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    Alumina-Coated Metal Structure and Catalyst Structure
    11.
    发明申请
    Alumina-Coated Metal Structure and Catalyst Structure 审中-公开
    氧化铝涂层金属结构和催化剂结构

    公开(公告)号：US20070232482A1

    公开(公告)日：2007-10-04

    申请号：US10566657

    申请日：2004-07-28

    Applicant: Michael Bowe ,  Clive Lee-Tuffnell ,  David Segal ,  Stuart Jones

    Inventor： Michael Bowe ,  Clive Lee-Tuffnell ,  David Segal ,  Stuart Jones

    IPC: B01J37/02

    CPC classification number: B01J37/0225 ,  B01J21/04 ,  B01J23/83 ,  B01J35/023 ,  B01J37/0242 ,  C10G2/33

    Abstract: A metal substrate is coated with a layer of ceramic, by spraying droplets of a slurry of a ceramic precursor onto the substrate, the substrate being at a temperature between 500° C. and 750° C. The ceramic comprises alumina, and is made macroporous by spraying a mixture of alumina sol and alumina particles with no more than 35% by weight of dispersible alumina. Spraying onto a red-hot surface in this fashion leads to a very marked improvement in adhesion of the resulting ceramic to the metal substrate. A catalytically active material may then be incorporated in the ceramic layer, so as to form a catalyst structure (16).

    Abstract translation: 通过将陶瓷前体的浆料的液滴喷射到基底上，将金属基底涂覆有陶瓷层，该基底处于500℃至750℃之间的温度。陶瓷包括氧化铝，并且被制成大孔 通过喷涂不超过35重量％的可分散氧化铝的氧化铝溶胶和氧化铝颗粒的混合物。 以这种方式喷涂到红热表面上导致所得陶瓷与金属基材的粘合性的显着改善。 然后可以在陶瓷层中引入催化活性材料，以便形成催化剂结构（16）。

    Valve system
    12.
    发明申请
    Valve system 失效
    阀门系统

    公开(公告)号：US20050173009A1

    公开(公告)日：2005-08-11

    申请号：US10514810

    申请日：2003-05-13

    Applicant: Michael Bowe ,  John Stairmand ,  Richard Mills

    Inventor： Michael Bowe ,  John Stairmand ,  Richard Mills

    IPC: F15C1/16 ,  F16K3/24 ,  F16K25/04 ,  F16K47/04

    CPC classification number: F15C1/16 ,  F16K3/24 ,  F16K25/04 ,  F16K47/04 ,  Y10T137/0396 ,  Y10T137/2087 ,  Y10T137/2098 ,  Y10T137/2109 ,  Y10T137/2115

    Abstract: A valve system (10) controls the fluid flow between an inlet (12) and an outlet (14). The system (10) splits the flow into two parallel flow ducts (15, 16) and recombines the flows through opposed tangential inlets (18) and (19) of a fluidic vortex valve (20) which has an axial outlet (22). An adjustable valve (24) controls the flow through one of the parallel flow ducts (15), controlling the strength of the vortex generated within the vortex valve (20). Hence a small valve (24) can control and adjust the flows in both ducts (15 and 16).

    Abstract translation: 阀系统（10）控制入口（12）和出口（14）之间的流体流动。 系统（10）将流体分成两个平行的流动管道（15,16），并将流体通过具有轴向出口（22）的流体涡旋阀（20）的相对的切向入口（18）和（19）重新组合。 可调节阀（24）控制通过平行流动管道（15）中的一个的流量，以控制在涡流阀（20）内产生的涡流的强度。 因此，小阀（24）可以控制和调节两个管道（15和16）中的流量。

    Processing biological waste materials to provide energy
    14.
    发明申请
    Processing biological waste materials to provide energy 审中-公开
    加工生物废料提供能源

