利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

26 条记录 (耗时 0.07 秒)

    Methanol manufacture using pressure swing reforming
    1.
    发明申请
    Methanol manufacture using pressure swing reforming 有权
    使用压力挥发重整的甲醇制造

    公开(公告)号：US20050154068A1

    公开(公告)日：2005-07-14

    申请号：US11011984

    申请日：2004-12-14

    申请人： Frank Hershkowitz ,  James Lattner

    发明人： Frank Hershkowitz ,  James Lattner

    IPC分类号： C07C1/24 ,  C07C29/151 ,  C07C27/06

    CPC分类号： C07C29/1518 ,  Y02P30/42 ,  C07C31/04 ,  C07C31/08 ,  C07C31/10 ,  C07C31/02

    摘要： A process for producing methanol is described in which a hydrocarbon is steam reformed in a reforming zone, and during the reforming stage, of a cyclic steam reformer having a reforming stage and a regeneration stage, the steam reforming being conducted under conditions effective to produce a first effluent stream containing synthesis gas. Fuel and an oxygen-containing gas are combusted in the regeneration stage of the reformer so as to reheat the reforming zone to a temperature sufficient for the reforming stage and generate a flue gas. At least part of the first effluent stream is contacted with a methanol synthesis catalyst under conditions effective to convert synthesis gas to methanol and form a methanol-containing stream and a tail gas stream comprising unreacted carbon monoxide and hydrogen. At least part of the tail gas stream is recycled as fuel for the regeneration stage of the cyclic steam reformer.

    摘要翻译： 描述了一种生产甲醇的方法，其中烃在重整区中进行蒸汽重整，并且在重整阶段期间，在具有重整阶段和再生阶段的循环蒸汽重整器中，蒸汽重整在有效产生 含有合成气的第一流出物流。 燃料和含氧气体在重整器的再生阶段中燃烧，以便将重整区再加热到足以进行重整阶段的温度并产生烟道气。 在有效地将合成气转化成甲醇并形成含甲醇流和包含未反应的一氧化碳和氢气的尾气流的条件下，将至少部分第一流出物流与甲醇合成催化剂接触。 至少部分尾气流作为循环蒸汽重整器的再生阶段的燃料再循环。

    Methanol manufacture using pressure swing reforming
    3.
    发明申请
    Methanol manufacture using pressure swing reforming 有权
    使用压力挥发重整的甲醇制造

    公开(公告)号：US20050137269A1

    公开(公告)日：2005-06-23

    申请号：US10738782

    申请日：2003-12-17

    申请人： Frank Hershkowitz ,  James Lattner

    发明人： Frank Hershkowitz ,  James Lattner

    IPC分类号： C07C1/24 ,  C07C29/151 ,  C07C27/10

    CPC分类号： C07C29/1518 ,  Y02P30/42 ,  C07C31/04 ,  C07C31/08 ,  C07C31/10 ,  C07C31/02

    摘要： A process for producing methanol is described in which a hydrocarbon is steam reformed in a reforming zone, and during the reforming stage, of a cyclic steam reformer having a reforming stage and a regeneration stage, the steam reforming being conducted under conditions effective to produce a first effluent stream containing synthesis gas. A fuel and an oxygen-containing gas are combusted in the regeneration stage of the reformer so as to reheat the reforming zone to a temperature sufficient for the reforming stage and generate a flue gas. At least part of the first effluent stream is contacted with a methanol synthesis catalyst under conditions effective to convert synthesis gas to methanol and form a methanol-containing stream and a tail gas stream comprising unreacted carbon monoxide and hydrogen. Hydrogen is separated from at least one of the first effluent stream and the tail gas stream and at least part of the hydrogen is recycled as part of the fuel for the regeneration stage of the cyclic steam reformer.

