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    Process, system and facility for desorbing
    1.
    发明授权
    Process, system and facility for desorbing 有权
    脱附的过程，系统和设施

    公开(公告)号：US08062509B2

    公开(公告)日：2011-11-22

    申请号：US12241459

    申请日：2008-09-30

    申请人： Manuela Serban ,  Christopher D. Gosling ,  Maureen L. Bricker

    发明人： Manuela Serban ,  Christopher D. Gosling ,  Maureen L. Bricker

    IPC分类号： C07C7/12

    CPC分类号： C10G25/003 ,  B01J20/20 ,  B01J20/3416 ,  B01J20/3475 ,  C10G11/18 ,  C10G67/06

    摘要： One exemplary embodiment can be a process for desorbing one or more polynuclear aromatics from at least one fraction from a hydrocracking zone using an adsorption zone. The adsorption zone can include first and second vessels. Generally, the process includes passing the at least one fraction from an effluent of the hydrocracking zone through the first vessel containing a first activated carbon, and passing a petroleum fraction boiling in the range of about 200-about 400° C. for desorbing the one or more polynuclear aromatics through the second vessel containing a second activated carbon.

    摘要翻译： 一个示例性实施方案可以是使用吸附区从加氢裂化区从至少一个馏分解吸一种或多种多环芳烃的方法。 吸附区可以包括第一和第二容器。 通常，该方法包括将来自加氢裂化区的流出物的至少一个馏分通过含有第一活性炭的第一容器，并通过在约200-约400℃范围内沸腾的石油馏分以解吸一个 或更多个多核芳族化合物通过含有第二活性炭的第二容器。

    PROCESS, SYSTEM AND FACILITY FOR DESORBING
    2.
    发明申请
    PROCESS, SYSTEM AND FACILITY FOR DESORBING 有权
    过程，系统和设施的解决

    公开(公告)号：US20100078359A1

    公开(公告)日：2010-04-01

    申请号：US12241459

    申请日：2008-09-30

    申请人： Manuela Serban ,  Christopher D. Gosling ,  Maureen L. Bricker

    发明人： Manuela Serban ,  Christopher D. Gosling ,  Maureen L. Bricker

    IPC分类号： C10G25/00 ,  B01D15/00 ,  B01J19/00

    CPC分类号： C10G25/003 ,  B01J20/20 ,  B01J20/3416 ,  B01J20/3475 ,  C10G11/18 ,  C10G67/06

    摘要： One exemplary embodiment can be a process for desorbing one or more polynuclear aromatics from at least one fraction from a hydrocracking zone using an adsorption zone. The adsorption zone can include first and second vessels. Generally, the process includes passing the at least one fraction from an effluent of the hydrocracking zone through the first vessel containing a first activated carbon, and passing a petroleum fraction boiling in the range of about 200-about 400° C. for desorbing the one or more polynuclear aromatics through the second vessel containing a second activated carbon.

    摘要翻译： 一个示例性实施方案可以是使用吸附区从加氢裂化区从至少一个馏分解吸一种或多种多环芳烃的方法。 吸附区可以包括第一和第二容器。 通常，该方法包括将来自加氢裂化区的流出物的至少一个馏分通过含有第一活性炭的第一容器，并通过在约200-约400℃范围内沸腾的石油馏分以解吸一个 或更多个多核芳族化合物通过含有第二活性炭的第二容器。

    CATALYST FOR CONVERSION OF HYDROCARBONS
    6.
    发明申请
    CATALYST FOR CONVERSION OF HYDROCARBONS 有权
    碳氢化合物转化催化剂

    公开(公告)号：US20130261363A1

    公开(公告)日：2013-10-03

    申请号：US13547351

    申请日：2012-07-12

    申请人： Manuela Serban ,  Mark P. Lapinski

    发明人： Manuela Serban ,  Mark P. Lapinski

    IPC分类号： B01J23/63 ,  C07C5/42 ,  B01J21/04 ,  B01J27/135 ,  B01J27/138 ,  B01J27/13

    CPC分类号： B01J37/18 ,  B01J23/63 ,  B01J27/10 ,  B01J27/13 ,  B01J27/135 ,  B01J27/138 ,  B01J35/008 ,  B01J35/08 ,  B01J37/0072 ,  B01J37/0201 ,  C10G35/06 ,  C10G69/10 ,  C10G2300/1044 ,  C10G2400/02 ,  C10G2400/04

    摘要： One embodiment is a catalyst for catalytic reforming of naphtha. The catalyst can have a noble metal including one or more of platinum, palladium, rhodium, ruthenium, osmium, and iridium, an alkali or alkaline-earth metal, a lanthanide-series metal, and a support. Generally, an average bulk density of the catalyst is about 0.300 to about 1.00 gram per cubic centimeter. The catalyst has a platinum content of less than about 0.375 wt %, a tin content of about 0.1 to about 2 wt %, a potassium content of about 100 to about 600 wppm, and a cerium content of about 0.1 to about 1 wt %. The lanthanide-series metal can be distributed at a concentration of the lanthanide-series metal in a 100 micron surface layer of the catalyst less than two times a concentration of the lanthanide-series metal at a central core of the catalyst.

