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公开(公告)号：US10035120B2
公开(公告)日：2018-07-31
申请号：US15521357
申请日：2015-10-29
Applicant: SABIC Global Technologies B.V.
Inventor： Zeeshan Nawaz , Shahzada Khuram , Khalid Karim
CPC classification number: B01J8/065 , B01J8/0045 , B01J8/0214 , B01J8/025 , B01J8/0285 , B01J8/0496 , B01J8/067 , B01J2208/0015 , B01J2208/00159 , B01J2208/00212 , B01J2208/00761 , B01J2208/00876 , B01J2208/00946 , B01J2208/022 , B01J2208/065 , B01J2219/2455 , B01J2219/2481 , C07C1/041 , C10G2/34 , C10G2/341 , C10G2400/20 , C10G2400/22
Abstract: A reactor for hydrocarbon production that separates wax reaction products from lightweight gaseous reaction products. The reactor has a housing, a catalyst bed, a product recovery zone, and a stripping zone. The catalyst bed can be provided in multi-tubular and other fixed bed configurations. The stripping zone receives light-weight gas reaction products from the product recovery zone, while a gas outlet of the housing receives non-lightweight gaseous hydrocarbon reaction products from the product recovery zone. A wax outlet of the housing receives wax products from the product recovery zone.
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公开(公告)号：US09409138B2
公开(公告)日：2016-08-09
申请号：US14130369
申请日：2012-06-29
Applicant: Freimut Marold
Inventor： Freimut Marold
IPC: B01J8/00 , B01J8/02 , B01J8/04 , B01J19/00 , B01J19/24 , B01J19/30 , B01J19/32 , B01J35/00 , B01J35/02
CPC classification number: B01J8/0496 , B01J19/249 , B01J2208/022 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/2472 , B01J2219/2479 , B01J2219/2481 , B01J2219/2482 , B01J2219/2485 , B01J2219/2495
Abstract: A reactor has a container through which a reactive medium is passed and a plurality of plates in the container defining a plurality of between-plate reaction spaces through which the reactive medium travels. The plates are self-supporting and fixed in the container. Respective self-contained packings each formed by a support independent of the container are each of a flat shape that completely or almost completely fills the between-plate space and are each fittable to a variable depth in and removable from a respective one of the spaces. The supports each hold a catalyst for the reactive medium and are also removable from and insertable with the respective catalyst into the respective spaces such that when the catalyst is exhausted the packings can be replaced with fresh packings.
Abstract translation: 反应器具有通过反应介质通过的容器，并且容器中的多个板限定反应介质穿过的多个板间反应空间。 板是自支撑并固定在容器中。 由独立于容器的支撑件形成的各自独立的填料各自是平坦的形状，其完全或几乎完全填充板间空间，并且每个填充物可适应于相应的一个空间中的可移除的深度。 所述载体各自保持用于反应介质的催化剂，并且也可以从各自的催化剂中除去和插入到相应的空间中，使得当催化剂被排出时，填料可用新鲜的填料代替。
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公开(公告)号：US08202917B2
公开(公告)日：2012-06-19
申请号：US12462083
申请日：2009-07-29
Applicant: Rafael Espinoza
Inventor： Rafael Espinoza
CPC classification number: B01J8/0221 , B01J19/249 , B01J2208/0015 , B01J2208/00814 , B01J2208/022 , B01J2219/00038 , B01J2219/182 , B01J2219/1943 , B01J2219/2459 , B01J2219/2462 , B01J2219/2481 , B01J2219/2485 , C10G2/341 , C10G49/002
Abstract: A novel catalytic reactor suitable for use in chemical and petrochemical processes. The reactor is of a pillow panel that has superior heat transfer properties. This invention also relates to a chemical process, such as a Fischer-Tropsch synthesis process performed with use of the novel pillow panel reactor.
Abstract translation: 适用于化学和石化工艺的新型催化反应器。 反应器是具有优异的传热性能的枕头面板。 本发明还涉及一种化学方法，例如使用新型枕板反应器进行的费 - 托合成方法。
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公开(公告)号：US20100189609A1
公开(公告)日：2010-07-29
申请号：US12669412
申请日：2008-06-30
Applicant: Agostino Barbieri , Nicola Sorlini
Inventor： Agostino Barbieri , Nicola Sorlini
CPC classification number: B01J8/0285 , B01J8/025 , B01J19/249 , B01J2208/0015 , B01J2208/022 , B01J2219/00085 , B01J2219/2455 , B01J2219/246 , B01J2219/2462 , B01J2219/2481 , B01J2219/2485 , B01J2219/2493 , B01J2219/2496 , F28D9/0031 , F28F13/06
Abstract: Plate heat exchange unit (12) for isothermal or pseudo-isothermal chemical reactors, for the heat exchange between a fluid circulating inside the plates and an outer flow of reactant gases, wherein the walls (14, 15), of the plates (13) have notches (14s, 15s) surrounded by suitable joining lines (105), obtaining openings (104) passing through the plates (13) themselves, the plates resulting substantially permeable in the transversal direction to the reactant gases.
