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31. 发明申请

US20080226517A1 Catalytic Reactor 审中-公开
标题翻译：催化反应器
公开(公告)号：US20080226517A1
公开(公告)日：2008-09-18
申请号：US11813866
申请日：2005-12-19
申请人： John Vitucci , Michael Joseph Bowe
发明人： John Vitucci , Michael Joseph Bowe
IPC分类号： B01J19/00
CPC分类号： B01J19/249 , B01J2219/2453 , B01J2219/2458 , B01J2219/2459 , B01J2219/2464 , B01J2219/2465 , B01J2219/2467 , B01J2219/247 , B01J2219/2472 , B01J2219/2479 , B01J2219/2482 , B01J2219/2486 , B01J2219/2493 , B01J2219/2497 , B01J2219/2498 , C01B3/382 , C01B3/384 , C01B2203/0233 , C01B2203/062 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0894 , C01B2203/1005 , C01B2203/1047 , C01B2203/1058 , C01B2203/107 , C01B2203/1241 , C01B2203/142 , C01B2203/84 , C10G2/32 , Y02P20/128 , Y02P20/52
摘要： A compact catalytic reactor (20) for reforming comprises a reactor module (70) to define a multiplicity of first and second flow channels arranged alternately, for carrying first and second gas flows, and a removable gas-permeable catalyst structure (80) with a substrate for example of metal foil is provided in each flow channel in which a chemical reaction is to occur. The reactor is for use with a first gas flow whose pressure is above ambient pressure and is no less than that of the second gas flow. The reactor module (70) may be formed of a stack of plates (72, 74, 75). The module (70) is enclosed within a pressure vessel (90), the pressure within the pressure vessel being arranged to be at a pressure substantially that of the first gas flow. Consequently no parts of the module (70) are under tension. This simplifies the design of the reactor module, and increases the proportion of its volume occupied by the catalyst.
摘要翻译：用于重整的紧凑型催化反应器（20）包括反应器模块（70），用于限定交替布置的用于承载第一和第二气流的多个第一和第二流动通道，以及可移除的透气催化剂结构（80），其具有在其中将发生化学反应的每个流动通道中提供例如金属箔的基底。该反应器用于压力高于环境压力且不小于第二气流的第一气流。反应器模块（70）可以由一堆板（72,74,75）形成。模块（70）被包围在压力容器（90）内，压力容器内的压力被设置成基本上是第一气流的压力。因此，模块（70）的任何部分没有受到张力。这简化了反应器模块的设计，并增加了其由催化剂占据的体积的比例。

32. 发明申请

US20070056247A1 Combustion of gaseous fuel 审中-公开
标题翻译：气体燃料燃烧
公开(公告)号：US20070056247A1
公开(公告)日：2007-03-15
申请号：US10557994
申请日：2004-06-21
申请人： Michael Joseph Bowe
发明人： Michael Joseph Bowe
IPC分类号： E04F21/00
CPC分类号： F23C13/00 , C10J3/00 , C10J3/86 , C10J2300/0916 , C10J2300/093 , C10J2300/0956 , C10J2300/1884 , C10J2300/1892 , C10K1/004 , C10K1/024 , C10K1/026 , C10K3/023 , F23C13/08 , F23C2900/99008 , Y02E20/346 , Y02P20/145
摘要： A fuel gas is passed into one set of channels in a compact reactor (12) consisting of a plurality of metal sheets (41) arranged to define first and second gas flow channels (14 and 15), the channels being arranged alternately to ensure good thermal contact between the gases in them and each channel containing a removable metallic heat conducting insert (44) coated with a ceramic. In the set of channels carrying the fuel the ceramic supports particles of a transition metal oxide, which is reduced by the combustion gas to form metal particles. In the other set of channels the ceramic supports particles of a transition metal, and these channels carry a flow of an oxidizing gas, which oxidises the metal. The flows to the two sets of channels are then exchanged. If the oxidizing gas is steam, the result is a stream of pure hydrogen.
摘要翻译：燃料气体在由多个设置成限定第一和第二气体流动通道（14和15）的多个金属板（41）组成的紧凑型反应器（12）中进入一组通道，所述通道交替布置以确保良好它们之间的气体和每个通道之间的热接触包含涂覆有陶瓷的可移除的金属导热插入件（44）。在承载燃料的一组通道中，陶瓷支持过渡金属氧化物的颗粒，其被燃烧气体还原以形成金属颗粒。在另一组通道中，陶瓷支持过渡金属的颗粒，并且这些通道携带氧化气体的流动，氧化气体使金属氧化。然后交换到两组信道的流。如果氧化气体是蒸汽，结果是纯氢气流。