    摘要翻译： 描述了一种生产甲醇的方法，其中烃在重整区中进行蒸汽重整，并且在重整阶段期间，在具有重整阶段和再生阶段的循环蒸汽重整器中，蒸汽重整在有效产生 含有合成气的第一流出物流。 燃料和含氧气体在重整器的再生阶段中燃烧，以便将重整区重新加热到足以用于重整阶段的温度并产生烟道气。 在有效地将合成气转化成甲醇并形成含甲醇流和包含未反应的一氧化碳和氢气的尾气流的条件下，将至少部分第一流出物流与甲醇合成催化剂接触。 氢气与第一流出物流和尾气流中的至少一个分离，并且至少部分氢气作为用于循环蒸汽重整器的再生阶段的燃料的一部分被再循环。

    Production of synthesis gas blends for conversion to methanol or fischer-tropsch liquids
    4.
    发明申请
    Production of synthesis gas blends for conversion to methanol or fischer-tropsch liquids 有权
    生产用于转化为甲醇或费 - 托液体的合成气共混物

    公开(公告)号：US20070004809A1

    公开(公告)日：2007-01-04

    申请号：US11211982

    申请日：2005-08-25

    申请人： James Lattner ,  Christopher Jenkins

    发明人： James Lattner ,  Christopher Jenkins

    IPC分类号： C01B3/26 ,  C07C27/00

    CPC分类号： C07C1/20 ,  C01B3/382 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0255 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/0811 ,  C01B2203/0844 ,  C01B2203/1047 ,  C01B2203/1241 ,  C01B2203/141 ,  C01B2203/142 ,  C01B2203/82 ,  C07C29/1518 ,  C10G2/32 ,  C12C11/02 ,  C07C11/02 ,  C07C31/04

    摘要： The present invention provides a process for producing synthesis gas blends which are especially suitable for conversion either into oxygenates such as methanol or into Fischer-Tropsch liquids. Such a process involves reforming of two separate gaseous hydrocarbon feedstreams (formed, for example, by dividing a natural gas feedstock) in a steam-reforming unit and an oxygen-blown reforming unit, respectively. The syngas effluent from each reforming unit is then combined, after appropriate pressure adjustments, to realize a synthesis gas blend containing selected amounts and ratios of H2, CO and CO2. In further invention embodiments, processes are provided for converting the resulting syngas blends into oxygenates or Fischer-Tropsch hydrocarbons. Further conversion of the oxygenates so produced into light olefins also constitutes part of this invention.

    摘要翻译： 本发明提供了一种生产合成气共混物的方法，其特别适用于转化为含氧化合物如甲醇或费 - 托液体。 这种方法包括分别在蒸汽重整单元和氧气重整单元中重新分离两个单独的气态烃进料流（例如通过分配天然气原料形成）。 然后，在适当的压力调节之后，将来自每个重整单元的合成气流出物合并，以实现含有选定量的H 2 CO 2和CO 2 CO 2的比例的合成气共混物。 在进一步的发明实施方案中，提供了将所得合成气共混物转化为含氧化合物或费 - 托烃的方法。 将如此生产的含氧化合物进一步转化成轻质烯烃也构成本发明的一部分。

    Method and system for regenerating catalyst from a plurality of hydrocarbon conversion apparatuses
    5.
    发明申请
    Method and system for regenerating catalyst from a plurality of hydrocarbon conversion apparatuses 有权
    从多个烃转化装置再生催化剂的方法和系统

    公开(公告)号：US20070197846A1

    公开(公告)日：2007-08-23

    申请号：US11787857

    申请日：2007-04-18

    申请人： James Beech ,  Michael Nicoletti ,  James Lattner ,  Dennis Alexion ,  Peter Paik

    发明人： James Beech ,  Michael Nicoletti ,  James Lattner ,  Dennis Alexion ,  Peter Paik

    IPC分类号： C07C1/00

    CPC分类号： B01J8/26 ,  B01J8/0055 ,  B01J8/388 ,  B01J29/90 ,  B01J38/06 ,  C10G3/45 ,  C10G3/49 ,  C10G3/62 ,  C10G11/182 ,  C10G2300/4093 ,  C10G2400/20 ,  Y02P30/20

