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29 条记录 (耗时 0.018 秒)

    Catalytic reforming process
    1.
    发明授权
    Catalytic reforming process 失效
    催化重整过程

    公开(公告)号：US06610196B1

    公开(公告)日：2003-08-26

    申请号：US09667482

    申请日：2000-09-22

    申请人： Fan-Nan Lin ,  John S. Parsons

    发明人： Fan-Nan Lin ,  John S. Parsons

    IPC分类号： C10G35085

    CPC分类号： B01J23/6567 ,  B01J23/90 ,  C10G35/04 ,  C10G35/085 ,  C10G35/09

    摘要： A substantially water-free hydrocarbon feed is charged to a reformer reactor operated under reforming conditions; thereafter, a chlorine-containing additive is introduced, without the simultaneous introduction of water, into the substantially water-free hydrocarbon feed being charged to the reformer reactor in an amount and for a time period that are effective to inhibit deactivation of the reformer catalyst; thereafter, the introduction of the chlorine-containing additive is terminated and the charging of the substantially water-free hydrocarbon feed to the reformer reactor is continued.

    摘要翻译： 将基本上无水的烃进料加入到在重整条件下操作的重整器反应器中; 然后，将不含同时引入水的含氯添加剂以有效抑制重整器催化剂失活的量和一段时间内引入到重整器反应器中的基本上不含水的烃进料中; 此后，终止含氯添加剂的引入，继续向重整器反应器充入基本上不含水的烃进料。

    Catalytic reforming catalyst activation
    2.
    发明授权
    Catalytic reforming catalyst activation 有权

    公开(公告)号：US06410472B1

    公开(公告)日：2002-06-25

    申请号：US09919453

    申请日：2001-07-31

    申请人： Donald H. Macahan ,  Fan-Nan Lin

    发明人： Donald H. Macahan ,  Fan-Nan Lin

    IPC分类号： B01J2034

    摘要： Catalyst activation of a platinum reforming catalyst system contained in a multiple reactor system by simultaneously reducing the catalyst with a sustained hydrogen flow through the multiple reactor system while introducing a nonmetallic chlorine-containing compound serially into each reactor of the multiple reactor system in an amount to add from about 0.05 to about 0.3 weight percent chlorine to the catalyst and thereafter purging the system with about 100 to about 50,000 cubic feet of hydrogen per cubic foot of catalyst prior to commencing use of the treated catalyst system for reforming hydrocarbon feed.

    Catalyst life prediction in hydrodesulfurization
    6.
    发明授权
    Catalyst life prediction in hydrodesulfurization 失效
    加氢脱硫催化剂寿命预测

    公开(公告)号：US5341313A

    公开(公告)日：1994-08-23

    申请号：US924138

    申请日：1992-08-03

    申请人： Stephen L. Parrott ,  Raul Adarme ,  Fan-Nan Lin ,  Edwin P. Sasscer

    发明人： Stephen L. Parrott ,  Raul Adarme ,  Fan-Nan Lin ,  Edwin P. Sasscer

    IPC分类号： C10G45/72 ,  G06F17/50 ,  G06G7/58

    CPC分类号： C10G45/72 ,  G06F17/50 ,  G06F2217/16

    摘要： Catalyst life in desulfurization of distillate hydrocarbon streams is predicted with the aid of a computer simulation which embodies an analytical kinetic model of a hydrodesulfurization reaction and a semi-empirical model for catalyst deactivation. The simulation specifies the decline of catalyst activity with time and a current reaction temperature required to maintain the initial catalyst activity. The useful life of the catalyst is considered to be the time required for catalyst activity in the simulated reaction to decline sufficiently from its initial level so that a predefined maximum reaction temperature is reached while maintaining a desired level of sulfur in the desulfurized product. The computer time needed to simulate the reaction is decreased by combining superior features of LOTUS 1-2-3 and FORTRAN language, such that input/output and graphic operations are implemented with LOTUS 1-2-3 and numerical calculations are executed in FORTRAN.

    摘要翻译： 借助于体现加氢脱硫反应的分析动力学模型和催化剂失活的半经验模型的计算机模拟预测了馏出物烃流脱硫的催化剂寿命。 该模拟规定了催化剂活性随时间的下降以及维持初始催化剂活性所需的当前反应温度。 催化剂的使用寿命被认为是模拟反应中的催化剂活性从其初始水平充分降低所需的时间，从而达到预定的最大反应温度，同时在脱硫产物中保持所需水平的硫。 通过结合LOTUS 1-2-3和FORTRAN语言的优越特性，可以减少模拟反应的计算机时间，从而使用LOTUS 1-2-3实现输入/输出和图形操作，并在FORTRAN中执行数值计算。

    Alcohol synthesis
    7.
    发明授权
    Alcohol synthesis 失效
    酒精合成

    公开(公告)号：US4537909A

    公开(公告)日：1985-08-27

    申请号：US584374

    申请日：1984-02-28

    申请人： Fan-Nan Lin ,  Filippo Pennella

    发明人： Fan-Nan Lin ,  Filippo Pennella

    IPC分类号： C07C29/158 ,  C07C27/06 ,  C07C29/15

    CPC分类号： C07C29/158 ,  C12C11/02 ,  Y02P20/52

    摘要： The preparation of alcohols from synthesis gas has been beneficiated by the use of a novel five-component catalyst system comprising an iron group metal and an activity improving amount of a precious metal such as rhodium.