33. 发明授权

US07067561B2 Catalytic plant and process 失效
标题翻译：催化工厂和工艺
公开(公告)号：US07067561B2
公开(公告)日：2006-06-27
申请号：US11140884
申请日：2005-06-01
申请人： Michael Joseph Bowe
发明人： Michael Joseph Bowe
IPC分类号： C07C27/00 , B01J8/18 , B01J10/00 , F27B15/14
CPC分类号： 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
摘要： 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.
摘要翻译：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。

34. 发明申请

US20130041049A1 Gas-to-Liquid Technology 有权
标题翻译：气液技术
公开(公告)号：US20130041049A1
公开(公告)日：2013-02-14
申请号：US13638009
申请日：2011-04-27
申请人： Michael Joseph Bowe , Robert Peat , David James West , Philip Hawker
发明人： Michael Joseph Bowe , Robert Peat , David James West , Philip Hawker
IPC分类号： C07C37/68 , B01J19/00
CPC分类号： C01B3/34 , C01B2203/0233 , C01B2203/0244 , C01B2203/025 , C01B2203/0405 , C01B2203/043 , C01B2203/062 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/0872 , C01B2203/0894 , C01B2203/1064 , C01B2203/1241 , C01B2203/148 , C07C1/04 , C10G2/32 , C10G2300/1025 , C10L3/10 , Y02P20/128
摘要： A gas-to-liquids process and plant for treating natural gas, in which the natural gas is subjected to expansion through a flow restrictor so as to undergo cooling through the Joule Thomson effect, enables liquids to be separated from the gas stream. The natural gas may be cooled before it reaches the flow restrictor by heat exchange with fluid that has passed through the flow restrictor. This decreases the proportion of longer-chain hydrocarbons in the natural gas, which may simplify subsequent processing, and may enable the size of the plant to be decreased.
摘要翻译：用于处理天然气的气体 - 液体方法和设备，其中天然气通过限流器进行膨胀以通过焦耳汤姆森效应进行冷却，使液体能够与气流分离。天然气可以在通过与通过限流器的流体进行热交换而到达限流器之前被冷却。这降低了天然气中长链烃的比例，这可以简化后续处理，并且可以使得设备的尺寸减小。

35. 发明申请

US20110194997A1 Catalytic Reactor 失效
标题翻译：催化反应器
公开(公告)号：US20110194997A1
公开(公告)日：2011-08-11
申请号：US13122669
申请日：2009-10-21
申请人： Anthony Henry Reading , Ian Kenneth Baxter , Michael Joseph Bowe
发明人： Anthony Henry Reading , Ian Kenneth Baxter , Michael Joseph Bowe
IPC分类号： B01J8/04 , B23P19/04
CPC分类号： B01J19/249 , B01J2219/185 , B01J2219/2453 , B01J2219/2458 , B01J2219/2459 , B01J2219/2465 , B01J2219/2466 , B01J2219/2472 , B01J2219/2474 , B01J2219/2479 , B01J2219/2482 , B01J2219/2485 , B01J2219/2498 , Y10T29/49751 , Y10T29/53
摘要： A compact catalytic reactor defines a multiplicity of first and second flow channels arranged alternately, for an endothermic reaction and for an exothermic reaction respectively, and each containing a removable fluid-permeable catalytic insert to catalyze the reaction. The flow channels have a straight portion extending from one end face of the reactor and a linking portion that communicates between the end of the straight portion and at least one side face of the reactor, wherein the straight portion and the linking portion are defined at least in part by fin structures. The fm structures of the linking portion may be perforated, so that there are perforations aligned with each straight portion, but at the end of the reactor each line of perforations is obstructed. Removal of the obstructions enables the catalytic inserts to be pushed out of the flow channels when they are spent.
摘要翻译：紧凑的催化反应器分别定义了交替排列的多个第一和第二流动通道，分别用于吸热反应和放热反应，每个含有可移除的流体可渗透催化剂插入物以催化反应。流动通道具有从反应器的一个端面延伸的直线部分和连通部分，其在直线部分的端部与反应器的至少一个侧面之间连通，其中直线部分和连接部分至少限定部分由鳍结构。连接部分的fm结构可以是穿孔的，使得具有与每个直线部分对准的穿孔，但是在反应器的端部，每一排穿孔被阻塞。消除障碍物使催化插入物在消耗时被推出流道。

