利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

14 条记录 (耗时 0.015 秒)

    FCC spent catalyst distributor
    2.
    发明授权
    FCC spent catalyst distributor 失效
    FCC废催化剂分配器

    公开(公告)号：US07368090B2

    公开(公告)日：2008-05-06

    申请号：US10925481

    申请日：2004-08-25

    申请人： Daniel N. Myers ,  Mikhail Tretyak ,  Rusty M. Pittman ,  Steven Niewiedzial

    发明人： Daniel N. Myers ,  Mikhail Tretyak ,  Rusty M. Pittman ,  Steven Niewiedzial

    IPC分类号： B01J8/18 ,  B01J23/90 ,  B32B5/02 ,  C10G11/00 ,  C10G11/02

    CPC分类号： C10G11/182 ,  B01J38/30

    摘要： An distributor arrangement introduces spent FCC catalyst more uniformly across the dense bed of the regenerator to provide more even contact with regeneration gas in order to avoid hot spots and zones of incomplete combustion. The invention forms a fluidized hopper to collect spent catalyst and a horizontally extended header with multiple horizontally extended outlet arms to place catalyst into the regenerator. The invention may use an aeration means to fluidize the header to further assist catalyst flow. Furthermore, the spent catalyst delivered to the top of the regenerator dense reduces NOx emissions in the flue gas.

    摘要翻译： 分销商安排将废FCC催化剂更均匀地引入再生器的致密床，以提供与再生气体更均匀的接触，以避免热点和不完全燃烧的区域。 本发明形成流化料斗以收集废催化剂和具有多个水平延伸的出口臂的水平延伸的集管，以将催化剂置于再生器中。 本发明可以使用曝气装置来使集管流化以进一步辅助催化剂流动。 此外，输送到再生器顶部的废催化剂致密地减少烟道气中的NO x排放。

    PROCESS FOR UPGRADING FCC PRODUCT WITH ADDITIONAL REACTOR WITH CATALYST RECYCLE
    4.
    发明申请
    PROCESS FOR UPGRADING FCC PRODUCT WITH ADDITIONAL REACTOR WITH CATALYST RECYCLE 有权
    使用催化回收将附加反应器升级成FCC产品的方法

    公开(公告)号：US20110155634A1

    公开(公告)日：2011-06-30

    申请号：US13041984

    申请日：2011-03-07

    申请人： David A. Lomas ,  Rusty M. Pittman

    发明人： David A. Lomas ,  Rusty M. Pittman

    IPC分类号： C10G57/00

    CPC分类号： C10G11/18 ,  B01J8/0055 ,  B01J8/26 ,  B01J8/386 ,  B01J8/388 ,  B01J2208/00327 ,  C10G11/182 ,  C10G51/026 ,  C10G51/06

    摘要： A process is disclosed for contacting feed with mixed catalyst in a secondary reactor that is incorporated into an FCC reactor. The mixed catalyst used in the secondary reactor is regenerated catalyst from a regenerator that regenerates spent catalyst from an FCC reactor that is mixed with spent catalyst from either the FCC reactor or the secondary reactor. The mixing of spent and regenerated catalyst reduces the catalyst temperature and tempers catalyst activity to inhibit both thermal and catalytic cracking reactions.

    摘要翻译： 公开了一种将掺入到FCC反应器中的二次反应器中的进料与混合催化剂接触的方法。 在二次反应器中使用的混合催化剂是再生催化剂，该再生器从与FCC反应器或二次反应器的废催化剂混合的FCC反应器再生废催化剂。 废再生催化剂的混合降低催化剂温度和缓解催化剂活性，以抑制热和催化裂化反应。

    FCC process with improved yield of light olefins
    5.
    发明授权
    FCC process with improved yield of light olefins 有权
    FCC工艺，提高了轻质烯烃的产率

    公开(公告)号：US07312370B2

    公开(公告)日：2007-12-25

    申请号：US10316222

    申请日：2002-12-10

    申请人： Rusty M. Pittman ,  Lawrence L. Upson

    发明人： Rusty M. Pittman ,  Lawrence L. Upson

    IPC分类号： C07C4/06 ,  C10G11/02

    CPC分类号： C07C4/06 ,  C10G11/05 ,  C10G11/18

    摘要： An FCC process for obtaining light olefins comprises contacting a hydrocarbon feed stream with blended catalyst comprising regenerated catalyst and coked catalyst. The catalyst has a composition including a first component and a second component. The second component comprises a zeolite with no greater than medium pore size wherein the zeolite comprises at least 1 wt-% of the catalyst composition. The contacting occurs in a riser to crack hydrocarbons in the feed stream and obtain a cracked stream containing hydrocarbon products including light olefins and coked catalyst. The cracked stream is passed out of an end of the riser such that the hydrocarbon feed stream is in contact with the blended catalyst in the riser for less than or equal to 2 seconds on average. The hydrocarbon products including light olefins are separated from the coked catalyst. The first portion of the coked catalyst is passed to a regeneration zone in which coke is combusted from the catalyst to produce a regenerated catalyst. A second portion of the coked catalyst is blended with the regenerated catalyst and introduced to the riser. The regenerated catalyst has substantially the same relative proportions of the first component and the second component as the blended catalyst that contact the hydrocarbon feed stream.

    摘要翻译： 用于获得轻质烯烃的FCC方法包括使烃进料流与包含再生催化剂和焦化催化剂的混合催化剂接触。 催化剂具有包含第一组分和第二组分的组合物。 第二组分包括不大于中等孔径的沸石，其中沸石包含至少1重量％的催化剂组合物。 接触发生在提升管中以在进料流中裂解烃，并获得含有烃产物（包括轻质烯烃和焦化催化剂）的裂化物流。 裂化的物流从提升管的一端流出，使得烃进料流在提升管中与混合的催化剂平均接触平均小于或等于2秒。 包含轻质烯烃的烃产物与焦化催化剂分离。 焦化催化剂的第一部分被送入再生区，在该再生区中焦炭从催化剂燃烧，以产生再生催化剂。 将焦炭催化剂的第二部分与再生催化剂混合并引入提升管。 再生催化剂与第一组分和第二组分的相对比例与作为与烃进料流接触的共混催化剂基本相同。