    摘要： The present invention is directed to a method and system for integrating a catalyst regeneration system with a plurality of hydrocarbon conversion apparatuses, preferably, a plurality of multiple riser reactor units. One embodiment of the present invention is a reactor system including a plurality of reactor units, at least one reactor unit preferably comprising a plurality of riser reactors. The system also includes a regenerator for converting an at least partially deactivated catalyst to a regenerated catalyst. A first conduit system transfers the at least partially deactivated catalyst from the reactor units to the regenerator, and a second conduit system transfers regenerating catalysts from the regenerator to the plurality of reactor units. Optionally, catalysts from a plurality of hydrocarbon conversion apparatuses may be directed to a single stripping unit and/or a single regeneration unit.

    摘要翻译： 本发明涉及用于将催化剂再生系统与多个烃转化装置（优选多个提升管反应器单元）整合的方法和系统。 本发明的一个实施方案是包括多个反应器单元的反应器系统，至少一个反应器单元优选包括多个提升管反应器。 该系统还包括用于将至少部分失活的催化剂转化为再生催化剂的再生器。 第一管道系统将至少部分失活的催化剂从反应器单元转移到再生器，并且第二管道系统将再生催化剂从再生器传递到多个反应器单元。 任选地，来自多个烃转化装置的催化剂可以被引导到单个汽提单元和/或单个再生单元。

    Process for producing methanol
    6.
    发明申请
    Process for producing methanol 失效
    生产甲醇的方法

    公开(公告)号：US20070021514A1

    公开(公告)日：2007-01-25

    申请号：US11484308

    申请日：2006-07-11

    申请人： James Lattner

    发明人： James Lattner

    IPC分类号： C07C27/26

    CPC分类号： C07C29/1512 ,  C07C29/152 ,  Y02P20/52 ,  C07C31/04

    摘要： This invention is directed to a process for producing methanol. The methanol product that is produced according to this invention is achieved with a high conversion of synthesis gas. The high conversion of synthesis gas is achieved by flowing a liquid layer across a plurality of catalyst beds countercurrent to the gas flow. The gas containing methanol product exiting each bed flows through the liquid layer. The liquid acts to extract methanol from the gas, as well as cool the gas.

    摘要翻译： 本发明涉及一种生产甲醇的方法。 根据本发明生产的甲醇产物是通过合成气的高转化率实现的。 合成气的高转化率是通过使液体层流过与气流逆流的多个催化剂床而实现的。 离开每个床的含甲醇产物的气体流过液体层。 液体用于从气体中提取甲醇，以及冷却气体。

    Multiple riser reactor with centralized catalyst return
    7.
    发明申请
    Multiple riser reactor with centralized catalyst return 有权
    具有集中催化剂返回的多个提升管反应器

    公开(公告)号：US20060229483A1

    公开(公告)日：2006-10-12

    申请号：US11452808

    申请日：2006-06-14

    申请人： Keith Kuechler ,  James Lattner ,  Nicolas Coute ,  Jeffrey Smith ,  Justin Krieger

    发明人： Keith Kuechler ,  James Lattner ,  Nicolas Coute ,  Jeffrey Smith ,  Justin Krieger

    IPC分类号： C07C1/00 ,  B01J8/18

    CPC分类号： C07C51/252 ,  B01J8/0055 ,  B01J8/388 ,  C07C1/20 ,  C10G3/45 ,  C10G3/49 ,  C10G3/62 ,  C10G11/18 ,  C10G2300/1011 ,  C10G2300/1022 ,  C10G2300/1037 ,  C10G2300/4056 ,  C10G2400/02 ,  C10G2400/20 ,  Y02P30/20 ,  Y10S585/921 ,  Y10S585/922 ,  Y10S585/923 ,  Y10S585/924 ,  Y10S585/926 ,  C07C57/04

