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    Lock hopper mass flow arrangement
    2.
    发明授权
    Lock hopper mass flow arrangement 有权
    锁料斗质量流量排列

    公开(公告)号：US09169062B2

    公开(公告)日：2015-10-27

    申请号：US13173231

    申请日：2011-06-30

    申请人： Edwin V. Reece ,  John Abughazaleh ,  Michael J. Sandefur ,  David P. Mann

    发明人： Edwin V. Reece ,  John Abughazaleh ,  Michael J. Sandefur ,  David P. Mann

    IPC分类号： B65G53/38 ,  B65D88/64 ,  B65D88/70

    CPC分类号： B65D88/64 ,  B65D88/70

    摘要： Methods, systems, and apparatus for mass flow are provided. The apparatus can include a housing, an inlet disposed at a first end of the housing, and an outlet disposed at a second end of the housing. The housing can include a first section and a second section. The second section can have at least one tapered sidewall that slopes away from an inner surface of the first section toward the outlet. The apparatus can also include a divider disposed at least partially within the first and second sections of the housing. The divider can have at least one tapered surface disposed proximate the at least one tapered sidewall of the second section. An edge of the divider can be located between the outlet and a point within the second section where the cross-sectional area of the second section is about three times or less a cross-sectional area of the outlet.

    摘要翻译： 提供了用于质量流量的方法，系统和装置。 该装置可以包括壳体，设置在壳体的第一端处的入口和设置在壳体的第二端处的出口。 壳体可以包括第一部分和第二部分。 第二部分可以具有至少一个锥形侧壁，其从第一部分的内表面向着出口倾斜。 该装置还可以包括至少部分地设置在壳体的第一和第二部分内的分隔件。 分隔件可以具有靠近第二部分的至少一个锥形侧壁设置的至少一个锥形表面。 分隔件的边缘可以位于出口和第二部分内的点之间，其中第二部分的横截面面积为出口的横截面面积的约三倍或更小。

    LOCK HOPPER MASS FLOW ARRANGEMENT
    3.
    发明申请
    LOCK HOPPER MASS FLOW ARRANGEMENT 有权

    公开(公告)号：US20130004247A1

    公开(公告)日：2013-01-03

    申请号：US13173231

    申请日：2011-06-30

    申请人： Edwin V. Reece ,  John Abughazaleh ,  Michael J. Sandefur ,  David P. Mann

    发明人： Edwin V. Reece ,  John Abughazaleh ,  Michael J. Sandefur ,  David P. Mann

    IPC分类号： B65G53/40 ,  B65G69/00 ,  B65G69/06

    CPC分类号： B65D88/64 ,  B65D88/70

    摘要： Methods, systems, and apparatus for mass flow are provided. The apparatus can include a housing, an inlet disposed at a first end of the housing, and an outlet disposed at a second end of the housing. The housing can include a first section and a second section. The second section can have at least one tapered sidewall that slopes away from an inner surface of the first section toward the outlet. The apparatus can also include a divider disposed at least partially within the first and second sections of the housing. The divider can have at least one tapered surface disposed proximate the at least one tapered sidewall of the second section. An edge of the divider can be located between the outlet and a point within the second section where the cross-sectional area of the second section is about three times or less a cross-sectional area of the outlet.

    摘要翻译： 提供了用于质量流量的方法，系统和装置。 该装置可以包括壳体，设置在壳体的第一端处的入口和设置在壳体的第二端处的出口。 壳体可以包括第一部分和第二部分。 第二部分可以具有至少一个锥形侧壁，其从第一部分的内表面向着出口倾斜。 该装置还可以包括至少部分地设置在壳体的第一和第二部分内的分隔件。 分隔件可以具有靠近第二部分的至少一个锥形侧壁设置的至少一个锥形表面。 分隔件的边缘可以位于出口和第二部分内的点之间，其中第二部分的横截面面积为出口的横截面面积的约三倍或更小。

    Maximum reaction rate converter system for exothermic reactions
    6.
    发明授权
    Maximum reaction rate converter system for exothermic reactions 有权
    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。

    Maximum reaction rate converter process for exothermic reactions
    9.
    发明授权
    Maximum reaction rate converter process for exothermic reactions 有权
    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。