    摘要翻译： 一个实施方案是用于石脑油催化重整的催化剂。 催化剂可以具有包括铂，钯，铑，钌，锇和铱中的一种或多种的贵金属，碱金属或碱土金属，镧系金属和载体。 通常，催化剂的平均体积密度为约0.300至约1.00克/立方厘米。 催化剂的铂含量小于约0.375重量％，锡含量为约0.1至约2重量％，钾含量为约100至约600wppm，铈含量为约0.1至约1重量％。 镧系元素金属可以在催化剂的100微米表面层中以镧系元素金属的浓度分布，其量小于催化剂中心核心处的镧系金属浓度的两倍。

    PROCESS FOR REMOVING NITROGEN FROM FUEL STREAMS WITH CAPROLACTAMIUM IONIC LIQUIDS
    7.
    发明申请
    PROCESS FOR REMOVING NITROGEN FROM FUEL STREAMS WITH CAPROLACTAMIUM IONIC LIQUIDS 有权
    用碳酰氯离子液体从燃料流中除去硝酸的方法

    公开(公告)号：US20130248423A1

    公开(公告)日：2013-09-26

    申请号：US13429596

    申请日：2012-03-26

    申请人： Manuela Serban ,  Alan B. Levy ,  Lihao Tang ,  Alakananda Bhattacharyya

    发明人： Manuela Serban ,  Alan B. Levy ,  Lihao Tang ,  Alakananda Bhattacharyya

    IPC分类号： C10G17/00

    CPC分类号： C10G21/27 ,  C10G21/28 ,  C10G31/08 ,  C10G53/06 ,  C10G2300/202

    摘要： A process for removing a nitrogen compound from a fuel feed, such as vacuum gas oil or diesel fuel, wherein the process includes contacting the fuel feed comprising the nitrogen compound with a fuel-immiscible caprolactamium ionic liquid to produce a fuel and fuel-immiscible caprolactamium ionic liquid mixture, and separating the mixture to produce a vacuum gas oil or a diesel effluent having a reduced nitrogen content relative to the vacuum gas oil or diesel feed. The invention provides an alternate use for caprolactamium ionic liquid that is produced in large quantities for the manufacture of caprolactam.

    摘要翻译： 一种从诸如减压瓦斯油或柴油燃料的燃料进料中除去氮化合物的方法，其中所述方法包括使包含氮化合物的燃料进料与燃料不混溶的己内酰胺离子液体接触以产生燃料和燃料不混溶的己内酰胺 离子液体混合物，并分离混合物以产生相对于真空瓦斯油或柴油进料具有降低的氮含量的减压瓦斯油或柴油流出物。 本发明提供了大量生产己内酰胺的己内酰胺离子液体的替代用途。

    INTEGRATED HYDROGENATION/DEHYDROGENATION REACTOR IN A PLATFORMING PROCESS
    8.
    发明申请
    INTEGRATED HYDROGENATION/DEHYDROGENATION REACTOR IN A PLATFORMING PROCESS 有权
    一体化加氢过程中的氢化/脱氢反应器

    公开(公告)号：US20130158311A1

    公开(公告)日：2013-06-20

    申请号：US13327178

    申请日：2011-12-15

    申请人： Manuela Serban ,  Kurt M. Vanden Bussche ,  Mark D. Moser ,  David A. Wegerer

    发明人： Manuela Serban ,  Kurt M. Vanden Bussche ,  Mark D. Moser ,  David A. Wegerer

    IPC分类号： C07C5/42

    CPC分类号： C10G59/00 ,  C10G2400/30

    摘要： A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and partially processing each feedstream in separate reactors. The processing includes passing the light stream to a combination hydrogenation/dehydrogenation reactor. The process reduces the energy by reducing the endothermic properties of intermediate reformed process streams.

    摘要翻译： 提出了一种重整烃流的方法。 该方法包括将石脑油进料流分成至少两个进料流，并在单独的反应器中部分处理每个进料流。 该处理包括将光流传递到组合氢化/脱氢反应器。 该方法通过降低中间重整工艺流的吸热性能来降低能量。