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公开(公告)号：US09381486B2
公开(公告)日：2016-07-05
申请号：US14131927
申请日：2012-07-13
申请人： James Banister
发明人： James Banister
IPC分类号： B01J16/00 , B01J21/00 , B01J21/04 , B01J23/70 , B01J23/89 , B01J35/00 , B01J35/02 , B01J35/04 , B01J37/00 , B01J37/02 , B01J12/00 , C10G2/00 , B01J19/24
CPC分类号： B01J16/005 , B01J12/007 , B01J19/2485 , B01J19/249 , B01J21/04 , B01J23/8913 , B01J35/0066 , B01J35/023 , B01J35/04 , B01J37/0219 , B01J37/0221 , B01J37/0248 , B01J2219/2404 , B01J2219/2406 , B01J2219/2407 , B01J2219/2411 , B01J2219/2424 , B01J2219/2428 , B01J2219/2438 , B01J2219/2445 , B01J2219/2448 , C10G2/332 , C10G2/341
摘要： There is herein described a Fischer-Tropsch reactor. More particularly, there is described a Fischer-Tropsch reactor that incorporates forced flow through a small pore, thick layer, monolith supported catalyst and high levels of heat transfer that is able to operate with high levels of catalyst effectiveness. The catalyst bed (103) is supported on a distinct porous structure (101) through which the syn-gas flow is forced and the catalyst layer has a thickness of more than 200 microns.
摘要翻译： 在此描述了费 - 托反应器。 更具体地，描述了一种费 - 托反应器，其包含强制流过小孔，厚层，整体式负载的催化剂和能够以高水平的催化剂有效性操作的高水平的热传递。 催化剂床（103）被支撑在不同的多孔结构（101）上，通过该不同的多孔结构（101），合成气流被强制并且催化剂层的厚度大于200微米。
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公开(公告)号：US09187699B2
公开(公告)日：2015-11-17
申请号：US13623541
申请日：2012-09-20
CPC分类号： C10G47/22 , B01J19/24 , B01J19/2485 , B01J2219/00164 , B01J2219/24 , B01J2219/2412 , B01J2219/2419 , B01J2219/2445 , B01J2219/2446 , C10G1/065 , C10G9/00
摘要： Disclosed is a pyrolysis process that is capable of being with reduced coke and/or tar formation. The process can pyrolyze hydrocarbon feed that contains low- to mid-range levels of non-volatiles. Pyrolysis is carried out with a predetermined amount of the feed being in the liquid phase so as to minimize coke and/or tar formation in the pyrolysis reactor. The pyrolysis feed may also include a diluent, such as molecular hydrogen, that further acts to minimize coke and/or tar formation in the pyrolysis reactor. The amount of diluent in the pyrolysis feed can be adjusted to adjust or control dry point of the hydrocarbon in the pyrolysis feed.
摘要翻译： 公开了能够减少焦炭和/或焦油形成的热解方法。 该方法可以热解含有低至中等程度的非挥发物的烃类进料。 以预定量的进料处于液相进行热解，以便最小化热解反应器中的焦炭和/或焦油形成。 热解原料还可以包括稀释剂，例如分子氢，其还用于使热解反应器中的焦炭和/或焦油形成最小化。 可以调节热解原料中的稀释剂的量以调节或控制热解原料中烃的干点。
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公开(公告)号：US08980186B2
公开(公告)日：2015-03-17
申请号：US13201919
申请日：2010-02-26
CPC分类号： B01J19/2485 , B01J35/04 , B01J2219/00117 , B01J2219/2445 , C04B38/0009 , F01N2330/30
摘要： A honeycomb body is disclosed having cells extending along a common direction, a first plurality of the cells being open at both ends of the body and a second plurality of the cells being closed at one or both ends of the body, the second plurality of cells arranged in one or more groups of cells cooperating to define one or more fluid passages extending through the body at least in part perpendicularly to the common direction, wherein, in a plane perpendicular to the common direction, the ratio of the area of cells of the first plurality to the area of cells of the second plurality varies along the length of at least one of the one or more fluid passages.