Abstract translation: 用于等温或假等温化学反应器的板式热交换单元（12），用于在板内循环的流体与反应气体的外部流之间的热交换，其中板（13）的壁（14,15） 具有由合适的接合线（105）包围的凹口（14s，15s），获得穿过板（13）本身的开口（104），所述板在反应气体的横向上基本上可渗透。
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公开(公告)号：US20090220394A1
公开(公告)日：2009-09-03
申请号：US12090325
申请日：2006-10-17
Applicant: Richard Root Woods , Brook Forest Porter , Kandaswamy Duraiswamy , Leonard Weschta , Christian Hulteberg
Inventor： Richard Root Woods , Brook Forest Porter , Kandaswamy Duraiswamy , Leonard Weschta , Christian Hulteberg
CPC classification number: C01B3/384 , B01J8/0407 , B01J8/0419 , B01J8/0438 , B01J8/0442 , B01J19/249 , B01J2208/00309 , B01J2208/00504 , B01J2208/0053 , B01J2208/022 , B01J2219/1943 , B01J2219/2453 , B01J2219/2458 , B01J2219/246 , B01J2219/2462 , B01J2219/2464 , B01J2219/2465 , B01J2219/247 , B01J2219/2479 , B01J2219/2481 , B01J2219/2482 , B01J2219/2491 , B01J2219/2493 , B01J2219/2495 , B01J2219/2496 , B01J2219/2498 , C01B3/0005 , C01B3/382 , C01B3/48 , C01B2203/0233 , C01B2203/0283 , C01B2203/04 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/1288 , C01B2203/142 , C01B2203/143 , Y02E60/324 , Y02P20/128
Abstract: A hydrogen generation system is disclosed that includes an integrated steam reforming reactor. The reactor has an overall cylindrical shape, receives a reformate and separately receiving a combustion gas mixture. The reactor includes a plurality of reforming stages arranged in a stacked series of disc shaped stage configuration, wherein each reforming stage has a disc shaped combustion portion adjacent a disc shaped catalyst pack through which the reformate passes, wherein the reformate is directed axially between stages and radially within each stage; and the combustion mixture is directed radially between groups of stages and circumferentially within each stage.
Abstract translation: 公开了一种氢气生成系统，其包括集成的蒸汽重整反应器。 反应器具有总体圆柱形形状，接收重整产物并分别接收燃烧气体混合物。 反应器包括多个重整级，其布置成堆叠的一系列盘形级结构，其中每个重整级具有邻近重整产品通过的盘形催化剂组件的盘形燃烧部分，其中重整产品在轴向上定向在阶段和 在每个阶段的径向; 并且燃烧混合物在每个阶段内径向地指向阶段组和周向。
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Patent Agency Ranking
公开(公告)号：US07497998B2
公开(公告)日：2009-03-03
申请号：US11515776
申请日：2006-09-06
Applicant: Enrique Tabak
Inventor： Enrique Tabak
CPC classification number: C01B17/803 , B01J8/0242 , B01J19/248 , B01J19/249 , B01J2208/00194 , B01J2208/00814 , B01J2208/00884 , B01J2208/021 , B01J2208/022 , B01J2219/2453 , B01J2219/2456 , B01J2219/2459 , B01J2219/246 , B01J2219/2481
Abstract: A converter having an exterior shell with a central axis, at least one gas inlet and at least one gas outlet. The exterior shell includes a base and an interior support structure. A number of vertically stacked catalytic chambers within the exterior shell are each in communication with one or more gas inlets and gas outlets. Each chamber is defined by an inner wall of the external shell, a permeable catalytic bed support platform, a lower division plate spaced below the platform defining a gas retention plenum and an upper division plate above the platform. At least one of: the platform; the upper division plate; and the lower division plate have a toroid surface symmetric about the central axis with an outer periphery supported by the inner wall of the exterior shell and an inner periphery supported by the interior support structure.
