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    Combined thermal and catalytic treatment of heavy petroleum in a slurry phase counterflow reactor
    31.
    发明申请
    Combined thermal and catalytic treatment of heavy petroleum in a slurry phase counterflow reactor 有权
    在淤浆相逆流反应器中对重石油进行联合热处理和催化处理

    公开(公告)号：US20020166797A1

    公开(公告)日：2002-11-14

    申请号：US09852107

    申请日：2001-05-09

    Inventor： Dwijen K. Banerjee

    IPC: C10G057/00

    CPC classification number: C10G65/10 ,  B01J8/0035 ,  B01J8/22 ,  B01J8/228 ,  B01J2208/00256 ,  B01J2208/00274 ,  B01J2208/00283 ,  B01J2208/00539 ,  B01J2208/0061 ,  B01J2208/0084 ,  C10G47/22

    Abstract: A slurry phase reactor is designed to treat extra heavy petroleum crude in a combination of thermal-zone and catalytic-zone in a counterflow system where liquid feed is added to the top and hydrogen at the bottom. Feed enters the gas-phase thermal zone, where it passes to a liquid-phase thermal zone. In the liquid-phase thermal zone, the hydrocarbon is thermally cracked and the unreacted liquid is further passed to a catalytic-zone below in communication with the thermal-zone. Catalyst can be added or removed as required in a continuous mode without shutting down the system. The heat generated inside the catalytic cracking zone is distributed to the entire reactor as the gaseous product flows upward. Feed is brought to the reaction conditions by the heat recovered from the gas-phase zone. Reaction temperature could be controlled by feed temperature.

    Abstract translation: 浆料相反应器被设计成在反向流动系统中处理热区域和催化区域的组合中的额外重质石油原油，其中液体进料添加到顶部，底部加氢。 进料进入气相热区，在那里它进入液相热区。 在液相热区中，烃被热裂化，并且未反应的液体进一步传递到与热区连通的下游催化区。 可以根据需要在连续模式下添加或除去催化剂，而无需关闭系统。 当气体产物向上流动时，催化裂化区内产生的热分布到整个反应器中。 通过从气相区回收的热量将进料送入反应条件。 反应温度可以通过进料温度控制。

    Catalytic hydrogenation process
    35.
    发明授权
    Catalytic hydrogenation process 失效
    催化加氢工艺

    公开(公告)号：US5093535A

    公开(公告)日：1992-03-03

    申请号：US476453

    申请日：1990-06-04

    Applicant: George E. Harrison ,  Alan J. Dennis

    Inventor： George E. Harrison ,  Alan J. Dennis

    IPC: B01J8/02 ,  C07B31/00 ,  C07B61/00 ,  C07C5/10 ,  C07C13/18 ,  C07C29/14 ,  C07C29/141 ,  C07C31/125

    CPC classification number: B01J8/02 ,  C07C29/141 ,  B01J2208/00061 ,  B01J2208/00141 ,  B01J2208/00212 ,  B01J2208/00256 ,  B01J2208/00495 ,  B01J2208/0053 ,  B01J2208/00539 ,  B01J2208/00548 ,  B01J2208/0061

    Abstract: A liquid phase catalytic hydrogenation process is described in which an organic feedstock, such as an aldehyde containing from 2 to about 20 carbon atoms, is contracted with hydrogen in the presence of a solid hydrogenation catalyst under hydrogenation conditions to produce a hydrogenation product, such as the corresponding alcohol containing from 2 to about 20 carbon atoms, which process comprises passing a feed solution of the organic feedstock in an inert diluent therefor downwardly in co-current with a hydrogen-containing gas through a hydrogenation zone containing a bed of a particulate hydrogenation catalyst whose particles substantially all lie in the range of from about 1.5 mm to about 5 mm, maintaining the bed of catalyst particles under temperature and pressure conditions conducive to hydrogenation, recovering from a bottom part of the bed a liquid phase containing the hydrogenation product, controlling the rate of supply of the feed solution to the bed so as to maintain a superficial liquid velocity of the liquid down the bed in the range of from about 1.5 cm/sec to about 5 cm/sec, and controlling the rate of supply of the hydrogen-containing gas to the bed so as to maintain at the top surface of the bed of catalyst particles a flow of hydrogen-containing gas containing from 1.00 to about 1.15 times the stoichiometric quantity of hydrogen theoretically necessary to convert the organic feedstock completely to the hydrogenation product.

    Fluidized bed apparatus for the treatment of fluidized carbon black with gases
    36.
    发明授权
    Fluidized bed apparatus for the treatment of fluidized carbon black with gases 失效
    用于用气体处理流化炭黑的流化床装置

    公开(公告)号：US4755358A

    公开(公告)日：1988-07-05

    申请号：US818590

    申请日：1986-01-14

    Applicant: Manfred Voll ,  Richard Engel

    Inventor： Manfred Voll ,  Richard Engel

    IPC: C09C1/00 ,  B01J8/24 ,  C09C1/56 ,  C09C1/58 ,  B01J8/18 ,  C09C1/48

    CPC classification number: B01J8/1809 ,  C09C1/56 ,  B01J2208/0061 ,  C01P2006/80

    Abstract: Method for the treatment of fluidized carbon black with gases in a fluidized bed, wherein the carbon black and the treatment gases are conveyed for introduction in an unique operating procedure into the treating region in a countercurrent stream manner. The mass streams of the carbon black and the treating gases are held constant and the mass streams of the starting carbon black or the treated carbon black is regulated with the help of an optical electrical level sensor so that the height of the fluidized bed is held on a predetermined level. An apparatus is shown for the carrying out of the fluidized bed countercurrent process which has a novel carbon black product delivery system and is provided with a optical electrical level sensor means for controlling the level of the fluidized bed. The sensor comprises a hair pin shaped lighting circuit composed of two legs or rods separated by a gap. A light source impinges on the end of one of the said legs and the other leg is oriented to an electrical signal generating light sensor.

