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    DUAL RISER FLUID BED PROCESS AND REACTOR
    4.
    发明申请
    DUAL RISER FLUID BED PROCESS AND REACTOR 审中-公开
    双流体流化床和反应器

    公开(公告)号：US20160214911A1

    公开(公告)日：2016-07-28

    申请号：US15056020

    申请日：2016-02-29

    Applicant: Kellogg Brown & Root LLC

    Inventor： Curtis ENG

    IPC: C07C1/20 ,  C07C4/06

    CPC classification number: C07C1/20 ,  B01J8/0055 ,  B01J8/0065 ,  B01J8/1863 ,  B01J8/26 ,  B01J29/40 ,  B01J29/90 ,  B01J38/02 ,  B01J2208/00176 ,  B01J2219/00006 ,  C07C4/06 ,  C07C2529/40 ,  C10G3/46 ,  C10G3/49 ,  C10G11/18 ,  C10G2400/20 ,  Y02P20/52 ,  Y02P20/584 ,  Y02P20/588 ,  Y02P30/20 ,  Y02P30/42 ,  C07C11/04 ,  C07C11/06

    Abstract: Processes and systems for cracking feeds to produce olefins are provided. The process for cracking feeds can include converting a first feed containing at least about 50 wt % methanol in a first riser under a first set of process conditions to produce a first effluent enriched in ethylene, propylene, or a mixture thereof, wherein the first effluent contains at least about 25 wt % dry basis propylene and converting a second feed containing C4-C10 light hydrocarbons in a second riser under a second set of process conditions to produce a second effluent enriched in ethylene, propylene, or a mixture thereof. The process can also include combining the first effluent with the second effluent to produce a mixed effluent, separating the mixed effluent to produce a coked-catalyst and a gaseous product, regenerating the coked-catalyst, and recycling the regenerated catalyst to the first and second risers.

    Abstract translation: 提供了用于裂化原料以生产烯烃的方法和系统。 用于裂化原料的方法可以包括在第一组工艺条件下在第一提升管中转化含有至少约50重量％甲醇的第一进料，以产生富含乙烯，丙烯或其混合物的第一流出物，其中第一流出物 含有至少约25重量％的干基丙烯，并在第二组工艺条件下在第二提升管中转化含有C 4 -C 10轻烃的第二进料，以产生富含乙烯，丙烯或其混合物的第二流出物。 该方法还可以包括将第一流出物与第二流出物混合以产生混合流出物，分离混合流出物以产生焦化催化剂和气态产物，再生焦化催化剂，并将再生催化剂再循环到第一和第二 立管。

    METHOD FOR SEPARATING GAS IN A FLUIDIZED GAS/SOLID MIXTURE
    7.
    发明申请
    METHOD FOR SEPARATING GAS IN A FLUIDIZED GAS/SOLID MIXTURE 有权
    在流化气/固体混合物中分离气体的方法

    公开(公告)号：US20130186273A1

    公开(公告)日：2013-07-25

    申请号：US13812326

    申请日：2011-08-12

    Applicant: Juan-David Llamas ,  Patrick Leroy ,  Celine Derouin ,  Nicolas Lenepveu

    Inventor： Juan-David Llamas ,  Patrick Leroy ,  Celine Derouin ,  Nicolas Lenepveu

    IPC: B01D45/08

    CPC classification number: B01D45/08 ,  B01D45/12 ,  B01D45/16 ,  B01D50/002 ,  B01J8/0065 ,  F01M13/04

    Abstract: Process for separating gases from a fluidized gas/solid mixture, comprising at least one injection of gas and optionally at least one injection of solids into and at least one discharge of solids from said fluidized bed, a discharge for gas from the mixture characterized in that it comprises a step of separating the solids entrained by the gas by means of an internal placed in that portion of the fluidized mixture where the voidage is greater than 0.7, occupying less than 10% of the free cross section of the bed.

