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18 条记录 (耗时 0.032 秒)

    Converting oxygenates to olefins over a catalyst comprising acidic molecular sieve of controlled carbon atom to acid site ratio
    4.
    发明授权
    Converting oxygenates to olefins over a catalyst comprising acidic molecular sieve of controlled carbon atom to acid site ratio 有权
    将含氧化合物转化为含有控制碳原子的酸性分子筛的催化剂与酸性位置比

    公开(公告)号：US07227048B2

    公开(公告)日：2007-06-05

    申请号：US10227907

    申请日：2002-08-26

    申请人： Paul N. Chisholm ,  Nicolas P. Coute ,  James R. Lattner ,  Teng Xu ,  Jeffrey S. Smith ,  Keith Holroyd Kuechler

    发明人： Paul N. Chisholm ,  Nicolas P. Coute ,  James R. Lattner ,  Teng Xu ,  Jeffrey S. Smith ,  Keith Holroyd Kuechler

    IPC分类号： C07C1/20

    CPC分类号： B01J38/12 ,  B01J29/85 ,  B01J29/90 ,  C07C1/20 ,  C07C2529/70 ,  C07C2529/85 ,  C10G3/49 ,  C10G3/62 ,  C10G2300/708 ,  C10G2400/20 ,  Y02P20/584 ,  Y02P30/20 ,  Y02P30/42 ,  C07C11/02

    摘要： The present invention provides a process for making an olefin product from an oxygenate-containing feedstock comprising:a) contacting the feedstock in a reaction zone with catalyst particles comprising a molecular sieve containing acid sites and having an average coke loading of 1 to 10 carbon atoms per acid site of said molecular sieve, under conditions effective to convert the feedstock into an olefin product stream and to provide unregenerated catalyst particles,b) removing a portion of said catalyst particles from said reaction zone and contacting said portion with a regeneration medium in a regeneration zone under conditions effective to obtain regenerated catalyst particles which have an average coke loading of no greater than 10 carbon atoms per acid site of said molecular sieve, andc) introducing said regenerated catalyst particles into said reaction zone to provide a catalyst mixture of unregenerated catalyst particles and regenerated catalyst particles, in an amount sufficient to provide an average coke loading on said catalyst mixture in an amount ranging from 1 to 10 carbon atoms per acid site of said molecular sieve.

    摘要翻译： 本发明提供了一种从含氧化合物原料制备烯烃产物的方法，包括：a）使反应区中的原料与包含含有酸性位点并具有1-10个碳原子的平均焦炭负载的分子筛的催化剂颗粒接触 在有效将原料转化为烯烃产物流并提供未再生催化剂颗粒的条件下，在所述分子筛的每个酸性位点处，b）从所述反应区除去一部分所述催化剂颗粒，并将所述部分与再生介质接触， 在有效获得在所述分子筛的每个酸性位点具有不大于10个碳原子的平均焦炭负载量的再生催化剂颗粒的条件下，c）将所述再生催化剂颗粒引入所述反应区以提供未再生的催化剂混合物 催化剂颗粒和再生催化剂颗粒，其量足够 以在所述催化剂混合物上提供在所述分子筛的每个酸性位置上具有1至10个碳原子的量的平均焦炭负载量。

    Multiple riser reactor with centralized catalyst return
    6.
    发明授权
    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：US07385099B2

    公开(公告)日：2008-06-10

    申请号：US11452808

    申请日：2006-06-14

    申请人： Keith Holroyd Kuechler ,  James R. Lattner ,  Nicolas P. Coute ,  Jeffrey S. Smith ,  Justin Leonard Krieger

    发明人： Keith Holroyd Kuechler ,  James R. Lattner ,  Nicolas P. Coute ,  Jeffrey S. Smith ,  Justin Leonard Krieger

    IPC分类号： C07C1/00

    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线定向，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。

    Phenol and Cyclohexanone Mixtures
    7.
    发明申请
    Phenol and Cyclohexanone Mixtures 有权
    苯酚和环己酮混合物

    公开(公告)号：US20130231506A1

    公开(公告)日：2013-09-05

    申请号：US13814890

    申请日：2011-08-16

    申请人： Keith Holroyd Kuechler ,  Francisco Manuel Benitez

    发明人： Keith Holroyd Kuechler ,  Francisco Manuel Benitez

    IPC分类号： C07C49/403 ,  C07C39/04

    CPC分类号： C07C49/403 ,  C07C37/08 ,  C07C37/82 ,  C07C37/86 ,  C07C39/04 ,  C07C45/85 ,  C07C407/00 ,  C07C2601/14 ,  Y02P20/52

    摘要： Disclosed herein is a process for producing phenol. The process includes oxidizing at least a portion of a feed comprising cyclohexylbenzene to produce an oxidation composition comprising cyclohexyl-1-phenyl-1-hydroperoxide. The oxidation composition may then be cleaved in the presence of an acid catalyst to produce a cleavage reaction mixture comprising the acid catalyst, phenol and cyclohexanone. At least a portion of the cleavage reaction mixture may be neutralized with a basic material to form a treated cleavage reaction mixture. In various embodiments, the cleavage reaction mixture contains 1 wt % to 30 wt % phenol, 1 wt % to 30 wt % cyclohexanone and a complexation product.

    摘要翻译： 本文公开了一种生产苯酚的方法。 该方法包括氧化至少一部分包含环己基苯的进料以产生包含环己基-1-苯基-1-氢过氧化物的氧化组合物。 然后可以在酸催化剂的存在下将氧化组合物切割，以产生包含酸催化剂，苯酚和环己酮的裂解反应混合物。 裂解反应混合物的至少一部分可以用碱性物质中和以形成经处理的裂解反应混合物。 在各种实施方案中，裂解反应混合物含有1重量％至30重量％的苯酚，1重量％至30重量％的环己酮和络合产物。

    Regeneration temperature control in a catalytic reaction system
    9.
    发明授权
    Regeneration temperature control in a catalytic reaction system 失效
    催化反应体系中的再生温度控制

    公开(公告)号：US07256318B2

    公开(公告)日：2007-08-14

    申请号：US10403270

    申请日：2003-03-28

    申请人： James R. Lattner ,  Keith Holroyd Kuechler ,  Nicolas P. Coute ,  Paul N. Chisholm

    发明人： James R. Lattner ,  Keith Holroyd Kuechler ,  Nicolas P. Coute ,  Paul N. Chisholm

    IPC分类号： C07C1/00 ,  B01J38/12

    CPC分类号： B01J38/12 ,  B01J29/90 ,  C07C1/20 ,  Y02P20/584 ,  C07C11/02

    摘要： This invention is directed to controlling regenerator temperature in an oxygenate to olefin process. Because a significant amount of heat can produced in the regenerator during the regeneration process, at least a portion of the heat must be removed to keep the system from getting too hot. This invention removes heat during the regeneration of the catalyst, using appropriate circulation of catalyst between the reactor and the regenerator. Sufficient circulation can eliminate the need for the use of a catalyst cooler in the regeneration system.

    摘要翻译： 本发明涉及控制含氧化合物至烯烃过程中的再生器温度。 因为在再生过程中可以在再生器中产生大量的热量，必须除去至少一部分热量以保持系统不会变得太热。 本发明在催化剂的再生过程中，使用催化剂在反应器和再生器之间的适当循环来除去热量。 足够的循环可以消除在再生系统中使用催化剂冷却器的需要。