    Abstract translation: 在流化床中用气体处理流化炭黑的方法，其中将炭黑和处理气体以独特的操作程序输送，以逆流方式进入处理区域。 炭黑和处理气体的质量流保持恒定，并且通过光学电平传感器调节起始炭黑或处理过的炭黑的质量流，使得流化床的高度保持在 一个预定的水平。 示出了用于实施具有新型炭黑产品输送系统的流化床逆流方法的装置，并且设置有用于控制流化床水平的光学电平传感器装置。 该传感器包括由间隙分开的两个腿或杆组成的发针状照明电路。 光源撞击在所述腿中的一个的末端，而另一个腿被定向到产生光传感器的电信号。

    Fixed bed catalytic reactor system with improved liquid distribution
    37.
    发明授权
    Fixed bed catalytic reactor system with improved liquid distribution 失效
    固定床催化反应器系统具有改善的液体分布

    公开(公告)号：US4681674A

    公开(公告)日：1987-07-21

    申请号：US795816

    申请日：1985-11-07

    Applicant: Richard G. Graven ,  John C. Zahner

    Inventor： Richard G. Graven ,  John C. Zahner

    IPC: B01J8/04 ,  B01J8/02 ,  C10G45/58 ,  C10G49/00 ,  C10G65/02

    CPC classification number: B01J8/02 ,  C10G45/58 ,  C10G49/002 ,  B01J2208/00079 ,  B01J2208/00088 ,  B01J2208/00265 ,  B01J2208/00548 ,  B01J2208/0061 ,  Y10S208/01

    Abstract: A continuous process and system is provided for a petroleum oil in a multi-phase fixed bed catalytic reactor column comprising methods and means for:feeding the oil and a reactant gas at production flow rates above a first bed of porous solid catalyst particles under conversion conditions for cocurrent downward flow therethrough, collecting and withdrawing the treated oil from the first bed and redistributing at least a portion of the treated oil to at least one succeeding catalyst bed while permitting the gaseous phase to flow directly to the succeeding lower catalyst bed, recycling a quantity of treated oil collected below a catalyst bed and reapplying the treated oil at a preceding redistribution zone above the bed from which treated oil is collected, whereby the total of oil production flow rate and recycled treated oil flow rate is maintained at a predetermined minimum sufficient to effect uniform catalyst wetting. This technique is useful for hydrodewaxing of oils over zeolite catalysts.

    Abstract translation: 在多相固定床催化反应器塔中为石油提供连续的方法和系统，其包括以下方法和装置：在转化条件下，以多孔固体催化剂颗粒的第一床上方的生产流速输入油和反应气体 从而从第一床收集和取出经处理的油并将至少一部分经处理的油重新分配至至少一个后续催化剂床，同时允许气相直接流到后续的下层催化剂床，循环利用 在催化剂床下面收集的处理油的量，并在处理油被收集的床上方的先前再分配区上重新施加处理的油，由此将总产生的油生产流量和循环处理的油的流速保持在预定的最小值 以实现均匀的催化剂润湿。 该技术可用于油在沸石催化剂上的加氢脱蜡。

    Level control for a fluidized bed
    38.
    发明授权
    Level control for a fluidized bed 失效
    流化床的液位控制

    公开(公告)号：US4546012A

    公开(公告)日：1985-10-08

    申请号：US604028

    申请日：1984-04-26

    Applicant: Lionel H. Brooks

    Inventor： Lionel H. Brooks

    IPC: C01B31/04 ,  B01J2/16 ,  B01J8/24 ,  B05C19/02 ,  B05D1/22 ,  B05D7/24 ,  B05D7/00

    CPC classification number: B01J8/1809 ,  B05C19/02 ,  B05D1/22 ,  B05D7/24 ,  B01J2208/00407 ,  B01J2208/00548 ,  B01J2208/0061 ,  Y10S118/05

    Abstract: Fluidized bed apparatus for use in applying a coating, having a relatively lesser density, to particles, having relatively greater densities by causing passage of a gaseous atmosphere through a bed of the particles. The apparatus includes an enclosure holding a bed of the particles and means for causing flowing of the gaseous atmosphere carrying a material for forming the coating through the bed of particles to be fluidized. The apparatus further includes means for adding seed particles to the bed and weir tube means removing coated particles from the bed when the contents of the bed achieves a predetermined level. Finally, the apparatus includes discharge means receiving the coated particles from the tube means and conveying them to a collection location remote from the enclosure.

    Abstract translation: 用于通过使气态气体通过颗粒床而将具有相对较小密度的涂层施加到具有相对较大密度的颗粒的流化床装置。 该装置包括容纳颗粒床的外壳和用于使携带用于形成涂层的材料的气态气体流过要流化的颗粒床的装置。 该装置还包括用于将种子颗粒添加到床中的装置，并且堰管意味着当床的内容物达到预定水平时从床上去除涂覆的颗粒。 最后，该装置包括从管装置接收涂覆的颗粒并将其输送到远离外壳的收集位置的排放装置。

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