    Abstract translation: 用于从流化气体/固体混合物中分离气体的方法，包括至少一次气体注入和至少一次固体注入至少一次从所述流化床排出的固体，以及来自所述混合物的气体排放，其特征在于， 它包括通过内部放置在空隙率大于0.7的流化混合物的那部分内部分离由气体夹带的固体的步骤，其占据床的自由横截面的10％。

    FCC SEPARATOR WITHOUT A REACTOR
    8.
    发明申请
    FCC SEPARATOR WITHOUT A REACTOR 有权
    没有反应器的FCC分离器

    公开(公告)号：US20100187158A1

    公开(公告)日：2010-07-29

    申请号：US12751390

    申请日：2010-03-31

    Applicant: Kelly D. Seibert ,  Todd P. Mitchell ,  Mindy B. Kuhn

    Inventor： Kelly D. Seibert ,  Todd P. Mitchell ,  Mindy B. Kuhn

    IPC: C10G11/00

    CPC classification number: B01J8/0055 ,  B01J8/0065 ,  C10G11/182

    Abstract: This invention is directed to a process for fluid catalytic cracking, including, fluidizing a hydrocarbon stream in a riser, cracking the hydrocarbon stream with catalyst in the riser to produce a cracked stream and spent catalyst, separating the cracked stream and the spent catalyst in a primary separator to obtain a cracked stream with a first concentration of spent catalyst, and transporting the cracked stream with the first concentration of spent catalyst through a conduit to a multi-cyclone separator comprising multiple cyclones extending through a tube sheet to obtain a cracked stream with a second concentration of spent catalyst. The invention is also directed to an apparatus for catalytic cracking including a riser, a primary separator, a disengagement vessel surrounding the primary separator to collect the catalyst, a gas conduit having a first end in fluid connection with the disengagement vessel, and a multi-cyclone separator comprising a plurality of cyclones.

    Abstract translation: 本发明涉及一种用于流化催化裂化的方法，包括在提升管中流化烃流，在提升管中用催化剂裂解烃流以产生裂化物流和废催化剂，将裂化物流和废催化剂在 初级分离器以获得具有第一浓度的废催化剂的裂化流，并将具有第一浓度的废催化剂的裂化流通过导管输送到包含延伸穿过管板的多个旋风分离器的多旋风分离器，以获得具有 第二浓度的废催化剂。 本发明还涉及一种用于催化裂化的装置，包括提升管，主分离器，围绕主分离器收集催化剂的分离容器，具有与分离容器流体连通的第一端的气体导管， 旋风分离器包括多个旋风分离器。

    Catalyst regenerator for reducing entrained catalyst loss
    10.
    发明授权
    Catalyst regenerator for reducing entrained catalyst loss 失效
    用于减少夹带催化剂损失的催化剂再生器

    公开(公告)号：US07214636B2

    公开(公告)日：2007-05-08

    申请号：US10646240

    申请日：2003-08-22

    Applicant: James Harding Beech, Jr. ,  Richard E. Walter

    Inventor： James Harding Beech, Jr. ,  Richard E. Walter

    IPC: B01J20/34

    CPC classification number: B01J8/0065 ,  B01J8/0055 ,  B01J8/18 ,  B01J29/90 ,  B01J38/30 ,  B01J2208/00849 ,  C10G2400/20 ,  Y02P30/20

    Abstract: The present invention is directed to a swaged catalyst regenerator and processes for using the catalyst regenerator. In one embodiment, the swaged catalyst regenerator includes a regeneration zone having a first major diameter and into which a regeneration medium and an at least partially coked catalyst from a reactor can be fed. The catalyst regenerator also includes a separation zone having a second major diameter. The separation zone is provided to separate entrained catalyst from gaseous components, e.g., combustion products of a regeneration process, and return the entrained catalyst to the regeneration zone. The ratio of the second major diameter to the first major diameter is at least 1.1, 1.4, 1.7, 2.0, 2.3, 2.6 or 2.9. By providing a catalyst regenerator having these characteristics, desirable regeneration characteristics that minimize entrained catalyst loss can be achieved.

    Abstract translation: 本发明涉及一种模压催化剂再生器和使用该催化剂再生器的方法。 在一个实施方案中，模锻的催化剂再生器包括具有第一大直径的再生区，再生介质和来自反应器的至少部分焦化的催化剂可以进料到该再生区中。 催化剂再生器还包括具有第二大直径的分离区。 提供分离区以将夹带的催化剂与气态组分（例如再生过程的燃烧产物）分离，并将夹带的催化剂返回到再生区。 第二大直径与第一大直径的比率至少为1.1,1.4,1.7,2.0,2.3,2.6或2.9。 通过提供具有这些特性的催化剂再生器，可以实现使携带的催化剂损失最小化的期望的再生特性。

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