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    Cold Selective Catalytic Reduction
    11.
    发明申请
    Cold Selective Catalytic Reduction 失效
    冷选择性催化还原

    公开(公告)号：US20120195802A1

    公开(公告)日：2012-08-02

    申请号：US13441549

    申请日：2012-04-06

    Applicant: Anu Vij

    Inventor： Anu Vij

    IPC: B01D53/74

    CPC classification number: B01J8/025 ,  B01D53/8631 ,  B01D53/864 ,  B01D2251/2062 ,  B01D2257/404 ,  B01D2257/502 ,  B01D2257/7027 ,  B01D2257/708 ,  B01D2259/655 ,  B01J8/0278 ,  B01J8/0285 ,  B01J8/0426 ,  B01J8/0492 ,  B01J8/0496 ,  B01J2208/00061 ,  B01J2208/00504 ,  B01J2208/00522 ,  Y10S423/06

    Abstract: A system to control the emissions of a fluid stream in a cyclical fashion utilizing an up-flow cycle and a down-flow cycle. The system may include a first inlet and a first outlet at a first end of the system and a second inlet and a second outlet at a second end of the system, a catalyst zone between the first end and second end, two heat transfer zones, at least one heat transfer zone positioned between the catalyst zone and the first end of the system and between the catalyst zone and the second end of the system, and two heating zones, at least one heating zone positioned between the catalyst zone and each of the at least one heat transfer zones. The symmetrical arrangement permits a bi-directional fluid cycle to recover a portion of the energy supplied to the system during each cycle.

    Abstract translation: 一种利用上流循环和下流循环以循环方式控制流体流的排放的系统。 系统可以包括在系统的第一端处的第一入口和第一出口以及在系统的第二端处的第二入口和第二出口，在第一端和第二端之间的催化剂区，两个传热区， 位于催化剂区域和系统的第一端之间以及催化剂区域和系统的第二端之间的至少一个传热区域和两个加热区域，至少一个加热区域位于催化剂区域与每个催化剂区域之间 至少一个传热区。 对称布置允许双向流体循环在每个循环期间恢复供应给系统的能量的一部分。

    Cold selective catalytic reduction
    12.
    发明授权
    Cold selective catalytic reduction 失效
    冷选择性催化还原

    公开(公告)号：US08153090B2

    公开(公告)日：2012-04-10

    申请号：US12899328

    申请日：2010-10-06

    Applicant: Anu Vij

    Inventor： Anu Vij

    IPC: B01D53/86 ,  B01J8/04 ,  B01J19/00 ,  G05D7/00

    CPC classification number: B01J8/025 ,  B01D53/8631 ,  B01D53/864 ,  B01D2251/2062 ,  B01D2257/404 ,  B01D2257/502 ,  B01D2257/7027 ,  B01D2257/708 ,  B01D2259/655 ,  B01J8/0278 ,  B01J8/0285 ,  B01J8/0426 ,  B01J8/0492 ,  B01J8/0496 ,  B01J2208/00061 ,  B01J2208/00504 ,  B01J2208/00522 ,  Y10S423/06

    Abstract: A system to control the emissions of a fluid stream in a cyclical fashion utilizing an up-flow cycle and a down-flow cycle. The system may include a first inlet and a first outlet at a first end of the system and a second inlet and a second outlet at a second end of the system, a catalyst zone between the first end and second end, two heat transfer zones, at least one heat transfer zone positioned between the catalyst zone and the first end of the system and between the catalyst zone and the second end of the system, and two heating zones, at least one heating zone positioned between the catalyst zone and each of the at least one heat transfer zones. The symmetrical arrangement permits a bi-directional fluid cycle to recover a portion of the energy supplied to the system during each cycle.

    Abstract translation: 一种利用上流循环和下流循环以循环方式控制流体流的排放的系统。 系统可以包括在系统的第一端处的第一入口和第一出口以及在系统的第二端处的第二入口和第二出口，在第一端和第二端之间的催化剂区，两个传热区， 位于催化剂区域和系统的第一端之间以及催化剂区域和系统的第二端之间的至少一个传热区域和两个加热区域，至少一个加热区域位于催化剂区域与每个催化剂区域之间 至少一个传热区。 对称布置允许双向流体循环在每个循环期间恢复供应给系统的能量的一部分。

    Method for a burner and a corresponding device
    13.
    发明授权
    Method for a burner and a corresponding device 有权
    燃烧器和相应装置的方法

