公开(公告)号：US20050113623A1

公开(公告)日：2005-05-26

申请号：US10720505

申请日：2003-11-24

申请人： Keith Kuechler ,  Jeffrey Brinen ,  James Lattner ,  Allen Gawlik

发明人： Keith Kuechler ,  Jeffrey Brinen ,  James Lattner ,  Allen Gawlik

IPC分类号： C07C1/20 ,  C07C1/00 ,  B01J8/04

CPC分类号： C07C1/20 ,  Y02P30/42 ,  C07C11/06 ,  C07C11/04 ,  C07C11/02

摘要： A process and apparatus are provided for converting oxygenate to olefins which comprises: contacting a feedstock comprising oxygenate with a catalyst comprising a molecular sieve under conditions effective to produce a vaporous product comprising the olefins, water and unreacted oxygenate; condensing the vaporous product to provide a liquid stream rich in the water and unreacted oxygenate, and an olefins-rich vapor stream; introducing at least part of the liquid stream to a feed tray in a fractionation tower which provides an oxygenate-rich overhead product and a water-rich liquid bottoms product; providing a liquid, oxygenate-rich stream comprising at least about 20 wt % oxygenate above the feed tray; and passing the olefins-rich vapor stream through a recovery train to recover at least some of the olefins.

摘要翻译： 提供了将含氧化合物转化为烯烃的方法和装置，其包括：在有效产生包含烯烃，水和未反应的含氧化合物的蒸气产物的条件下，使包含含氧化合物的原料与包含分子筛的催化剂接触; 冷凝蒸汽产物以提供富含水和未反应的含氧化合物的液体物流和富含烯烃的蒸汽流; 将至少部分液体物流引入分馏塔中的进料塔中，所述分馏塔提供富氧富含塔顶馏出物和富含水的液体塔底产物; 提供在所述进料盘上方含有至少约20重量％含氧化合物的液体富含氧化物流; 并使富含烯烃的蒸气流通过回收馏分以回收至少一些烯烃。

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。

公开(公告)号：US20070078287A1

公开(公告)日：2007-04-05

申请号：US11601999

申请日：2006-11-20

申请人： James Lattner ,  Keith Kuechler ,  Richard Walter

发明人： James Lattner ,  Keith Kuechler ,  Richard Walter

IPC分类号： C07C1/00

CPC分类号： B01J38/30 ,  B01J29/90 ,  C07C1/20 ,  C07C2529/70 ,  C07C2529/85 ,  Y02P20/584 ,  Y02P30/42 ,  C07C11/02

摘要： The present invention provides a method for adding heat to a reactor system used to convert oxygenates to olefin, in which supplemental heat is added with a heating fuel, e.g., a torch oil, having low autoignition temperature, low sulfur, and low nitrogen content.

摘要翻译： 本发明提供一种用于向用于将含氧化合物转化为烯烃的反应器系统中加热的方法，其中补充的热量加入具有低自燃温度，低硫和低氮含量的加热燃料，例如割炬油。

公开(公告)号：US20050067326A1

公开(公告)日：2005-03-31

申请号：US10656673

申请日：2003-09-05

申请人： Stephen Vaughn ,  Kenneth Clem ,  Keith Kuechler ,  James Lattner

发明人： Stephen Vaughn ,  Kenneth Clem ,  Keith Kuechler ,  James Lattner

IPC分类号： B01J8/00 ,  C07C1/20 ,  C10G3/00 ,  B07B4/00 ,  B07B7/00 ,  B07B13/00

CPC分类号： B01J8/0065 ,  B01J8/0055 ,  C07C1/20 ,  C10G3/49 ,  C10G3/62 ,  C10G2300/4093 ,  C10G2400/20 ,  Y02P30/20 ,  C07C11/02

摘要： The present invention provides various processes for selectively removing undesirably sized catalyst particles from a reaction system. In one embodiment, a plurality of catalyst particles, having a first median particle diameter, is withdrawn from the reaction system and is directed to a separation unit such as a counter flow cyclone separator. In the separation unit, the particles are separated into a small catalyst stream and a large catalyst stream, the small catalyst stream having a second median particle diameter less than the first median particle diameter, and the large catalyst stream having a third median particle diameter greater than the first median particle diameter. At least a portion of the small or large catalyst stream is then directed back to the reaction system in order to maintain a desirable particle size distribution therein.

