Cyclone system for disengaging solid and gaseous particles in FCC systems with reduced coke formation in disengager vessels
    13.
    发明授权
    Cyclone system for disengaging solid and gaseous particles in FCC systems with reduced coke formation in disengager vessels 有权
    用于在FCC系统中脱离固体和气体颗粒的旋风系统,其中分离容器中的焦炭形成减少

    公开(公告)号:US07332133B2

    公开(公告)日:2008-02-19

    申请号:US10814641

    申请日:2004-04-01

    IPC分类号: B32B5/02 B01D19/00

    摘要: An improved cyclone system for disengaging solid and gaseous particles in fluid catalytic cracking (FCC) processes with reduced coke formation in disengager vessels, without favoring release of the disengaged catalyst into cyclones in subsequent stages, said system comprising legless cyclones 42 fitted with external collector pipes 43, is described.The collector pipes 43 optimize the purge of gases coming from the disengager vessel 49, reducing the time the hydrocarbons remain inside said disengager vessel 49, thus preventing overcracking and subsequent coke formation. Positioning of the external collector pipes 43 prevents release of the disengaged catalyst into cyclones in subsequent stages.The present invention also relates to a process and device for disengaging solid and gaseous particles in fluid catalytic cracking (FCC) processes, reducing coke formation in disengager vessels and minimizing the release of catalyst into consecutive stages, said process and device being part of the system of the present invention.

    摘要翻译: 一种改进的旋风系统,用于在流化催化裂化(FCC)方法中分离固体和气体颗粒,在脱离容器中具有减少的焦炭形成,而不利于在随后的阶段中将分离的催化剂释放到旋风分离器中,所述系统包括装配有外部收集器管的无腿旋风分离器42 描述了图43。 收集器管道43优化来自脱离容器49的气体的吹扫,减少了碳氢化合物保留在分离容器49内的时间,从而防止过度裂化和随后的焦炭形成。 外部收集器管43的定位防止脱离的催化剂在随后的阶段中释放到旋风分离器中。 本发明还涉及用于在流化催化裂化(FCC)方法中脱离固体和气体颗粒的方法和装置,减少分离容器中的焦炭形成并最小化催化剂释放到连续阶段,所述方法和装置是系统的一部分 的本发明。

    Process for disengaging solid and gaseous particles in FCC processes with reduced coke formation in disengager vessels
    15.
    发明授权
    Process for disengaging solid and gaseous particles in FCC processes with reduced coke formation in disengager vessels 有权
    在FCC工艺中脱离固体和气体颗粒的方法,其中分离容器中的焦炭形成减少

    公开(公告)号:US07867321B2

    公开(公告)日:2011-01-11

    申请号:US11955920

    申请日:2007-12-13

    IPC分类号: B01D53/12

    CPC分类号: C10G11/18

    摘要: An improved cyclone system for disengaging solid and gaseous particles in fluid catalytic cracking (FCC) processes with reduced coke formation in disengager vessels, without favoring release of the disengaged catalyst into cyclones in subsequent stages, said system comprising legless cyclones 42 fitted with external collector pipes 43, is described. The collector pipes 43 optimize the purge of gases coming from the disengager vessel 49, reducing the time the hydrocarbons remain inside the disengager vessel 49, thus preventing overcracking and subsequent coke formation. Positioning of the external collector pipes 43 prevents release of the disengaged catalyst into cyclones in subsequent stages. The present invention also relates to a process and device for disengaging solid and gaseous particles in fluid catalytic cracking (FCC) processes, reducing coke formation in disengager vessels and minimizing the release of catalyst into consecutive stages, said process and device being part of the system of the present invention.

    摘要翻译: 一种改进的旋风系统,用于在流化催化裂化(FCC)方法中分离固体和气体颗粒,在脱离容器中具有减少的焦炭形成,而不利于在随后的阶段中将分离的催化剂释放到旋风分离器中,所述系统包括装配有外部收集器管的无腿旋风分离器42 描述了图43。 收集管43优化来自脱离容器49的气体的吹扫,减少了烃在分离容器49内的保留时间,从而防止过度裂化和随后的焦炭形成。 外部收集器管43的定位防止脱离的催化剂在随后的阶段中释放到旋风分离器中。 本发明还涉及用于在流化催化裂化(FCC)方法中脱离固体和气体颗粒的方法和装置,减少分离容器中的焦炭形成并最小化催化剂释放到连续阶段,所述方法和装置是系统的一部分 的本发明。