Abstract translation: A转换器具有具有中心轴线的外壳，至少一个气体入口和至少一个气体出口。 外壳包括底座和内部支撑结构。 外壳内的多个垂直堆叠的催化室各自与一个或多个气体入口和气体出口连通。 每个室由外壳的内壁，可渗透的催化床支撑平台，在平台下方限定气体保持气室的下分隔板和在平台上方的上分隔板限定。 至少有一个：平台; 上部分板; 并且下分隔板具有围绕中心轴线对称的环形表面，外围由外壳的内壁支撑，内周由内部支撑结构支撑。
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公开(公告)号：US20080146683A1
公开(公告)日：2008-06-19
申请号：US11908923
申请日：2006-03-17
CPC classification number: B01J8/28 , B01J8/0055 , B01J8/065 , B01J8/067 , B01J8/1836 , B01J8/22 , B01J8/226 , B01J8/34 , B01J19/248 , B01J19/249 , B01J2208/00132 , B01J2208/0015 , B01J2208/0061 , B01J2208/0084 , B01J2208/022 , B01J2219/00015 , B01J2219/0002 , B01J2219/245 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/247 , B01J2219/2474 , B01J2219/2481 , B01J2219/2496 , B01J2219/2497 , C10G2/344 , C10G2300/1022 , F28D7/00 , F28D7/163 , F28D9/00 , F28F9/22 , Y02P20/582
Abstract: Method of operating a three-phase slurry reactor includes feeding at a low level at least one gaseous reactant into a vertically extending slurry body of solid particles suspended in a suspension liquid, the slurry body being contained in at least two vertically extending shafts housed within a common reactor shell, each shaft being divided into a plurality of vertically extending channels at least some of which are in slurry flow communication and the slurry body being present in at least some of the channels. The gaseous reactant is allowed to react as it passes upwardly through the slurry body present in at least some of the channels of the shafts, thereby to form a non-gaseous and/or a gaseous product. Gaseous product, if present, and/or unreacted gaseous reactant is allowed to disengage from the slurry body in a head space above the slurry body.
Abstract translation: 操作三相浆料反应器的方法包括将低至少一种气态反应物进料到悬浮在悬浮液中的固体颗粒的垂直延伸的淤浆体中，所述淤浆体包含在容纳在悬浮液悬浮液中的至少两个垂直延伸的轴内 共同的反应器壳体，每个轴被分成多个垂直延伸的通道，其中至少一些通道处于淤浆流动连通状态，并且淤浆体存在于至少一些通道中。 当气态反应物向上通过存在于轴的至少一些通道中的淤浆体时，使其反应，从而形成非气态和/或气态产物。 气体产物（如果存在）和/或未反应的气态反应物允许在浆料体上方的顶部空间中从浆料体脱离。
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公开(公告)号：US20080114083A1
公开(公告)日：2008-05-15
申请号：US11908916
申请日：2006-03-17
CPC classification number: C10G2/342 , B01J8/1836 , B01J8/22 , B01J8/226 , B01J19/249 , B01J2208/0015 , B01J2208/022 , B01J2219/00015 , B01J2219/0002 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/2474 , B01J2219/2481 , B01J2219/2496 , C10G2/32
Abstract: A method of operating a three-phase slurry reactor includes feeding at a low level at least one gaseous reactant into a vertically extending slurry body of solid particles suspended in a suspension liquid, the slurry body being contained in a plurality of vertically extending horizontally spaced slurry channels inside a common reactor shell, the slurry channels being defined between vertically extending horizontally spaced divider walls or plates and each slurry channel having a height, width and breadth such that the height and breadth are much larger than the width. The gaseous reactant is allowed to react as it passes upwardly through the slurry body present in the slurry channels, thereby to form non-gaseous and/or gaseous product. Gaseous product and/or unreacted gaseous reactant is allowed to disengage from the slurry body in a head space above the slurry body.