摘要翻译： 公开了一种蜂窝体，其具有沿公共方向延伸的单元，第一多个单元在主体的两端开口，第二多个单元在主体的一端或两端封闭，第二多个单元 配置在一组或多组细胞中，所述一组或多组细胞协调以限定一个或多个流体通道，所述流体通道至少部分垂直于共同方向延伸穿过所述主体，其中在与所述共同方向垂直的平面中，所述细胞的面积比 首先多个到第二个单元的单元区域沿一个或多个流体通道中的至少一个的长度变化。
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公开(公告)号：US20140147345A1
公开(公告)日：2014-05-29
申请号：US14131927
申请日：2012-07-13
申请人： James Banister
发明人： James Banister
IPC分类号： B01J16/00
CPC分类号： B01J16/005 , B01J12/007 , B01J19/2485 , B01J19/249 , B01J21/04 , B01J23/8913 , B01J35/0066 , B01J35/023 , B01J35/04 , B01J37/0219 , B01J37/0221 , B01J37/0248 , B01J2219/2404 , B01J2219/2406 , B01J2219/2407 , B01J2219/2411 , B01J2219/2424 , B01J2219/2428 , B01J2219/2438 , B01J2219/2445 , B01J2219/2448 , C10G2/332 , C10G2/341
摘要： There is herein described a Fischer-Tropsch reactor. More particularly, there is described a Fischer-Tropsch reactor that incorporates forced flow through a small pore, thick layer, monolith supported catalyst and high levels of heat transfer that is able to operate with high levels of catalyst effectiveness. The catalyst bed (103) is supported on a distinct porous structure (101) through which the syn-gas flow is forced and the catalyst layer has a thickness of more than 200 microns.
摘要翻译： 在此描述了费 - 托反应器。 更具体地，描述了一种费 - 托反应器，其包含强制流过小孔，厚层，整体式负载的催化剂和能够以高水平的催化剂有效性操作的高水平的热传递。 催化剂床（103）被支撑在不同的多孔结构（101）上，通过该不同的多孔结构（101），合成气流被强制并且催化剂层的厚度大于200微米。
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公开(公告)号：US20120315200A1
公开(公告)日：2012-12-13
申请号：US13593564
申请日：2012-08-24
CPC分类号： B01J8/02 , B01J19/2485 , B01J19/32 , B01J2219/2404 , B01J2219/2408 , B01J2219/2422 , B01J2219/2424 , B01J2219/2428 , B01J2219/2443 , B01J2219/2445 , B01J2219/2448 , B05D1/38 , F01N3/0222 , F01N3/28 , F01N2330/34 , F01N2330/38 , F01N2330/40 , Y02T10/20 , Y10T156/10
摘要： Systems and methods for fabricating bodies (e.g., porous bodies) are described. Various aspects provide for reactors and the fabrication of reactors. Some reactors include surfaces that provide for heterogeneous reactions involving a fluid (and/or components thereof). A fluid may be a gas and/or a liquid. A contaminant in the fluid (e.g., a dissolved or suspended substance) may react in a reaction. A contaminant may be filtered from a fluid. Some reactors provide for independent control of heat transfer (between the fluid, the reactor, and the environment) with respect to mass transfer (e.g., fluid flow through the reactor).
摘要翻译： 描述了用于制造体（例如，多孔体）的系统和方法。 各个方面提供反应堆和反应堆的制造。 一些反应器包括提供涉及流体（和/或其组分）的非均相反应的表面。 流体可以是气体和/或液体。 流体中的污染物（例如溶解或悬浮物质）可能在反应中发生反应。 污染物可以从流体中过滤。 一些反应器提供相对于传质（例如通过反应器的流体流）的热传递（在流体，反应器和环境之间）的独立控制。
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6.发明授权Metallic monolith catalyst support for selective gas phase reactions in tubular fixed bed reactors 有权用于管式固定床反应器中选择性气相反应的金属整料催化剂载体公开(公告)号：US07678343B2
公开(公告)日：2010-03-16
申请号：US09746219
申请日：2000-12-22
CPC分类号： B01J35/04 , B01J19/2485 , B01J37/0225 , B01J2219/2404 , B01J2219/2407 , B01J2219/2408 , B01J2219/2428 , B01J2219/2434 , B01J2219/2445 , B01J2219/2446
摘要： There is disclosed a catalyst support for selective gas phase reactions in a tubular fixed bed reactor comprising a metallic monolith having channels the walls of which are adapted to receive a catalytically active phase or an intermediate layer acting as a carrier for a catalytically active phase. The monoliths are coated with catalytically active material and loaded lengthwise into tubular reactors, the channels being parallel to the length of the reactors. The catalysts are particularly useful in the chlorination/oxychlorination of alkenes and alkanes, and the oxidation of alkenes. Compared with the use of conventional catalysts in pellet form or in the form of ceramic monoliths the catalysts of the invention offer greater yields and selectivity, the avoidance of hot spots, greater catalyst life and flexibility in use.