36. 发明申请

US20100186824A1 Gas-to-Liquid Plant Using Parallel Units 审中-公开
标题翻译：使用并联单元的气体到液体的工厂
公开(公告)号：US20100186824A1
公开(公告)日：2010-07-29
申请号：US12718633
申请日：2010-03-05
申请人： Michael Joseph Bowe , Clive Derek Lee-Tuffnell , Iain Kenneth Baxter , Christopher Hopper
发明人： Michael Joseph Bowe , Clive Derek Lee-Tuffnell , Iain Kenneth Baxter , Christopher Hopper
IPC分类号： F17D3/00 , B01J7/00
CPC分类号： B01J8/22 , B01J8/02 , B01J8/04 , B01J19/0093 , B01J2219/0002 , B01J2219/00038 , B01J2219/0004 , B01J2219/00835 , C10G2/32 , C10G2300/1025 , Y10T137/0324
摘要： A plant is provided for processing natural gas. The plant comprises two or more modules connected in parallel. The plant is configured to convert the associated gas into a material with a higher density. In addition, a method of processing gas associated with one or more oil wells. The method comprises the steps of: providing a modular plant comprising two or more modules in parallel wherein at least one of the modules is a robust module and at least one of the modules is an economical module; turning down one or more of the modules when productivity drops; switching off one or more of the modules at least when productivity drops beyond the turndown limit. The natural gas is treated in a Fischer-Tropsch unit.
摘要翻译：提供一种处理天然气的工厂。该设备包括并联连接的两个或多个模块。工厂被配置为将相关联的气体转换成具有较高密度的材料。另外，处理与一个或多个油井相关联的气体的方法。该方法包括以下步骤：提供包括并联的两个或多个模块的模块化设备，其中模块中的至少一个是鲁棒模块，并且至少一个模块是经济模块; 当生产率下降时，降低一个或多个模块; 至少当生产率下降到超出调低限制时，关闭一个或多个模块。天然气以费托为单位进行处理。

37. 发明授权

US07749466B2 Catalytic reactor 失效
标题翻译：催化反应器
公开(公告)号：US07749466B2
公开(公告)日：2010-07-06
申请号：US11813867
申请日：2006-01-11
申请人： John Vitucci , Michael Joseph Bowe , Lawrence Andrew Stryker , Douglas Eugene Decker , Vinh N. Le
发明人： John Vitucci , Michael Joseph Bowe , Lawrence Andrew Stryker , Douglas Eugene Decker , Vinh N. Le
IPC分类号： B01J8/02 , B01J8/04 , B01J10/00 , B01J19/00 , B01J35/02 , B01J12/00
CPC分类号： C01B3/384 , B01J19/249 , B01J2219/2453 , B01J2219/2458 , B01J2219/2459 , B01J2219/2464 , B01J2219/2465 , B01J2219/2467 , B01J2219/247 , B01J2219/2472 , B01J2219/2479 , B01J2219/2482 , B01J2219/2486 , B01J2219/2493 , B01J2219/2497 , B01J2219/2498 , C01B3/382 , C01B2203/0233 , C01B2203/062 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/1047 , C01B2203/107 , C01B2203/142 , C01B2203/84 , C10G2/34 , C10G2/341 , Y02P20/128 , Y02P20/52
摘要： A compact catalytic reactor for Fischer-Tropsch synthesis (50) comprises a reactor module (70) defining a multiplicity of first and second flow channels arranged alternately, for carrying a gas mixture, and a coolant respectively. A removable gas-permeable catalyst structure (82) with a substrate for example of metal foil is provided in each flow channel in which the synthesis reaction is to occur. The reactor module (70) is enclosed within a pressure vessel (90), the pressure within the pressure vessel being arranged to be at a pressure substantially that of the high pressure reacting gas mixture. Consequently all the flow channels within the module are either at the pressure of their surroundings, or are under compression; no parts are under tension. This simplifies the design of the module, and increases the proportion of reactor volume which can be occupied by the catalyst.
摘要翻译：用于费 - 托合成的紧凑型催化反应器（50）包括反应器模块（70），其分别交替排列多个第一和第二流动通道，用于承载气体混合物和冷却剂。在其中要进行合成反应的每个流动通道中提供具有例如金属箔的基底的可移除气体可渗透的催化剂结构（82）。反应器模块（70）被封闭在压力容器（90）内，压力容器内的压力被设置成基本上是高压反应气体混合物的压力。因此，模块内的所有流动通道处于其周围的压力下，或处于压缩状态; 没有零件处于紧张状态。这简化了模块的设计，并增加了催化剂可以占据的反应器体积的比例。

