利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

8 条记录 (耗时 0.03 秒)

    FLUID CATALYTIC CRACKING CATALYST STRIPPING
    2.
    发明申请
    FLUID CATALYTIC CRACKING CATALYST STRIPPING 审中-公开
    流体催化裂化催化剂剥离

    公开(公告)号：US20120103870A1

    公开(公告)日：2012-05-03

    申请号：US13281903

    申请日：2011-10-26

    申请人： John Scott Buchanan ,  Steven S. Lowenthal ,  George A. Swan, III ,  James O. Guerra

    发明人： John Scott Buchanan ,  Steven S. Lowenthal ,  George A. Swan, III ,  James O. Guerra

    IPC分类号： C10G11/00 ,  B01J8/00

    CPC分类号： B01J8/388 ,  B01J8/0055 ,  B01J8/1827 ,  B01J8/1872 ,  B01J2208/0084 ,  C10G11/18 ,  C10G2300/70

    摘要： This disclosure relates to devices, e.g., baffle plate and combination dipleg valve/baffle devices, for use in achieving rapid disengagement of entrained hydrocarbons vapors, especially in high flux spent catalyst flow exiting from a cyclone separator dipleg in a fluidized catalytic cracking (FCC) unit. The baffle plate is preferably located near and typically below the catalyst dipleg of a fluid catalytic cracking reactor or separation zone and comprises a baffle plate body member having a surface, and in preferred embodiments also includes one or more apertures located on at least a portion of the surface. The valve/baffle is located at the outlet of the catalyst dipleg and comprises a combination valve and catalyst baffle in which the valve/baffle is designed to allow the top surface of the valve/baffle to seat against the dipleg outlet until the weight of the catalyst above the valve/baffle forces it to open. This disclosure also relates to FCC units that include the devices, and FCC methods utilizing the devices.

    摘要翻译： 本公开涉及用于实现夹带的烃蒸气的快速脱离，特别是在流化床催化裂化（FCC）中从旋风分离器三通流出来的高通量废催化剂流中的装置，例如挡板和组合式二通阀/挡板装置， 单元。 挡板优选地位于流化床催化裂化反应器或分离区的催化剂二段附近并且通常位于其下方，并且包括具有表面的挡板主体构件，并且在优选实施例中还包括位于至少一部分上的一个或多个孔 表面。 阀/挡板位于催化剂液滴的出口处，并且包括组合阀和催化剂挡板，其中阀/挡板被设计成允许阀/挡板的顶表面抵靠径向出口抵靠直到重量 在阀/挡板上方的催化剂迫使其打开。 本公开还涉及包括设备的FCC单元以及利用该设备的FCC方法。

    Removal of nitrogen compounds from FCC distillate
    4.
    发明授权
    Removal of nitrogen compounds from FCC distillate 有权
    从FCC馏出物中除去氮化合物

    公开(公告)号：US08673134B2

    公开(公告)日：2014-03-18

    申请号：US12908091

    申请日：2010-10-20

    申请人： Stacey E. Siporin ,  David Thomas Ferrughelli ,  Steven S. Lowenthal ,  Randolph J. Smiley ,  Alan Roy Katritzky ,  Bruce R. Cook

    发明人： Stacey E. Siporin ,  David Thomas Ferrughelli ,  Steven S. Lowenthal ,  Randolph J. Smiley ,  Alan Roy Katritzky ,  Bruce R. Cook

    IPC分类号： C10G29/24

    CPC分类号： C10G11/18 ,  C10G21/16 ,  C10G29/24 ,  C10G45/02 ,  C10G67/00 ,  C10G69/12

    摘要： A method for the removal of nitrogen compounds from FCC feed or from catalytically cracked distillates including FCC cycle oils by using formaldehyde to selectively couple organic heterocyclic nitrogen species in the FCC feed or FCC distillate to form higher boiling coupling products out of the boiling range of FCC distillate. Removal of the nitrogenous compounds improves the operation of subsequent hydrodesulfurization steps needed for the distillate fraction to conform to low sulfur standards. The formaldehyde is preferably used in the form of paraformaldehyde. The reaction between the nitrogenous compounds in the cycle oil fraction with the formaldehyde is conveniently carried out in the cycle oil pumparound circuit of the FCC main column.

    摘要翻译： 一种从FCC原料或催化裂化的馏出物（包括FCC循环油）中除去氮化合物的方法，该方法是使用甲醛选择性地将FCC原料中的有机杂环氮物质或FCC馏出物结合，从而在FCC沸点范围内形成较高沸点的偶联产物 馏出物 去除含氮化合物改善了馏出物馏分所需的随后加氢脱硫步骤的操作以符合低硫标准。 甲醛优选以多聚甲醛的形式使用。 循环油馏分中的含氮化合物与甲醛的反应在FCC主塔的循环油循环回路中方便地进行。

    Process for flexible vacuum gas oil conversion
    5.
    发明授权
    Process for flexible vacuum gas oil conversion 有权
    柔性真空瓦斯油转化工艺

    公开(公告)号：US08163168B2

    公开(公告)日：2012-04-24

    申请号：US12459729

    申请日：2009-07-07

    申请人： Martin L. Gorbaty ,  Bruce R. Cook ,  David T. Ferrughelli ,  Jason B. English ,  Steven S. Lowenthal

    发明人： Martin L. Gorbaty ,  Bruce R. Cook ,  David T. Ferrughelli ,  Jason B. English ,  Steven S. Lowenthal

    IPC分类号： C10G69/04

    CPC分类号： C10G69/06 ,  C10G11/18 ,  C10G51/04 ,  C10G69/02 ,  C10G69/04 ,  C10G2300/1074 ,  C10G2300/4081 ,  C10G2400/02

    摘要： The present invention relates to a process for the selective conversion of hydrocarbon feed having a Conradson Carbon Residue content of 0 to 6 wt %, based on the hydrocarbon feed. The hydrocarbon feed is treated in a two-step process. The first is thermal conversion and the second is catalytic cracking of the products of the thermal conversion. The present invention results in a process for increasing the distillate production from a hydrocarbon feedstream for a fluid catalytic cracking unit. The resulting product slate from the present invention can be further varied by changing the conditions in the thermal and catalytic cracking steps as well as by changing the catalyst in the cracking step.

