluid communication therewith, a second heat exchanger disposed external to the second shell and in fluid communication therewith, and a flow path disposed within the first shell. A first portion can be reacted in the presence of the catalyst to provide an ammonia effluent. The heat of reaction from the ammonia effluent can be exchanged within the first heat exchanger and the second heat exchanger. The heated second portion of the feed gas can be introduced to the first shell and can be reacted in the presence of the catalyst.
摘要翻译：用于生产氨的系统和方法。该系统可以包括具有设置在其中的两个或更多个离散催化剂床的第一壳体，围绕第一壳体设置的第二壳体，设置在第一壳体外部并与其流体连通的第一热交换器，第二壳体并与其流体连通，以及设置在第一壳体内的流路。第一部分可以在催化剂的存在下反应以提供氨流出物。来自氨流出物的反应热可以在第一热交换器和第二热交换器内进行交换。进料气体的加热的第二部分可以被引入到第一壳体中并且可以在催化剂的存在下反应。

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