38. 发明申请

US20080166276A1 Catalytic Reactor 审中-公开
标题翻译：催化反应器
公开(公告)号：US20080166276A1
公开(公告)日：2008-07-10
申请号：US11816545
申请日：2006-01-18
申请人： Michael Joseph Bowe
发明人： Michael Joseph Bowe
IPC分类号： B01J19/00
CPC分类号： B01J19/249 , B01J2219/2453 , B01J2219/2458 , B01J2219/2459 , B01J2219/2462 , B01J2219/2465 , B01J2219/247 , B01J2219/2472 , B01J2219/2479 , B01J2219/2482 , B01J2219/2485 , B01J2219/2495 , B01J2219/2496 , B01J2219/2498
摘要： A compact catalytic reactor (10) for performing a chemical reaction between reactants defines a multiplicity of first and second flow channels (16, 17) arranged alternately, the first flow channels providing flow paths for reactants and the second flow channels providing a source of heat for the reaction. Each flow channel in which a chemical reaction is to take place contains a removable fluid-permeable catalyst structure (20). The walls defining the first flow channels (16), and preferably those of the second flow channels (17) too, are treated so as to have surfaces with a high emissivity. This reactor is particularly suited to reactions carried out at a temperature above about 500° C., at which temperature radiative heat transfer becomes significant.
摘要翻译：用于在反应物之间进行化学反应的紧凑型催化反应器（10）限定交替布置的多个第一和第二流动通道（16,17），所述第一流动通道为反应物提供流动路径，并且第二流动通道提供热源为了反应。要发生化学反应的每个流动通道都含有可移除的流体可渗透的催化剂结构（20）。限定第一流动通道（16）并且优选地也是第二流动通道（17）的壁被处理以具有高发射率的表面。该反应器特别适用于在高于约500℃的温度下进行的反应，在该温度下辐射热传递变得显着。

39. 发明申请

US20080148635A1 Catalytic Reactors 失效
标题翻译：催化反应器
公开(公告)号：US20080148635A1
公开(公告)日：2008-06-26
申请号：US11817152
申请日：2006-02-15
申请人： Michael Joseph Bowe
发明人： Michael Joseph Bowe
IPC分类号： C10L3/08 , B01J19/00
CPC分类号： C10G2/341 , B01J19/249 , B01J2219/2453 , B01J2219/2459 , B01J2219/2462 , B01J2219/2465 , B01J2219/2472 , B01J2219/2479 , B01J2219/2498 , C10G2300/1025
摘要： A compact catalytic reactor defines a multiplicity of first and second flow channels arranged alternately in the reactor, for carrying first and second fluids, respectively, wherein at least the first fluids undergo a chemical reaction. Each first flow channel containing a removable gas-permeable catalyst structure (20) incorporating a metal substrate, the catalyst structure defining flow paths therethrough, with catalytic material on at least some surfaces of each such path. The catalyst structure also incorporates a multiplicity of projecting resilient lugs (22) which support the catalyst structure (20) spaced away from at least one adjacent wall of the channel (17).
摘要翻译：紧凑型催化反应器限定在反应器中交替布置的多个第一和第二流动通道，用于分别承载第一和第二流体，其中至少第一流体经历化学反应。每个第一流动通道包含结合有金属基底的可移除气体可渗透催化剂结构（20），所述催化剂结构在每个所述路径的至少某些表面上具有催化材料，所述催化剂结构限定了穿过其中的流动路径催化剂结构还包括多个突出的弹性突起（22），其支撑与通道（17）的至少一个相邻壁间隔开的催化剂结构（20）。

40. 发明申请

US20070258872A1 CATALYTIC REACTOR 有权
标题翻译：催化反应器
公开(公告)号：US20070258872A1
公开(公告)日：2007-11-08
申请号：US11740897
申请日：2007-04-26
申请人： David James West , Michael Joseph Bowe , Robert Frew Gillespie , Steven Brabon , Robert Peat
发明人： David James West , Michael Joseph Bowe , Robert Frew Gillespie , Steven Brabon , Robert Peat
IPC分类号： B01J8/02
CPC分类号： B01J19/249 , B01J2219/00265 , B01J2219/2453 , B01J2219/2458 , B01J2219/2459 , B01J2219/246 , B01J2219/2462 , B01J2219/2464 , B01J2219/2465 , B01J2219/247 , B01J2219/2472 , B01J2219/2474 , B01J2219/2479 , B01J2219/2482 , B01J2219/2486 , B01J2219/2487 , B01J2219/2497 , B01J2219/2498 , C01B3/384 , C01B2203/0233 , C01B2203/0822 , C01B2203/0827 , C01B2203/1005 , Y02P20/128 , Y02P20/52
摘要： A compact catalytic reactor defines a multiplicity of first and second flow channels arranged alternately, the first flow channels being no more than 10 mm deep and providing flow paths for combustible reactants, and containing a catalyst structure (20) to catalyse combustion of the reactants, and having at least one inlet for at least one of the reactants. The first flow channel also includes an insert (40 or 60) adjacent to each inlet, this insert not being catalytic to the combustion reaction; the insert may define gaps which are narrower than the maximum gap size for preventing flame propagation.
摘要翻译：紧凑型催化反应器限定交替布置的多个第一和第二流动通道，第一流动通道不超过10mm深，并为可燃性反应物提供流动路径，并且包含催化剂结构（20）以催化反应物的燃烧，并且具有用于至少一种反应物的至少一个入口。第一流动通道还包括与每个入口相邻的插入件（40或60），该插入件不会催化燃烧反应; 插入件可以限定比用于防止火焰传播的最大间隙尺寸更窄的间隙。

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