    摘要翻译： 本发明涉及一种基于烃进料选择性转化具有0至6重量％的康拉德森碳残余物的烃进料的方法。 烃进料以两步法处理。 第一种是热转化，第二种是热转化产物的催化裂化。 本发明导致用于增加用于流化催化裂化装置的烃进料流的馏出物生产的方法。 通过改变热和催化裂化步骤的条件以及通过改变裂化步骤中的催化剂，可进一步改变本发明产生的产品板条。

    Process for flexible vacuum gas oil conversion
    6.
    发明申请
    Process for flexible vacuum gas oil conversion 有权
    柔性真空瓦斯油转化工艺

    公开(公告)号：US20100018895A1

    公开(公告)日：2010-01-28

    申请号：US12459729

    申请日：2009-07-07

    申请人： Martin L. Gorbaty ,  Bruce R. Cook ,  David T. Ferrughelli ,  Jason B. English ,  Steven S. Lowenthal

    发明人： Martin L. Gorbaty ,  Bruce R. Cook ,  David T. Ferrughelli ,  Jason B. English ,  Steven S. Lowenthal

    IPC分类号： C10G69/04 ,  C10G47/00

    CPC分类号： C10G69/06 ,  C10G11/18 ,  C10G51/04 ,  C10G69/02 ,  C10G69/04 ,  C10G2300/1074 ,  C10G2300/4081 ,  C10G2400/02

    摘要： The present invention relates to a process for the selective conversion of hydrocarbon feed having a Conradson Carbon Residue content of 0 to 6 wt %, based on the hydrocarbon feed. The hydrocarbon feed is treated in a two-step process. The first is thermal conversion and the second is catalytic cracking of the products of the thermal conversion. The present invention results in a process for increasing the distillate production from a hydrocarbon feedstream for a fluid catalytic cracking unit. The resulting product slate from the present invention can be further varied by changing the conditions in the thermal and catalytic cracking steps as well as by changing the catalyst in the cracking step.

    摘要翻译： 本发明涉及一种基于烃进料选择性转化具有0至6重量％的康拉德森碳残余物的烃进料的方法。 烃进料以两步法处理。 第一种是热转化，第二种是热转化产物的催化裂化。 本发明导致用于增加用于流化催化裂化装置的烃进料流的馏出物生产的方法。 通过改变热和催化裂化步骤的条件以及通过改变裂化步骤中的催化剂，可进一步改变本发明产生的产品板条。

    REMOVAL OF NITROGEN COMPOUNDS FROM FCC DISTILLATE
    8.
    发明申请
    REMOVAL OF NITROGEN COMPOUNDS FROM FCC DISTILLATE 有权
    从FCC馏分中除去硝酸化合物

    公开(公告)号：US20110132806A1

    公开(公告)日：2011-06-09

    申请号：US12908091

    申请日：2010-10-20

    申请人： Stacey E. Siporin ,  David Thomas Ferrughelli ,  Steven S. Lowenthal ,  Randolph J. Smiley ,  Alan Roy Katritzky ,  Bruce R. Cook

    发明人： Stacey E. Siporin ,  David Thomas Ferrughelli ,  Steven S. Lowenthal ,  Randolph J. Smiley ,  Alan Roy Katritzky ,  Bruce R. Cook

    IPC分类号： C10G67/00 ,  C10G29/20

    CPC分类号： C10G11/18 ,  C10G21/16 ,  C10G29/24 ,  C10G45/02 ,  C10G67/00 ,  C10G69/12

    摘要： A method for the removal of nitrogen compounds from FCC feed or from catalytically cracked distillates including FCC cycle oils by using formaldehyde to selectively couple organic heterocyclic nitrogen species in the FCC feed or FCC distillate to form higher boiling coupling products out of the boiling range of FCC distillate. Removal of the nitrogenous compounds improves the operation of subsequent hydrodesulfurization steps needed for the distillate fraction to conform to low sulfur standards. The formaldehyde is preferably used in the form of paraformaldehyde. The reaction between the nitrogenous compounds in the cycle oil fraction with the formaldehyde is conveniently carried out in the cycle oil pumparound circuit of the FCC main column.

    摘要翻译： 一种从FCC原料或催化裂化的馏出物（包括FCC循环油）中除去氮化合物的方法，其中使用甲醛选择性地将有机杂环氮物质在FCC进料或FCC馏出物中偶联，以在沸点范围内形成较高沸点的偶联产物 馏出物 去除含氮化合物改善了馏出物馏分所需的随后加氢脱硫步骤的操作以符合低硫标准。 甲醛优选以多聚甲醛的形式使用。 循环油馏分中的含氮化合物与甲醛的反应在FCC主塔的循环油循环回路中方便地进行。