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140 条记录 (耗时 0.037 秒)

    Process for producing cyclohexanone
    94.
    发明授权
    Process for producing cyclohexanone 有权
    环己酮生产工艺

    公开(公告)号：US08222459B2

    公开(公告)日：2012-07-17

    申请号：US12933700

    申请日：2009-02-19

    申请人： Jihad M. Dakka ,  John S. Buchanan ,  James R. Lattner ,  Sadi Mizrahi

    发明人： Jihad M. Dakka ,  John S. Buchanan ,  James R. Lattner ,  Sadi Mizrahi

    IPC分类号： C07C45/00

    CPC分类号： C07C407/00 ,  C07C37/07 ,  C07C37/08 ,  C07C45/006 ,  C07C45/53 ,  C07C2601/14 ,  C07C39/04 ,  C07C49/403 ,  C07C409/14

    摘要： In a process for producing cyclohexanone, cyclohexylbenzene is oxidized to produce cyclohexylbenzene hydroperoxide and then the resultant cyclohexylbenzene hydroperoxide is cleaved to produce an effluent stream comprising phenol and cyclohexanone. At least a portion of the effluent stream is then fed to at least one hydrogenation reaction zone, where the effluent stream portion is contacted with hydrogen in the presence of a hydrogenation catalyst under conditions effective to convert at least part of the phenol in the effluent portion into cyclohexanone.

    摘要翻译： 在制备环己酮的方法中，环己基苯被氧化以产生环己基苯氢过氧化物，然后将所得环己基苯氢过氧化物切割以产生包含苯酚和环己酮的流出物流。 然后将至少一部分流出物流送入至少一个氢化反应区，在氢化催化剂存在下，在有效地将至少部分苯酚在流出物部分中转化的条件下，流出料流部分与氢气接触 加入环己酮。

    Methane Conversion Process
    95.
    发明申请
    Methane Conversion Process 有权
    甲烷转化过程

    公开(公告)号：US20120036889A1

    公开(公告)日：2012-02-16

    申请号：US13184954

    申请日：2011-07-18

    申请人： Larry L. Iaccino ,  Robert D. Denton ,  Garth M. Norman ,  James R. Lattner

    发明人： Larry L. Iaccino ,  Robert D. Denton ,  Garth M. Norman ,  James R. Lattner

    IPC分类号： F25J3/08 ,  C07C2/00

    CPC分类号： C07C2/76 ,  C07C2529/69 ,  C10L3/08 ,  F25J3/0209 ,  F25J3/0223 ,  F25J3/0233 ,  F25J3/0252 ,  F25J2210/62 ,  F25J2215/04 ,  F25J2270/904 ,  Y02P20/125 ,  C07C15/04 ,  C07C15/24

    摘要： A process for converting a gaseous hydrocarbon feed comprising methane to an aromatic hydrocarbon is integrated with liquefied natural gas (LNG) and/or pipeline gas production. In the integrated process, the gaseous hydrocarbon feed is supplied to a conversion zone comprising at least one dehydroaromatization catalyst and is contacted with the catalyst under conversion conditions to produce a gaseous effluent stream comprising at least one aromatic compound, unreacted methane and H2. The gaseous effluent stream is then separated into a first product stream comprising said at least one aromatic compound and a second product stream comprising unreacted methane and H2. The second product stream is further separated into a methane-rich stream and a hydrogen-rich stream and at least part of the methane-rich stream is passed to LNG and/or pipeline gas production. The gaseous hydrocarbon feed supplied to the conversion zone has at least one of the following properties: (i) a sulfur level of at least 25 ppm by volume; (ii) a CO2 level of at least 50 ppm by volume; and (iii) a dew point of at least 203° K.

    摘要翻译： 将包含甲烷的气态烃进料转化成芳烃的方法与液化天然气（LNG）和/或管道气生产相结合。 在一体化方法中，将气态烃进料供给至包含至少一种脱氢芳烃化催化剂的转化区，并在转化条件下与催化剂接触以产生包含至少一种芳族化合物，未反应甲烷和H 2的气态流出物流。 然后将气态流出物流分离成包含所述至少一种芳族化合物的第一产物流和包含未反应的甲烷和H 2的第二产物流。 第二产物流进一步分离成富甲烷流和富氢流，至少部分富甲烷流被送到LNG和/或管道气生产。 供应到转化区的气态烃进料具有以下特性中的至少一个：（i）至少25ppm体积的硫含量; （ii）至少50ppm体积的CO 2水平; 和（iii）至少203°K的露点。

    Method of circulating catalyst between a catalyst regenerator and an external catalyst cooler
    98.
    发明授权
    Method of circulating catalyst between a catalyst regenerator and an external catalyst cooler 有权
    在催化剂再生器和外部催化剂冷却器之间循环催化剂的方法

    公开(公告)号：US07906697B2

    公开(公告)日：2011-03-15

    申请号：US12059717

    申请日：2008-03-31

    申请人： James H. Beech, Jr. ,  Chunshe Cao ,  Michael P. Nicoletti ,  James R. Lattner ,  Jesse F. Goellner ,  Rutton D. Patel ,  Timothy M. Healy

    发明人： James H. Beech, Jr. ,  Chunshe Cao ,  Michael P. Nicoletti ,  James R. Lattner ,  Jesse F. Goellner ,  Rutton D. Patel ,  Timothy M. Healy

    IPC分类号： C07C2/04

    CPC分类号： C07C1/20 ,  B01J29/90 ,  B01J38/30 ,  B01J38/32 ,  C07C2529/40 ,  C07C2529/70 ,  C07C2529/83 ,  C07C2529/85 ,  C10G3/49 ,  C10G3/62 ,  C10G2300/802 ,  C10G2400/20 ,  Y02P20/584 ,  Y02P30/20 ,  C07C11/02

    摘要： This invention relates to efficiently regenerating catalyst particles by minimizing the formation of localized “hot spots” and “cold spots” in a regeneration zone. Specifically this invention relates to a method for controlling regenerator temperature in an oxygenates-to-olefins system, comprising the steps of: contacting an oxygenate feed in a reactor with a catalytically effective amount of molecular sieve-containing catalyst under conditions effective for converting said oxygenate to a product containing light olefins and forming a coked catalyst; contacting a portion of the coked catalyst in a regenerator, having a catalyst bed height (Hc), an inlet height (Hi), and an outlet height (Ho), with an oxygen-containing regeneration medium under conditions effective to at least partially regenerate the coked catalyst; and conducting a portion of the catalyst from the regenerator to a catalyst cooler to form a cooled catalyst portion, wherein Ho is greater than Hi.

    摘要翻译： 本发明涉及通过最小化再生区中局部“热点”和“冷点”的形成来有效地再生催化剂颗粒。 具体地说，本发明涉及一种用于控制含氧化合物至烯烃体系中的再生器温度的方法，其包括以下步骤：在有效转化所述含氧化合物的条件下使反应器中的含氧化合物进料与催化有效量的含分子筛催化剂接触 涉及含有轻质烯烃并形成焦化催化剂的产品; 在具有催化剂床高度（Hc），入口高度（Hi）和出口高度（Ho））的再生器中使一部分焦化催化剂与含氧再生介质在有效至少部分再生的条件下接触 焦化催化剂; 并将催化剂的一部分从再生器导入催化剂冷却器以形成冷却的催化剂部分，其中Ho大于Hi。