    摘要翻译： 通过使用包含铁族金属和活性提高量的贵金属如铑的新型五组分催化剂体系，已经从合成气中制备醇。

    Catalytic reforming catalyst activation
    8.
    发明授权
    Catalytic reforming catalyst activation 失效

    公开(公告)号：US06593264B2

    公开(公告)日：2003-07-15

    申请号：US10175922

    申请日：2002-06-20

    申请人： Fan-Nan Lin ,  John S. Parsons ,  Donald H. Macahan ,  Brian H. Limoges

    发明人： Fan-Nan Lin ,  John S. Parsons ,  Donald H. Macahan ,  Brian H. Limoges

    IPC分类号： B01J3842

    CPC分类号： B01J37/22 ,  B01J23/62 ,  B01J23/6567 ,  C10G35/06 ,  C10G35/09

    摘要： A reforming catalyst containing a Group VIII metal, or a Group VII B metal, or tin, or germanium, or copper, or selenium or combinations of any two or more metals or oxides thereof is activated by: a) continuously flowing a reducing gas over the catalyst for contact with the catalyst; (b) during step a), flowing a halogen-containing compound over the catalyst for contact with the catalyst for a first time period, wherein the first time period is greater than about 1 minute, and wherein the first time period is less than about 60 minutes; and (c) following step b), and during step a), substantially discontinuing the flow of the halogen-containing compound over the catalyst for a second time period, wherein the second time period is greater than about 1 minute. Alternatively, the catalyst can be activated in an activation zone by: 1) removing water from the activation zone; 2) reducing iron oxide contained in the activation zone in the presence of a reducing gas thereby forming reduced iron and water; 3) removing water from the activation zone; 4) reducing the metal oxide of the catalyst in the presence of a reducing gas thereby forming reduced metal and water; 5) removing water from the activation zone; 6) during step 4), flowing a halogen-containing compound over the catalyst for contact with the catalyst for a first time period; and 7) following step 6) and during step 4), substantially discontinuing the flow of halogen-containing compound over the catalyst for a second time period.

    Two-stage isomerization of saturated C6 hydrocarbons
    9.
    发明授权
    Two-stage isomerization of saturated C6 hydrocarbons 有权
    饱和C 6烃的两阶段异构化

    公开(公告)号：US06503465B1

    公开(公告)日：2003-01-07

    申请号：US09564495

    申请日：2000-05-04

    申请人： Fan-nan Lin ,  Edgar Durand Davis

    发明人： Fan-nan Lin ,  Edgar Durand Davis

    IPC分类号： B01J804

    CPC分类号： C07C13/18 ,  C07C5/2246 ,  C07C5/226 ,  C07C5/2791 ,  C07C9/15 ,  C07C9/16 ,  C07C2521/04 ,  C07C2523/42 ,  C07C2527/10 ,  C07C2601/14 ,  C07C9/14

    摘要： A process and/or system is provided for isomerizing a hydrocarbon feedstock comprising saturated C6 hydrocarbons by contacting the hydrocarbon feedstock, in the presence of hydrogen and optionally a chloride, with a first isomerization catalyst composition in a first isomerization reactor defining a first reaction zone operated at a first reaction temperature, withdrawing a first intermediate stream comprising cyclohexane and n-hexane from the first reaction zone, separating the first intermediate stream, via a first separator, into a first product stream comprising cyclohexane and a second intermediate stream comprising n-hexane, contacting the second intermediate stream, in the presence of hydrogen and optionally a chloride, with a second isomerization catalyst composition in a second isomerization reactor defining a second reaction zone operated at a second reaction temperature greater than the first reaction temperature, and withdrawing from the second reaction zone a second product stream comprising isohexane.

    摘要翻译： 提供了一种方法和/或系统，用于使包含饱和C 6烃的烃原料异构化，所述烃原料在氢气和任选的氯化物的存在下与第一异构化催化剂组合物在第一异构化反应器中接触，所述第一异构化反应器限定第一反应区域的操作 在第一反应温度下，从第一反应区取出包含环己烷和正己烷的第一中间物流，通过第一分离器将第一中间物流分离成包含环己烷的第一产物流和包含正己烷的第二中间物流 在第二异构化反应器的第二异构化反应器中，在氢和任选的氯化物的存在下，将第二中间物流与第二异构化催化剂组合物接触，限定在大于第一反应温度的第二反应温度下操作的第二反应区， 第二反应区第二产物 t流包含异己烷。

    Catalytic reforming catalyst activation
    10.
    发明授权
    Catalytic reforming catalyst activation 失效
    催化重整催化剂活化

    公开(公告)号：US06472340B2

    公开(公告)日：2002-10-29

    申请号：US09918950

    申请日：2001-07-31

    申请人： Fan-Nan Lin

    发明人： Fan-Nan Lin

    IPC分类号： B01J2034

    CPC分类号： C10G35/09 ,  B01J23/42 ,  B01J37/18 ,  B01J37/24 ,  B01J38/18 ,  B01J38/20 ,  B01J38/42 ,  C10G35/085

    摘要： Catalyst activation of a platinum reforming catalyst system contained in a multiple reactor system by simultaneously reducing the catalyst with hydrogen while introducing a nonmetallic chlorine-containing compound into a reactor of the multiple reactor system in an amount to add from about 0.05 to about 0.3 weight percent chlorine to the catalyst and thereafter purging the system with about 100 to about 50,000 cubic feet of hydrogen per cubic foot of catalyst resulting in a reforming system having increased activity and providing enhanced RON values with reduced cracking of feedstock.

    摘要翻译： 通过在氢气中同时还原催化剂同时将非金属含氯化合物引入多反应器系统的反应器中，催化剂活化多重反应器体系中所含的铂重整催化剂体系，其量为约0.05至约0.3重量％ 氯，然后用约100至约50,000立方英尺的氢气每立方英尺催化剂吹扫系统，导致重整体系具有增加的活性并提供增强的RON值，减少原料开裂。