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49 条记录 (耗时 0.054 秒)

    Partial CO combustion with staged regeneration of catalyst
    1.
    发明授权
    Partial CO combustion with staged regeneration of catalyst 失效
    部分CO燃烧与催化剂分阶段再生

    公开(公告)号：US4849091A

    公开(公告)日：1989-07-18

    申请号：US182812

    申请日：1988-04-18

    申请人： Carlos A. Cabrera ,  Daniel N. Myers ,  Harold U. Hammershaimb

    发明人： Carlos A. Cabrera ,  Daniel N. Myers ,  Harold U. Hammershaimb

    IPC分类号： C10G11/18

    CPC分类号： C10G11/182 ,  Y10S208/01

    摘要： FCC catalyst is regenerated in a process providing increased coke-burning capacity without additional heat evolution or air consumption. The process uses a two-stage regeneration arrangement providing initial coke combustion in a low catalyst density-high efficiency contact zone followed by substantial separation of catalyst and regeneration gas and complete regeneration of catalyst particles in a dense bed regeneration zone. Catalyst and gas flow cocurrent prior to this separation but flow countercurrent after the separation. An effective control scheme for regulating oxygen addition to the final zone is also disclosed. This process is applicable to FCC operations for conventional and residual feedstocks.

    摘要翻译： FCC催化剂在提供增加的焦炭燃烧能力的过程中再生，而没有额外的放热或空气消耗。 该方法使用两级再生装置，其在低催化剂密度 - 高效率接触区域中提供初始焦炭燃烧，随后基本上分离催化剂和再生气体，并在致密床再生区中完全催化剂颗粒再生。 催化剂和气流在分离前并流，但在分离后逆流。 还公开了一种用于调节最终区域的氧气添加的有效控制方案。 该方法适用于常规和残留原料的FCC操作。

    SLURRY COLUMN GASOLINE ALKYLATION USING GAS PHASE OLEFIN INJECTION
    5.
    发明申请
    SLURRY COLUMN GASOLINE ALKYLATION USING GAS PHASE OLEFIN INJECTION 审中-公开
    使用气相烯烃注射的浆液柱汽油烷基化

    公开(公告)号：US20120230882A1

    公开(公告)日：2012-09-13

    申请号：US13480626

    申请日：2012-05-25

    申请人： Douglas A. Nafis ,  Lev Davydov ,  David N. Myers ,  Carl J. Stevens ,  Daniel N. Myers

    发明人： Douglas A. Nafis ,  Lev Davydov ,  David N. Myers ,  Carl J. Stevens ,  Daniel N. Myers

    IPC分类号： B01J8/22 ,  B01J8/00

    CPC分类号： B01J29/90 ,  B01J29/084 ,  B01J38/10 ,  B01J38/56 ,  B01J38/58 ,  C07C2/58 ,  C07C2529/08 ,  Y02P20/584 ,  C07C9/16

    摘要： Alkylation systems and processes are provided herein that include a slurry reactor. The slurry reactor receives a reactor feed slurry including catalyst and liquid isobutane, a olefin feed, and a circulating reactor vapor stream, where the slurry reactor produces a reactor liquid effluent stream, the reactor liquid effluent stream including catalyst, isobutane, and a liquid alkylate product. The catalyst in the reactor feed slurry can be regenerated catalyst from a catalyst regenerator. The catalyst can be regenerated after being removed from the liquid alkylate product and isobutane in the reactor liquid effluent stream.

    摘要翻译： 本文提供了包括淤浆反应器的烷基化系统和方法。 浆料反应器接收包括催化剂和液体异丁烷，烯烃进料和循环反应器蒸气流的反应器进料浆料，其中浆料反应器产生反应器液体流出物流，反应器液体流出物流包括催化剂，异丁烷和液体烷基化物 产品。 反应器进料浆料中的催化剂可以由催化剂再生器再生催化剂。 催化剂可以在反应器液体流出物流中从液体烷基化物产物和异丁烷中除去后再生。

    FCC spent catalyst distributor
    6.
    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。

    Distribution apparatus and method for short time contact of hydrocarbon compounds with particles
    7.
    发明授权
    Distribution apparatus and method for short time contact of hydrocarbon compounds with particles 失效
    碳氢化合物与颗粒短时间接触的分配装置和方法

    公开(公告)号：US6010620A

    公开(公告)日：2000-01-04

    申请号：US967525

    申请日：1997-11-11

    申请人： Daniel N. Myers ,  Aziz A. Sattar

    发明人： Daniel N. Myers ,  Aziz A. Sattar

    IPC分类号： B01J8/00 ,  B01J8/12 ,  B01J8/24 ,  B01J19/26 ,  C10G11/18

    CPC分类号： C10G11/18 ,  B01J19/26 ,  B01J8/005 ,  B01J8/0055 ,  B01J8/12 ,  B01J8/1827 ,  B01J2208/00495 ,  B01J2208/00539 ,  B01J2208/00548

