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    Catalytic plant and process
    3.
    发明申请
    Catalytic plant and process 失效
    催化工厂和工艺

    公开(公告)号：US20050282918A1

    公开(公告)日：2005-12-22

    申请号：US11140884

    申请日：2005-06-01

    Applicant: Michael Bowe

    Inventor： Michael Bowe

    IPC: B01J8/02 ,  B01J8/04 ,  B01J19/00 ,  B01J19/24 ,  C10G2/00 ,  C07C27/06

    CPC classification number: C10G2/341 ,  B01J19/0093 ,  B01J19/249 ,  B01J2219/0002 ,  B01J2219/00835 ,  B01J2219/00867 ,  B01J2219/00869 ,  B01J2219/00871 ,  B01J2219/00873 ,  B01J2219/2453 ,  B01J2219/2458 ,  B01J2219/2459 ,  B01J2219/2462 ,  B01J2219/2479

    Abstract: Fischer-Tropsch synthesis is performed on a CO/H*2 feed gas using a plurality of compact catalytic reactor modules (12) each defining catalytic reaction channels and coolant channels, in two successive stages, with the same number of reactor modules for each stage. The gas flow velocity in the first stage is sufficiently high that no more than 75% of the CO undergoes conversion. The gases are cooled (16) between successive stages so as to remove water vapour, and the pressure is reduced (20) before they are subjected to the second stage. In addition the reaction temperature for the second stage is lower than for the first stage, such that no more than 75% of the remaining carbon monoxide undergoes conversion during the second stage too. The deleterious effect of water vapour on the catalyst is hence suppressed, while the overall capacity of the plant (10) can be adjusted by closing off modules in each stage while keeping the numbers equal.

    Abstract translation: 使用多个紧凑型催化反应器模块（12）在CO / H * 2进料气体上进行费 - 托合成，每个紧凑型催化反应器模块（12）在两个连续阶段中分别定义催化反应通道和冷却剂通道，每个阶段具有相同数量的反应器模块 。 第一级中的气体流速足够高，不超过75％的CO经历转化。 气体在连续的阶段之间被冷却（16），以便除去水蒸汽，并且在进行第二阶段之前压力降低（20）。 此外，第二阶段的反应温度低于第一阶段的反应温度，使得在第二阶段期间不超过75％的剩余一氧化碳也经历转化。 因此，可以抑制水蒸气对催化剂的有害影响，同时可以通过在保持数字相等的情况下关闭每个阶段中的模块来调整设备（10）的整体容量。

    Catalytic reactor
    4.
    发明申请
    Catalytic reactor 失效
    催化反应器

    公开(公告)号：US20050013769A1

    公开(公告)日：2005-01-20

    申请号：US10491782

    申请日：2002-09-12

    Applicant: Michael Bowe ,  Clive Lee-Tuffnell

    Inventor： Michael Bowe ,  Clive Lee-Tuffnell

    IPC: B01J19/24 ,  B01J23/40 ,  B01J23/75 ,  B01J23/89 ,  B01J35/04 ,  B01J35/06 ,  B01J37/02 ,  C01B3/38 ,  C10G2/00 ,  F28D9/00 ,  F28F3/04 ,  B01J8/02 ,  B01J35/02 ,  C01B3/26

    CPC classification number: C10G2/341 ,  B01J19/249 ,  B01J23/40 ,  B01J23/75 ,  B01J23/8913 ,  B01J35/04 ,  B01J35/06 ,  B01J37/0225 ,  B01J37/0226 ,  B01J37/0242 ,  B01J2219/2453 ,  B01J2219/2465 ,  B01J2219/247 ,  B01J2219/2472 ,  B01J2219/2479 ,  B01J2219/2485 ,  B01J2219/2497 ,  B01J2219/2498 ,  C01B3/384 ,  C01B2203/0233 ,  C01B2203/0811 ,  C01B2203/1035 ,  C01B2203/1052 ,  C01B2203/1082 ,  C01B2203/1241 ,  F28D9/0037 ,  F28D9/0093 ,  F28F3/04 ,  Y02P20/52

    Abstract: A catalytic reactor (20) comprises a plurality of sheets (21) defining flow channels (22) between them. Within each flow channel (22) is a foil (24) of corrugated material whose surfaces are coated with catalytic material. Flow channels (22, 22a) for a first gas extend in oblique directions relative to the flow channels (22b) for a second gas. The reactor (20) incorporates header chambers (26, 28) to supply gas mixtures to the flow channels (22), the headers communicating with adjacent channels being separate. The reactor (20) enables different gas mixtures to be supplied to adjacent channels (22), which may be at different pressures, and the corresponding chemical reactions are also different. Where one of the reactions is endothermic while the other reaction is exothermic, heat is transferred through the sheets (21) separating the endothermic reaction. When the catalyst is one set of flow channels becomes spent, it can be replaced by removing a header. The reactor (20) may be used in a compact plant to perform steam/methane reforming, obtaining the necessary heat by catalytic methane combustion, and also for Fisher-Tropsch synthesis, so that the overall process involves conversion of methane to long-chain hydrocarbons.