    摘要： The present invention is directed to a hydrocarbon conversion apparatus and process. The apparatus comprises the following: a plurality of riser reactors, each having a first end into which a catalyst is fed, a second end through which the catalyst can exit, and optionally a center axis extending therebetween. The apparatus also includes a separation zone having a plurality of inlets, each inlet not being oriented along the center axes of the riser reactors, the separation zone being provided to separate the catalyst from products of a reaction conducted in the hydrocarbon conversion apparatus. A plurality of deviating members are also provided, each deviating member being in fluid communication between the second end of a respective riser reactor and a respective inlet of the separation zone. The apparatus also includes a catalyst retention zone provided to contain catalyst, which is fed to the riser reactors. A catalyst return is in fluid communication between the separation zone and the catalyst retention zone.

    摘要翻译： 本发明涉及烃转化装置和方法。 该设备包括以下：多个提升管反应器，每个提升管反应器各自具有供给催化剂的第一端，催化剂可以从其中排出的第二端，以及可选地在其间延伸的中心轴线。 该装置还包括具有多个入口的分离区，每个入口不沿着提升管反应器的中心轴定向，分离区被提供以将催化剂与在烃转化装置中进行的反应产物分离。 还提供了多个偏离构件，每个偏离构件在相应提升管反应器的第二端和分离区的相应入口之间流体连通。 该装置还包括提供用于容纳催化剂的催化剂保留区，催化剂被供给至提升管反应器。 催化剂返回在分离区和催化剂保留区之间流体连通。

    Process for generating alpha olefin comonomers
    10.
    发明申请
    Process for generating alpha olefin comonomers 有权
    产生α-烯烃共聚单体的方法

    公开(公告)号：US20070185362A1

    公开(公告)日：2007-08-09

    申请号：US11654187

    申请日：2007-01-17

    申请人： James Lattner ,  John Walzer ,  Krishnan Sankaranarayanan ,  John Buchanan ,  Milind Ajinkya ,  Stephen Wood ,  Anastasios Skoulidas ,  Jay Reimers ,  Timothy Shaffer

    发明人： James Lattner ,  John Walzer ,  Krishnan Sankaranarayanan ,  John Buchanan ,  Milind Ajinkya ,  Stephen Wood ,  Anastasios Skoulidas ,  Jay Reimers ,  Timothy Shaffer

    IPC分类号： C07C2/02

    CPC分类号： C07C2/32 ,  C07C2/36 ,  C07C2531/22 ,  C07C2531/24 ,  Y02P20/52 ,  C07C11/02

    摘要： The present invention relates to a method for preparing olefin comonomers from ethylene. The comonomer generated can be used in a subsequent process, such as a polyethylene polymerization reactor. The comonomer generated can be transported, optionally without isolation or storage, to a polyethylene polymerization reactor. One method includes the steps of: feeding ethylene and a catalyst in a solvent/diluent to one or more comonomer synthesis reactors; reacting the ethylene and the catalyst under reaction conditions sufficient to produce an effluent comprising a desired comonomer; forming a gas stream comprising unreacted ethylene, and a liquid/bottoms stream comprising the comonomer, optionally by passing the effluent to one or more downstream gas/liquid phase separators; and purifying at least a portion of said liquid/bottoms stream by removing at least one of solid polymer, catalyst, and undesirable olefins therefrom.

    摘要翻译： 本发明涉及从乙烯制备烯烃共聚单体的方法。 所产生的共聚单体可用于随后的方法中，例如聚乙烯聚合反应器。 生成的共聚单体可以任选地不经隔离或储存运输到聚乙烯聚合反应器中。 一种方法包括以下步骤：将乙烯和催化剂在溶剂/稀释剂中进料到一个或多个共聚单体合成反应器中; 在足以产生包含所需共聚单体的流出物的反应条件下使乙烯和催化剂反应; 形成包含未反应的乙烯的气流和包含共聚单体的液体/塔底物流，任选地通过使流出物流到一个或多个下游气/液相分离器; 并通过从其中除去固体聚合物，催化剂和不期望的烯烃中的至少一种来净化至少一部分所述液体/塔底物流。