    Multifunctional entry device for a downward flow tube reactor
    16.
    发明授权
    Multifunctional entry device for a downward flow tube reactor 有权
    用于向下流动管式反应器的多功能进入装置

    公开(公告)号:US07531142B2

    公开(公告)日:2009-05-12

    申请号:US11512216

    申请日:2006-08-30

    IPC分类号: B01J8/18

    摘要: A device and a method for operating it for application in a vertical tube reactor with downward flow (downer), has the aim of ensuring the intimate mixing of the solid particulate catalyst with a reagent fluid. Homogeneous distribution of catalyst is due to the use of a plate having perforations. Said perforated plate normally allows the passage of a portion of the stream of catalyst. The other portion overflows the edge of the plate, flowing in the form of an annular curtain, near the inner surface of the surrounding tube of the device. After passing beyond the perforated plate, the curtain-flow undergoes a deflection produced by an annular screen, to be mixed with the stream originating from the orifices in the perforated plate. A hydrocarbon charge is injected below the perforated plate, forming a certain angle with respect to the direction of the downward flow of catalyst, by means of inlets distributed uniformly about cross sections of the surrounding tube. After the mixing region, the diameter of the device, when smaller than the diameter of the associated tube reactor, expands slightly.

    摘要翻译: 一种用于在具有向下流动(垂直)的竖管式反应器中运行的装置和方法,其目的是确保固体颗粒催化剂与试剂流体的紧密混合。 催化剂的均匀分布是由于使用具有穿孔的板。 所述多孔板通常允许催化剂流的一部分通过。 另一部分溢出板的边缘,以环形窗的形式在设备的周围管的内表面附近流动。 在穿过多孔板之后,窗帘流经由环形筛网产生的挠曲,以与来自多孔板的孔口的流混合。 通过在周围管的横截面均匀分布的入口,在多孔板下方注入碳氢化合物,相对于催化剂向下流动的方向形成一定角度。 在混合区域之后,当小于相关管式反应器的直径时,装置的直径稍微扩大。

    Second stage cyclone dipleg termination device in FCC units
    17.
    发明授权
    Second stage cyclone dipleg termination device in FCC units 有权
    FCC单元中第二级旋风式双向终止装置

    公开(公告)号:US07081229B2

    公开(公告)日:2006-07-25

    申请号:US10413223

    申请日:2003-04-15

    IPC分类号: B32B5/02

    摘要: A second stage cyclone dipleg termination device for cyclones that operate under conditions in which the pressure in the top of the cyclone dipleg is lower than the external pressure where fine particulate matter is collected and discharged. The second stage cyclone dipleg termination device operates in a separator vessel (2) or a vessel of the regenerator of a fluid catalytic cracking (FCC) converter to reverse the pressure conditions commonly found in this type of equipment. One end of a cyclone dipleg (7) is joined to a collector vessel (11), in such a way that a portion of the dipleg (7) enters into the inside of the collector vessel (11). The end of the dipleg (7) is connected to the conventional, normally used sealing device (17) in second stage cyclone (4) diplegs (7). The collector vessel (11), in turn, has on its bottom an outlet in the form of the dipleg (14). On the inside of this outlet an injector device is introduced (16) through which a fluid under high pressure is discharged, associated with a “venturi” type nozzle (15), which moves or drags the particulate matter discharged by the dipleg (7) of the cyclone (4) through the sealing valves (17), inside the collector vessel (11) the exterior of the collector vessel (11).

    摘要翻译: 在旋风分离器顶部的压力低于收集和排出细颗粒物质的外部压力的条件下操作的旋风分离器的第二级旋风二通直流终止装置。 第二级旋风二通终止装置在分离器容器(2)或流化催化裂化(FCC)转化器的再生器的容器中操作,以逆转在这种类型的设备中通常发现的压力条件。 旋流器(3)的一端与收集器容器(11)接合,使得一部分水滴(7)进入收集容器(11)的内部。 三通(7)的末端连接到第二级旋风分离器(4)脚管(7)中常规的通常使用的密封装置(17)。 收集器容器(11)又在其底部具有呈径形(14)形式的出口。 在该出口的内侧,引入喷射器装置(16),高压流体通过该喷射器装置排出,与“文氏管”型喷嘴(15)相关联,喷嘴(15)移动或拖动由径向(7)排出的颗粒物质, 的旋风器(4)通过密封阀(17)在收集器容器(11)内部的收集器容器(11)的外部。