    Abstract translation: 催化反应器（20）包括在它们之间限定流动通道（22）的多个片材（21）。 在每个流动通道（22）内是波纹材料的箔（24），其表面涂覆有催化材料。 用于第一气体的流动通道（22,22a）相对于用于第二气体的流动通道（22b）在倾斜方向上延伸。 反应器（20）包括集管室（26,28）以将气体混合物供应到流动通道（22），与相邻通道连通的集管是分离的。 反应器（20）使不同的气体混合物能够供应到邻近的通道（22），相邻的通道（22）可能处于不同的压力，相应的化学反应也不同。 其中一个反应是吸热的，而另一个反应是放热的，热量通过分离吸热反应的片（21）转移。 当催化剂是一组流动通道消耗时，可以通过去除集管来代替催化剂。 反应器（20）可用于紧凑型工厂中以进行蒸汽/甲烷重整，通过催化甲烷燃烧获得必要的热量，还可用于费 - 托合成，以使整个方法涉及将甲烷转化成长链烃 。

    Valve assembly
    6.
    发明申请
    Valve assembly 失效
    阀组件

    公开(公告)号：US20060076065A1

    公开(公告)日：2006-04-13

    申请号：US10519195

    申请日：2003-05-22

    Applicant: Michael Bowe

    Inventor： Michael Bowe

    IPC: F16K11/04

    CPC classification number: F16K1/123 ,  F16K3/265 ,  F16K47/08 ,  Y10T137/86759

    Abstract: A valve assembly (10) comprises a valve stem (14) with a bore (15) and radial apertures (17), and a sleeve (18) closed atone end and slidable over the valve stem (14) to obstruct the apertures (17). At the end of the valve stem opposite the outlet end, the valve stem (14) defines a fluidic vortex chamber (22) with both tangential inlets (28) and non-tangential peripheral inlets (26), and with an axial outlet (24) communicating with the bore (15). The sleeve (18) defines at least one radial port (32) near its closed end. The valve assembly operates in a conventional fashion except when approaching closure. Once the last of the apertures (17) in the valve stem has been closed, the only flow path is through the fluidic vortex chamber (22). Further movement of the sleeve (18) alters the distribution of the flow between the non-tangential inlets (26) and the tangential inlets (28), so adjusting the strength of the fluidic vortex and the resistance to fluid flow. The valve assembly (10) suppresses erosive and cavitational wear of the valve mechanism, and can provide a wide range of flow modulation.

    Abstract translation: 阀门组件（10）包括具有孔（15）和径向孔（17）的阀杆（14）和封闭在一端的套筒（18），并可在阀杆（14）上方滑动以阻塞孔（17） ）。 在阀杆的与出口端相对的端部处，阀杆（14）限定具有两个切向入口（28）和非切向外围入口（26）的流体涡流室（22），并且具有轴向出口（24） ）与孔（15）连通。 套筒（18）在其封闭端附近限定至少一个径向端口（32）。 阀门组件以常规方式操作，除非接近闭合。 一旦阀杆中最后的孔（17）已经关闭，则唯一的流动路径是通过流体涡流室（22）。 套筒（18）的进一步运动改变非切向入口（26）和切向入口（28）之间的流动分布，从而调节流体涡流的强度和对流体流动的抵抗力。 阀组件（10）抑制阀机构的腐蚀性和空穴磨损，并且可以提供宽范围的流动调节。

    Catalytic reactors
    9.
    发明申请
    Catalytic reactors 失效
    催化反应器

    公开(公告)号：US20050234138A1

    公开(公告)日：2005-10-20

    申请号：US11105371

    申请日：2005-04-14

    Applicant: Michael Bowe

    Inventor： Michael Bowe

    IPC: B01J19/24 ,  C10G2/00 ,  B01J8/04 ,  C07C27/06

    CPC classification number: B01J19/249 ,  B01J2219/00006 ,  B01J2219/2453 ,  B01J2219/2458 ,  B01J2219/2459 ,  B01J2219/2462 ,  B01J2219/2465 ,  B01J2219/247 ,  B01J2219/2479 ,  B01J2219/2482 ,  B01J2219/2485 ,  B01J2219/2486 ,  B01J2219/2493 ,  B01J2219/2496 ,  B01J2219/2497 ,  B01J2219/2498 ,  C10G2/341

    Abstract: A compact catalytic reactor comprises a stack of plates (72, 74, 75) to define a multiplicity of first and second flow channels arranged alternately in the stack; each flow channel in which a chemical reaction is to take place is defined by straight-through channels across at least one plate, each such straight-through channel containing a removable gas-permeable catalyst structure (80) incorporating a metal substrate. The first flow channels (76) are oriented in a direction that is perpendicular to that of the second flow channels (77), and between successive second flow channels in the stack the reactor defines at least three side-by-side first flow channels (76); and the reactor incorporates flow diversion means (80; 88) such that the first fluid must flow through at least three such first flow channels (76) in succession, in flowing from an inlet to an outlet. The overall flow paths can therefore be approximately co-current or counter-current.

    Abstract translation: 紧凑型催化反应器包括一叠板（72,74,75），用于限定交替布置在堆叠中的多个第一和第二流动通道; 要在其中进行化学反应的每个流动通道由穿过至少一个板的直通通道限定，每个这样的直通通道包含结合有金属基底的可移除气体可渗透的催化剂结构（80）。 第一流动通道（76）在垂直于第二流动通道（77）的方向上定向，并且在堆叠中的连续的第二流动通道之间，反应器限定了至少三个并排的第一流动通道 76）; 并且所述反应器包括流动分流装置（80; 88），使得所述第一流体必须在从入口流到出口的过程中依次流过至少三个所述第一流动通道（76）。 因此，整个流动路径可以是大致并流或逆流的。

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