    公开(公告)号：US07666367B1

    公开(公告)日：2010-02-23

    申请号：US10069261

    申请日：2000-07-03

    Applicant: Franz Durst ,  Jürgen Künzel

    Inventor： Franz Durst ,  Jürgen Künzel

    IPC: B01J19/00 ,  F23D14/02 ,  F23D14/12

    CPC classification number: F23C99/006 ,  B01D53/34 ,  B01J8/0426 ,  B01J2208/00061 ,  B01J2208/00132 ,  B01J2208/00256 ,  B01J2208/00274 ,  B01J2208/00513 ,  B01J2219/00263 ,  B01J2219/0272 ,  C01B7/01 ,  C01B7/012 ,  C01B7/0737 ,  F23D14/02 ,  F23L7/00 ,  F23L2900/07002 ,  F23L2900/07009

    Abstract: The invention relates to a device equipped with a burner for combusting a fuel/oxidant mixture inside a combustion chamber in which a material (3, 3′, 3″, 3′″) is provided that endures a maximum temperature. The inventive device also comprises one or more supply lines (25, 26) for the fuel as well as for the oxidant which are provided for supplying the same into the combustion chamber. The inventive device is characterized in that it is designed for carrying out a combustion with a combustion temperature of the fuel/oxidant mixture that exceeds the maximum temperature. The device is designed in such a way that at least one additional supply line (30) is provided via which an additional gas having, in particular, a low calorific value can be supplied to the combustion chamber. Said additional gas enables the temperature during combustion to be lowered to a value that is less than the maximum temperature.

    Abstract translation: 本发明涉及一种装备有用于在燃烧室内燃烧燃料/氧化剂混合物的燃烧器的装置，在该燃烧室内设有耐受最高温度的材料（3,3'，3“，3”“）。 本发明的装置还包括一个或多个用于燃料的供应管线（25,26）以及用于将氧气供应到燃烧室中的氧化剂。 本发明的装置的特征在于，其被设计用于燃烧燃料/氧化剂混合物的燃烧温度超过最高温度。 设备的设计方式是至少提供一个额外的供应管线（30），经由该至少一个附加的供应管线（30）可以向燃烧室提供特别是低热值的附加气体。 所述附加气体使燃烧期间的温度降低到小于最高温度的值。

    Process for effecting mass transfer between a liquid phase and a gaseous phase
    15.
    发明授权
    Process for effecting mass transfer between a liquid phase and a gaseous phase 有权
    用于在液相和气相之间进行质量传递的方法

    公开(公告)号：US07014177B2

    公开(公告)日：2006-03-21

    申请号：US10230058

    申请日：2002-08-29

    Applicant: Ermanno Filippi

    Inventor： Ermanno Filippi

    IPC: B01F3/04

    CPC classification number: B01D3/16 ,  B01J8/008 ,  B01J8/0415 ,  B01J8/0426 ,  B01J8/0496 ,  B01J19/305 ,  B01J19/325 ,  B01J2208/00106 ,  B01J2208/00212 ,  B01J2208/00884 ,  B01J2219/00024

    Abstract: A process for effecting mass transfer between a liquid phase and a gaseous phase in a filled-type column having an external shell which accommodates at least one filler-containing basket wherethrough the phases are caused to flow in countercurrent relationship. The process includes the step of feeding the gaseous phase to the at least one basket through a gas-permeable surface thereof which is larger than the basket cross-section, preferably in a prevailing radial flow direction.

    Abstract translation: 在具有外壳的填充型柱中进行液相和气相之间的质量传递的方法，所述外壳容纳至少一个含有填料的篮，通过这些相以相逆流的方式流动。 该方法包括以下步骤：将气相通过其大于篮横截面的气体可渗透表面送入至少一个篮子，优选地以主要的径向流动方向。

    Method for carrying out a chemical reaction
    16.
    发明授权
    Method for carrying out a chemical reaction 失效
    进行化学反应的方法

    公开(公告)号：US06482375B1

    公开(公告)日：2002-11-19

    申请号：US08930943

    申请日：1998-01-15

    Applicant: Willem Johan Jacob van der Wal ,  Antonius Johannes Maria van Wingerden ,  Anthony van Waveren ,  Erik Alexander Polman ,  Alette Mulder

    Inventor： Willem Johan Jacob van der Wal ,  Antonius Johannes Maria van Wingerden ,  Anthony van Waveren ,  Erik Alexander Polman ,  Alette Mulder

    IPC: B01J802

    CPC classification number: B01J8/0426 ,  B01J8/0285 ,  B01J8/0423 ,  B01J12/007 ,  B01J19/2485 ,  B01J2208/00309 ,  Y10S423/06

    Abstract: The invention relates to a method for carrying out two chemical reactions in a reactor system comprising at least two mutually separate reactor beds, of which the surfaces exposed to the reactants are catalytically active for the chemical reactions concerned, and at least one partition; wherein at least one first reactor bed is present, which is bounded by at least one partition, which bed is based on a continuous porous structure extending throughout the reactor, and which bed is fixedly connected to said partition; wherein at least one second bed is preset, which is based on a continuous porous structure extending throughout the reactor, and which bed is fixedly connected to said partition, and said second bed, with respect to the first bed, is disposed on the other side of said partition, so that a heat-exchanging contact between said beds is present and the reaction heat of a first chemical reaction carried out in said first reactor bed is supplied or absorbed by carrying out a second chemical reaction in said second bed.