    公开(公告)号：US20070029264A1

    公开(公告)日：2007-02-08

    申请号：US10557987

    申请日：2004-06-15

    Applicant: Michael Bowe

    Inventor： Michael Bowe

    IPC: C02F1/32

    CPC classification number: C02F1/36 ,  C02F3/28 ,  C10G2/30 ,  C10L3/08 ,  C12M21/04 ,  C12M43/08 ,  C12M45/02 ,  C12P5/023 ,  H01M8/0612 ,  Y02E50/343

    Abstract: Biological waste materials are mixed with water and subjected to intense ultrasonic irradiation (14), before being supplied to an anaerobic digester (16), so that a biogas is generated which contains methane. The biogas is supplied to a catalytic reformer unit (20) to form a synthesis gas; steam may also be supplied, and the proportion of steam to methane is adjustable so that the synthesis gas may be rich in hydrogen or alternatively rich in carbon monoxide. Adjusting the proportion of steam to biogas enables the output of the process to be adjusted according to market conditions. If the synthesis gas is rich in hydrogen, it may be supplied to a fuel cell (26) to generate electricity, while if it is rich in carbon monoxide, it may be used to generate liquid hydrocarbons in a Fischer-Tropsch synthesis reactor (32).

    Abstract translation: 将生物废料与水混合并进行强烈的超声波照射（14），然后供给厌氧消化器（16），以便产生含有甲烷的沼气。 将沼气供给到催化重整单元（20）以形成合成气; 还可以提供蒸汽，并且蒸汽对甲烷的比例是可调节的，使得合成气可能富含氢气或者富含一氧化碳。 调整蒸汽对沼气的比例，可以根据市场情况调整生产过程。 如果合成气富含氢气，则可将其供应给燃料电池（26）以产生电力，而如果富含一氧化碳，则其可用于在费 - 托合成反应器（32 ）。

    Catalytic reactor and process
    17.
    发明申请
    Catalytic reactor and process 有权
    催化反应器和工艺

    公开(公告)号：US20060041029A1

    公开(公告)日：2006-02-23

    申请号：US10536726

    申请日：2003-11-27

    Applicant: Michael Bowe ,  Clive Lee-Tuffnell

    Inventor： Michael Bowe ,  Clive Lee-Tuffnell

    IPC: C07C27/06

    CPC classification number: B01J19/249 ,  B01J2219/00117 ,  B01J2219/00135 ,  B01J2219/2453 ,  B01J2219/2459 ,  B01J2219/2465 ,  B01J2219/2466 ,  B01J2219/2479 ,  B01J2219/2482 ,  B01J2219/2485 ,  B01J2219/2493 ,  B01J2219/2497 ,  B01J2219/2498 ,  C10G2/341

    Abstract: Fischer-Tropsch synthesis is performed using a compact catalytic reactor unit (10) defining channels in which is a gas-permeable catalyst structure (16), the channels extending between headers (18). The synthesis occurs in at least two stages, as the reactor unit provides at least two successive channels (14, 14a) for the Fischer-Tropsch synthesis connected by a header, the gas flow velocity through the first channel being sufficiently high that no more than 65% of the carbon monoxide undergoes conversion. The gases are cooled (25) in the header between the two stages, so as to condense water vapour, and then pass through the second channel at a sufficiently high gas flow velocity that no more than 65% of the remaining carbon monoxide undergoes conversion. This lowers the partial pressure of water vapour and so suppresses oxidation of the catalyst.

    Abstract translation: 使用紧密的催化反应器单元（10）进行费 - 托合成，所述催化反应器单元限定通道，其中是透气催化剂结构（16），所述通道在集管（18）之间延伸。 合成发生在至少两个阶段，因为反应器单元为通过集管连接的费 - 托合成提供了至少两个连续的通道（14,14a），通过第一通道的气流速度足够高，不再有 超过65％的一氧化碳转化。 气体在两级之间的集管中冷却（25），以便冷凝水蒸气，然后以足够高的气体流速通过第二通道，其中不超过其余一氧化碳转化的65％。 这降低了水蒸气的分压并因此抑制了催化剂的氧化。

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