摘要翻译： 公开了一种用于管式固定床反应器中的选择性气相反应的催化剂载体，其包括具有通道的金属整料，其通道适于接收催化活性相或作为催化活性相载体的中间层。 整料用催化活性材料涂覆并纵向加载到管式反应器中，通道平行于反应器的长度。 催化剂特别适用于烯烃和烷烃的氯化/氧氯化和烯烃的氧化。 与使用颗粒形式的常规催化剂或以陶瓷整料的形式相比，本发明的催化剂提供更高的产率和选择性，避免热点，更大的催化剂寿命和使用的灵活性。
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公开(公告)号：US20030100448A1
公开(公告)日：2003-05-29
申请号：US09924676
申请日：2001-08-08
IPC分类号： B01J023/72 , B22F001/00
CPC分类号： B22F3/227 , B01J19/2485 , B01J35/04 , B01J2219/2435 , B01J2219/2437 , B01J2219/2445 , B01J2219/2446 , B22F3/1115 , B22F2998/00 , C01B3/16 , C01B2203/0283 , C01B2203/1023 , C01B2203/1076 , Y02P20/52
摘要： Monolithic metallic catalyst substrates offering improved heat conductivity are provided from metal powder extrusion batches of copper, tin, zinc, aluminum, iron, silver, nickel, and mixtures and alloys thereof by extrusion through a honeycomb extrusion die followed by drying and firing in a two stage firing process to oxidize organic extrusion batch components, remove residual oxides from the porous wall structure, and consolidate the metal powders to strong, integral honeycomb support structures.
摘要翻译： 提供改善的导热性的单片金属催化剂基材由铜，锡，锌，铝，铁，银，镍的金属粉末挤出批次及其混合物和合金通过蜂窝挤出模头挤出，然后在二 氧化有机挤出批料成分，从多孔壁结构中除去残余氧化物，并将金属粉末固结成坚固的整体蜂窝状支撑结构。
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公开(公告)号：US10011776B2
公开(公告)日：2018-07-03
申请号：US14758288
申请日：2013-12-27
申请人： ENI S.P.A.
发明人： Marco Paturzo , Mauro Favaretto , Marzio Piazza , Pio Forzatti , Gianpiero Groppi , Luca Lietti , Enrico Tronconi , Carlo Giorgio Visconti
CPC分类号： C10G2/341 , B01J19/2485 , B01J2219/2404 , B01J2219/2407 , B01J2219/2411 , B01J2219/243 , B01J2219/2434 , B01J2219/2443 , B01J2219/2445 , B01J2219/2446 , C10G2/332 , Y10T29/49828
摘要： A multi-structured tubular element for producing a reactor for effecting exothermic/endothermic chemical reactions, comprises two or more monolithic thermoconductive bodies, assembled together so that each has a part of the side surface interfaced with the side surface of one or more monolithic thermoconductive bodies adjacent thereto, so as to form as a whole, a honeycomb structure containing a plurality of longitudinal channels extending from one end to the other of said tubular element, suitable for being filled with a granular catalytic solid.
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公开(公告)号：US20170306243A1
公开(公告)日：2017-10-26
申请号：US15526364
申请日：2015-11-06
CPC分类号： C10G2/341 , B01J8/0453 , B01J8/067 , B01J19/2485 , B01J2208/00061 , B01J2208/00132 , B01J2208/00168 , B01J2208/00194 , B01J2208/00849 , B01J2208/00938 , B01J2208/065 , B01J2219/2406 , B01J2219/2407 , B01J2219/2408 , B01J2219/2411 , B01J2219/2412 , B01J2219/2422 , B01J2219/243 , B01J2219/2445 , B01J2219/2448
摘要： A reactor for producing desired reaction products has a housing, a plurality of catalyst conduits within the housing, and a plurality of coolant conduits within the housing. The coolant conduits are interspersed among the catalyst conduits, and each catalyst conduit is positioned adjacent to at least two coolant conduits.
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公开(公告)号：US09511345B1
公开(公告)日：2016-12-06
申请号：US14220146
申请日：2014-03-20
申请人： Errcive, Inc.
CPC分类号： B01J8/02 , B01J19/2485 , B01J19/32 , B01J2219/2404 , B01J2219/2408 , B01J2219/2422 , B01J2219/2424 , B01J2219/2428 , B01J2219/2443 , B01J2219/2445 , B01J2219/2448 , B05D1/38 , F01N3/0222 , F01N3/28 , F01N2330/34 , F01N2330/38 , F01N2330/40 , Y02T10/20 , Y10T156/10
摘要： Systems and methods for fabricating bodies (e.g., porous bodies) are described. Various aspects provide for reactors and the fabrication of reactors. Some reactors include surfaces that provide for heterogeneous reactions involving a fluid (and/or components thereof). A fluid may be a gas and/or a liquid. A contaminant in the fluid (e.g., a dissolved or suspended substance) may react in a reaction. A contaminant may be filtered from a fluid. Some reactors provide for independent control of heat transfer (between the fluid, the reactor, and the environment) with respect to mass transfer (e.g., fluid flow through the reactor).
摘要翻译： 描述了用于制造体（例如，多孔体）的系统和方法。 各个方面提供反应堆和反应堆的制造。 一些反应器包括提供涉及流体（和/或其组分）的非均相反应的表面。 流体可以是气体和/或液体。 流体中的污染物（例如溶解或悬浮物质）可能在反应中发生反应。 污染物可以从流体中过滤。 一些反应器提供相对于传质（例如通过反应器的流体流）的热传递（在流体，反应器和环境之间）的独立控制。
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