    Abstract translation: 本发明涉及一种在反应器系统中进行两次化学反应的方法，该反应器系统包括至少两个相互分离的反应器床，其中暴露于反应物的表面对于所涉及的化学反应具有催化活性，并且至少有一个隔板; 其中存在至少一个第一反应器床，该第一反应器床由至少一个隔板限定，该床基于延伸穿过整个反应器的连续多孔结构，并且该床固定地连接到所述隔板; 其中预设至少一个第二床，其基于延伸穿过所述反应器的连续多孔结构，并且所述床固定地连接到所述隔板，并且所述第二床相对于所述第一床设置在另一侧 所述隔板之间存在热交换接触，并且通过在所述第二床中进行第二化学反应来供应或吸收在所述第一反应器床中进行的第一化学反应的反应热。

    Hydrogen-producing fuel processing assemblies, heating assemblies, and methods of operating the same
    17.
    发明授权
    Hydrogen-producing fuel processing assemblies, heating assemblies, and methods of operating the same 有权
    制氢燃料加工组件，加热组件及其操作方法

    公开(公告)号：US07939051B2

    公开(公告)日：2011-05-10

    申请号：US11751417

    申请日：2007-05-21

    Applicant: Vernon Wade Popham ,  Curtiss Renn ,  Mesa Scharf ,  Kyle Taylor

    Inventor： Vernon Wade Popham ,  Curtiss Renn ,  Mesa Scharf ,  Kyle Taylor

    IPC: C01B3/26

    CPC classification number: C01B3/384 ,  B01J8/0426 ,  B01J8/0496 ,  B01J2208/00398 ,  B01J2208/00415 ,  B01J2208/00504 ,  B01J2208/00646 ,  B01J2208/00716 ,  C01B3/382 ,  C01B2203/0233 ,  C01B2203/04 ,  C01B2203/06 ,  C01B2203/0811 ,  C01B2203/085 ,  C01B2203/0866 ,  C01B2203/1288 ,  C01B2203/146 ,  C01B2203/1604

    Abstract: Hydrogen-producing fuel processing assemblies, including steam reforming fuel processing assemblies, startup assemblies for use therein, and methods of operating the same. In some embodiments, the startup assemblies include a startup reforming region that is upstream from a primary, or second, hydrogen-producing reforming region. In some embodiments, the startup reforming region and primary reforming regions are both steam reforming regions. In some embodiments, the startup assembly further includes at least one of a vaporization region and a startup heating assembly. In some embodiments, the startup heating assembly is an electrically powered heating assembly, and the fuel processing assembly further includes a (primary) heating assembly that combusts a byproduct stream from the fuel processing assembly to produce a combustion exhaust stream. In some embodiments, the startup reforming region is adapted to produce a gaseous output stream that will remain a gas-phase stream even if cooled below a minimum hydrogen-producing temperature.

    Abstract translation: 制氢燃料处理组件，包括蒸汽重整燃料处理组件，用于其中的启动组件及其操作方法。 在一些实施方案中，启动组件包括起始重整区域，其在第一或第二制氢重整区域的上游。 在一些实施方案中，启动重整区域和初级重整区域都是蒸汽重整区域。 在一些实施例中，启动组件还包括蒸发区域和启动加热组件中的至少一个。 在一些实施例中，启动加热组件是电动加热组件，并且燃料处理组件还包括（主）加热组件，其燃烧来自燃料处理组件的副产物流以产生燃烧废气流。 在一些实施方案中，启动重整区域适于产生气体输出流，即使在低于最低产氢温度下冷却时仍保持气相流。

    COLD SELECTIVE CATALYTIC REDUCTION
    18.
    发明申请
    COLD SELECTIVE CATALYTIC REDUCTION 失效
    冷选择性催化还原

    公开(公告)号：US20110081285A1

    公开(公告)日：2011-04-07

    申请号：US12899328

    申请日：2010-10-06

    Applicant: Anu Vij

    Inventor： Anu Vij

    IPC: B01D53/86 ,  B01J19/00 ,  B01J8/04 ,  G05D7/00

    CPC classification number: B01J8/025 ,  B01D53/8631 ,  B01D53/864 ,  B01D2251/2062 ,  B01D2257/404 ,  B01D2257/502 ,  B01D2257/7027 ,  B01D2257/708 ,  B01D2259/655 ,  B01J8/0278 ,  B01J8/0285 ,  B01J8/0426 ,  B01J8/0492 ,  B01J8/0496 ,  B01J2208/00061 ,  B01J2208/00504 ,  B01J2208/00522 ,  Y10S423/06