Abstract translation: 操作三相淤浆反应器的方法包括将低至少一种气态反应物进料到悬浮在悬浮液中的固体颗粒的垂直延伸的淤浆体中，浆料体包含在多个垂直延伸的水平间隔的浆料 通道在共同的反应器壳体内，浆液通道限定在垂直延伸的水平隔开的分隔壁或板之间，并且每个浆料通道具有高度，宽度和宽度，使得高度和宽度远大于宽度。 当气态反应物向上通过存在于浆料通道中的淤浆体时，使其反应，从而形成非气态和/或气态产物。 允许气体产物和/或未反应的气态反应物在淤浆体上方的顶部空间中与淤浆体脱离。
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9.发明授权Process and device for carrying out reactions in reactor with slot-shaped reaction spaces 失效在具有槽形反应空间的反应器中进行反应的方法和装置公开(公告)号：US07332139B2
公开(公告)日：2008-02-19
申请号：US09934085
申请日：2001-08-22
Applicant: Rüdiger Schütte , Torsten Balduf , Catrin Becker , Ina Hemme , Birgit Bertsch-Frank , Werner Wildner , Jürgen Rollmann , Georg Markowz
Inventor： Rüdiger Schütte , Torsten Balduf , Catrin Becker , Ina Hemme , Birgit Bertsch-Frank , Werner Wildner , Jürgen Rollmann , Georg Markowz
CPC classification number: F28F3/12 , B01F5/0403 , B01F13/0059 , B01F15/00935 , B01F2215/0036 , B01J19/0093 , B01J19/249 , B01J2208/022 , B01J2219/00265 , B01J2219/00835 , B01J2219/0086 , B01J2219/00889 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/2465 , B01J2219/2467 , B01J2219/2479 , B01J2219/2481 , B01J2219/2485 , B01J2219/2487 , B01J2219/2493 , B01J2219/2495 , B01J2219/2497 , B01J2219/2498 , C01B15/029 , C07C45/35 , C07C51/252 , C07D301/12 , F28D9/0081 , C07C47/22 , C07C57/04
Abstract: Reactions between at least two fluid reactants are performed in a reactor comprising wall elements (1), slot-shaped reaction spaces (3) and cavities (5) for conducting a fluid heat-carrier through. Depending on the process and throughput, a modular structural design is chosen wherein an arbitrary number of wall elements (1) are assembled to a right-parallelepipedal block (24), the reaction spaces (3) are formed between lateral surfaces (2) of right-parallelepipedal wall elements (1), the reactants are introduced into the reaction spaces (3) from edge regions of one side of the block (24) and are conducted through the reaction spaces (3) in parallel flows and the fluid heat-carrier is conducted through the tubular cavities (5) extending in the interior of the wall elements (1).
Abstract translation: 在包括壁元件（1），槽形反应空间（3）和空腔（5）的反应器中进行至少两种流体反应物之间的反应，用于使流体热载体通过。 根据工艺和生产量，选择模块化结构设计，其中任意数量的壁元件（1）组装到右平行六面体块（24），反作用空间（3）形成在 右平行六面体壁元件（1），将反应物从块体（24）的一侧的边缘区域引入反应空间（3）中，并通过平行流动的反应空间（3） 载体通过在壁元件（1）的内部延伸的管状空腔（5）进行。
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公开(公告)号：US07048897B1
公开(公告)日：2006-05-23
申请号：US09649528
申请日：2000-08-28
Applicant: Chowdary Ramesh Koripella , Christopher K. Dyer , Stephen P. Rogers , Dominic Francis Gervasio
Inventor： Chowdary Ramesh Koripella , Christopher K. Dyer , Stephen P. Rogers , Dominic Francis Gervasio
CPC classification number: H01M8/0631 , B01B1/005 , B01J19/2485 , B01J19/249 , B01J2208/00398 , B01J2208/00415 , B01J2208/022 , B01J2219/00117 , B01J2219/00128 , B01J2219/00135 , C01B3/323 , C01B3/38 , C01B3/382 , C01B3/384 , C01B3/386 , C01B3/583 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/044 , C01B2203/047 , C01B2203/066 , C01B2203/0811 , C01B2203/0844 , C01B2203/085 , C01B2203/0866 , C01B2203/1011 , C01B2203/1035 , C01B2203/1076 , C01B2203/1223 , C01B2203/1247 , C01B2203/1276 , C01B2203/1288 , C01B2203/142 , C01B2203/1619 , C01B2203/1633 , C01B2203/169 , C01B2203/82 , F28F3/02 , F28F13/00 , F28F21/04 , F28F2255/18
Abstract: A hydrogen generator including a three-dimensional multilayer ceramic carrier structure defining a fuel reformer. The reformer includes a vaporization zone and a reaction zone including a catalyst. The reformer is operational as either a steam reformer, a partial oxidation reformer or an autothermal reformer. The fuel reformer, or processor, further includes an inlet channel for liquid fuel and an outlet channel for hydrogen enriched gas. The fuel processor is formed utilizing multi-layer ceramic technology in which thin ceramic layers are assembled then sintered to provide miniature dimensions in which the encapsulated catalyst converts or reforms inlet fuel into a hydrogen enriched gas.
Abstract translation: 一种氢发生器，包括限定燃料重整器的三维多层陶瓷载体结构。 重整器包括蒸发区和包括催化剂的反应区。 重整器作为蒸汽重整器，部分氧化重整器或自热重整器可操作。 燃料重整器或处理器还包括用于液体燃料的入口通道和用于富氢气体的出口通道。 燃料处理器是利用多层陶瓷技术形成的，其中组装薄陶瓷层然后烧结以提供微型尺寸，其中封装的催化剂将入口燃料转化或改造成富氢气体。
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