摘要翻译： 本发明提供了用于从反应体系中选择性除去不期望的尺寸的催化剂颗粒的各种方法。 在一个实施方案中，具有第一中值粒径的多个催化剂颗粒从反应体系中排出并被引导至分离单元如逆流旋风分离器。 在分离单元中，将颗粒分离成小的催化剂流和大的催化剂流，小的催化剂流具有小于第一中值粒径的第二中值粒径，并且大的催化剂流具有较大的第三中值粒径 比第一个中值粒径。 然后将至少一部分小或大的催化剂流引导回反应体系，以便在其中保持所需的粒度分布。

公开(公告)号：US20050152814A1

公开(公告)日：2005-07-14

申请号：US11076233

申请日：2005-03-09

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

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

IPC分类号： B01J8/08 ,  B01J8/00 ,  B01J8/18 ,  B01J8/24 ,  B01J8/26 ,  C07B61/00 ,  C07C1/20 ,  C07C11/02 ,  C10G3/00 ,  C10G11/18 ,  B32B5/02

CPC分类号： B01J8/26 ,  B01J8/0055 ,  B01J8/1845 ,  B01J8/1872 ,  C10G3/49 ,  C10G3/62 ,  C10G11/18 ,  C10G2300/4093 ,  C10G2400/20 ,  Y10S585/921 ,  Y10S585/922 ,  Y10S585/923 ,  Y10S585/926

摘要： The present invention is directed to a hydrocarbon conversion apparatus. The apparatus comprises the following: a plurality of riser reactors, each of the riser reactors having a first end into which a catalyst can be fed and a second end through which the catalyst can exit the riser reactor, a separation zone into which the second ends of the riser reactors extend, the separation zone being provided to separate the catalyst from products of a reaction conducted in the hydrocarbon conversion apparatus; and at least one catalyst return in fluid communication with the separation zone and the first ends of the riser reactors, the catalyst return being provided to transfer the catalyst from the separation zone to the first ends of the riser reactors.

摘要翻译： 本发明涉及烃转化装置。 该设备包括以下：多个提升管反应器，每个提升管反应器具有第一端，催化剂可以进入该第一端，催化剂可以通过该第二端离开提升管反应器;分离区，第二端 提供的分离区被提供以将催化剂与在烃转化装置中进行的反应的产物分离; 并且至少一个催化剂返回与分离区和提升管反应器的第一端流体连通，提供催化剂返回以将催化剂从分离区转移到提升管反应器的第一端。

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。

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。

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。

公开(公告)号：US20050245781A1

公开(公告)日：2005-11-03

申请号：US10835494

申请日：2004-04-29

申请人： Luc Martens ,  James Lattner ,  Rutton Patel ,  David Skouby ,  Stephen Vaughn ,  Yun-feng Chang ,  Jesse Goellner ,  Mareel Janssen ,  Richard Senior

发明人： Luc Martens ,  James Lattner ,  Rutton Patel ,  David Skouby ,  Stephen Vaughn ,  Yun-feng Chang ,  Jesse Goellner ,  Mareel Janssen ,  Richard Senior

IPC分类号： B01J8/00 ,  B01J8/24 ,  C07C1/20 ,  C10G3/00

CPC分类号： B01J8/1809 ,  B01J8/0025 ,  B01J2208/00672 ,  B01J2208/00752 ,  B01J2208/00769 ,  C07C1/20 ,  C10G3/42 ,  C10G3/45 ,  C10G3/47 ,  C10G3/49 ,  C10G2300/703 ,  C10G2400/20 ,  Y02P30/20 ,  C07C11/02

摘要： This invention provides processes for maintaining a desired particle size distribution in an oxygenate to olefin reaction system. In one embodiment, the invention comprises replacing lost catalyst fines with less active co-catalyst particles. By adding less active co-catalyst particles to the reaction system, desirable fluidization characteristics and hydrodynamics can be maintained without affecting the overall (or primary catalyst) performance and product selectivities. The invention is also directed to a population of catalyst particles having a desirable particle size distribution well-suited for realizing ideal fluidization and hydrodynamic characteristics.

摘要翻译： 本发明提供了在含氧化合物至烯烃反应体系中维持所需粒度分布的方法。 在一个实施方案中，本发明包括用较少活性的助催化剂颗粒代替失去的催化剂细粉。 通过将更少的活性助催化剂颗粒加入到反应体系中，可以保持所需的流化特性和流体动力学，而不影响总体（或初级催化剂）性能和产物选择性。 本发明还涉及具有适合于实现理想的流化和流体动力特性的理想粒度分布的催化剂颗粒群。

公开(公告)号：US20050087477A1

公开(公告)日：2005-04-28

申请号：US10995869

申请日：2004-11-23

申请人： James Lattner ,  Jeffrey Smith ,  Rathna Davuluri

发明人： James Lattner ,  Jeffrey Smith ,  Rathna Davuluri

IPC分类号： B01J8/00 ,  B01J8/18 ,  C10G11/18 ,  C10G11/04 ,  C07C1/00

CPC分类号： B01J8/1863 ,  B01J8/0065 ,  B01J8/008 ,  B01J2208/00663 ,  C10G11/18 ,  Y10S208/01

摘要： This invention is to a circulating fluid bed reactor that is designed so as to have the ability to adjust catalyst holdup within the reaction zone of the reactor while maintaining substantially constant catalyst circulation rate through the reaction zone. The ability to adjust catalyst hold up independently of catalyst circulation rate provides an advantage of having the ability to maintain a constant conversion level as catalyst activity or feed rates change.