    Abstract: A system to control the emissions of a fluid stream in a cyclical fashion utilizing an up-flow cycle and a down-flow cycle. The system may include a first inlet and a first outlet at a first end of the system and a second inlet and a second outlet at a second end of the system, a catalyst zone between the first end and second end, two heat transfer zones, at least one heat transfer zone positioned between the catalyst zone and the first end of the system and between the catalyst zone and the second end of the system, and two heating zones, at least one heating zone positioned between the catalyst zone and each of the at least one heat transfer zones. The symmetrical arrangement permits a bi-directional fluid cycle to recover a portion of the energy supplied to the system during each cycle.

    Abstract translation: 一种利用上流循环和下流循环以循环方式控制流体流的排放的系统。 系统可以包括在系统的第一端处的第一入口和第一出口以及在系统的第二端处的第二入口和第二出口，在第一端和第二端之间的催化剂区，两个传热区， 位于催化剂区域和系统的第一端之间以及催化剂区域和系统的第二端之间的至少一个传热区域和两个加热区域，至少一个加热区域位于催化剂区域与每个催化剂区域之间 至少一个传热区。 对称布置允许双向流体循环在每个循环期间恢复供应给系统的能量的一部分。

    HYDROGEN-PRODUCING FUEL PROCESSING ASSEMBLIES, HEATING ASSEMBLIES, AND METHODS OF OPERATING THE SAME
    20.
    发明申请
    HYDROGEN-PRODUCING FUEL PROCESSING ASSEMBLIES, HEATING ASSEMBLIES, AND METHODS OF OPERATING THE SAME 有权
    生产燃料的加氢装置，加热装置及其操作方法

    公开(公告)号：US20070274904A1

    公开(公告)日：2007-11-29

    申请号：US11751417

    申请日：2007-05-21

    Applicant: Vernon Wade Popham ,  Curtiss Renn ,  Mesa Scharf ,  Kyle Taylor

    Inventor： Vernon Wade Popham ,  Curtiss Renn ,  Mesa Scharf ,  Kyle Taylor

    IPC: C01B3/26 ,  B01J19/00

    CPC classification number: C01B3/384 ,  B01J8/0426 ,  B01J8/0496 ,  B01J2208/00398 ,  B01J2208/00415 ,  B01J2208/00504 ,  B01J2208/00646 ,  B01J2208/00716 ,  C01B3/382 ,  C01B2203/0233 ,  C01B2203/04 ,  C01B2203/06 ,  C01B2203/0811 ,  C01B2203/085 ,  C01B2203/0866 ,  C01B2203/1288 ,  C01B2203/146 ,  C01B2203/1604

    Abstract: Hydrogen-producing fuel processing assemblies, including steam reforming fuel processing assemblies, startup assemblies for use therein, and methods of operating the same. In some embodiments, the startup assemblies include a startup reforming region that is upstream from a primary, or second, hydrogen-producing reforming region. In some embodiments, the startup reforming region and primary reforming regions are both steam reforming regions. In some embodiments, the startup assembly further includes at least one of a vaporization region and a startup heating assembly. In some embodiments, the startup heating assembly is an electrically powered heating assembly, and the fuel processing assembly further includes a (primary) heating assembly that combusts a byproduct stream from the fuel processing assembly to produce a combustion exhaust stream. In some embodiments, the startup reforming region is adapted to produce a gaseous output stream that will remain a gas-phase stream even if cooled below a minimum hydrogen-producing temperature.

    Abstract translation: 制氢燃料处理组件，包括蒸汽重整燃料处理组件，用于其中的启动组件及其操作方法。 在一些实施方案中，启动组件包括起始重整区域，其在第一或第二制氢重整区域的上游。 在一些实施方案中，启动重整区域和初级重整区域都是蒸汽重整区域。 在一些实施例中，启动组件还包括蒸发区域和启动加热组件中的至少一个。 在一些实施例中，启动加热组件是电动加热组件，并且燃料处理组件还包括（主）加热组件，其燃烧来自燃料处理组件的副产物流以产生燃烧废气流。 在一些实施方案中，启动重整区域适于产生气体输出流，即使在低于最低产氢温度下冷却时仍保持气相流。

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