    摘要： An arrangement for the controlled production of an essentially linear array of hydrocarbon feed injection jets maintains stable and reliable jets by passing individual piping for each jet through a support shroud that is located in a contacting vessel. Controlled atomization is provided by independently injecting a uniform quantity of gas medium into each of the plurality of uniformly created feed injection streams upstream of a discharge nozzle that separately discharges each mixed stream of hydrocarbons and gas medium into a stream of catalyst particles at or about the inner end of the support shroud. The feed injection jets are suitable for positioning in an inner location of large contacting vessel. Uniformity of distribution is obtained by dividing the hydrocarbons streams from an oil header into an individual oil conduit for each spray injection nozzle. The individual oil conduits each pass the feed perpendicularly into a separate mixing conduit that discharges a mixture of gas medium and oil into each spray nozzle. Another header supplies individual gas conduits that pass the gas medium longitudinally into the mixture conduits at a right angle to the catalyst stream. The ends of the mixture conduits dispose the spray injection nozzles in positions to produce an array of feed injection jets.

    摘要翻译： 用于控制生产基本上线性的烃类进料喷射射流阵列的装置通过使每个射流的各个管道通过位于接触容器中的支撑罩而保持稳定和可靠的喷射。 通过在排放喷嘴上游的多个均匀产生的进料注入流中的每一个中独立地注入均匀量的气体介质来提供可控制的雾化，其将烃和气体介质的每个混合流分别排放到催化剂颗粒流中或附近 支撑罩的内端。 进料喷射射流适合于定位在大型接触容器的内部位置。 通过将来自油头的碳氢化合物流分成用于每个喷射喷嘴的单个油导管来获得分布的均匀性。 各个油管道各自将进料垂直地送入单独的混合管道，将气体介质和油的混合物排放到每个喷嘴中。 另一个头部供应单独的气体导管，其将气体介质沿着与催化剂流成直角的方向纵向通入混合物管道。 混合物管道的端部将喷射喷嘴设置在产生一系列进料喷射射流的位置。

    Dual riser catalytic cracker for increased light olefin yield
    9.
    发明授权
    Dual riser catalytic cracker for increased light olefin yield 有权
    双重提升式催化裂化器，用于提高轻烯烃产率

    公开(公告)号：US09238600B2

    公开(公告)日：2016-01-19

    申请号：US13325292

    申请日：2011-12-14

    申请人： David A. Wegerer ,  Brian W. Hedrick ,  Zhihao Fei ,  Daniel N. Myers ,  Vincenza Myers ,  Paolo Palmas ,  Laura E. Leonard

    发明人： David A. Wegerer ,  Brian W. Hedrick ,  Zhihao Fei ,  Daniel N. Myers ,  Paolo Palmas ,  Laura E. Leonard

    IPC分类号： C07C4/06 ,  C10G51/02 ,  C10G11/05 ,  C10G11/18

    CPC分类号： C07C4/06 ,  C07C2521/04 ,  C07C2521/08 ,  C07C2521/16 ,  C07C2529/40 ,  C07C2529/50 ,  C07C2529/65 ,  C10G11/05 ,  C10G11/18 ,  C10G51/026 ,  C10G2400/20 ,  Y02P20/52 ,  Y02P20/584 ,  C07C11/04 ,  C07C11/06

    摘要： A process for improving the yield of ethylene and propylene from a light naphtha feedstock includes obtaining light naphtha feedstock from a primary cracking zone having a cracking catalyst. The light naphtha feedstock is contacted with an olefin catalyst in an olefin producing zone to produce an ethylene- and propylene-rich stream. After reacting with the olefin catalyst, the ethylene- and propylene-rich stream is separated from the olefin catalyst from in a separator zone. At least a portion of the olefin catalyst is regenerated by combusting coke deposited on a surface of the olefin catalyst in an oxygen-containing environment, and at least a portion of the olefin catalyst is heated. These portions could be the same one or they could be different. In some embodiments, at least a portion of the olefin catalyst could be neither regenerated nor heated. The olefin catalyst is returned to the olefin producing zone.

    摘要翻译： 从轻石脑油原料提高乙烯和丙烯的产率的方法包括从具有裂化催化剂的一次裂解区获得轻质石脑油原料。 轻质石脑油原料与烯烃生产区中的烯烃催化剂接触以产生富含乙烯和丙烯的料流。 在与烯烃催化剂反应后，将乙烯和富丙烯物流从分离器区域与烯烃催化剂分离。 至少一部分烯烃催化剂通过在含氧环境中燃烧沉积在烯烃催化剂的表面上的焦炭再生，至少部分烯烃催化剂被加热。 这些部分可以是相同的，也可以是不同的。 在一些实施方案中，烯烃催化剂的至少一部分既不能再生也不能加热。 将烯烃催化剂返回到烯烃生产区。