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    SLURRY COLUMN GASOLINE ALKYLATION USING GAS PHASE OLEFIN INJECTION
    2.
    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：US20110060178A1

    公开(公告)日：2011-03-10

    申请号：US12554044

    申请日：2009-09-04

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

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

    IPC: C07C2/58 ,  B01J8/08 ,  B01J19/00 ,  B01J38/00

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

    Abstract: 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.

    Abstract translation: 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。

    Multi-stage fluidized bed reactor for dehydrogenation of hydrocarbons
    3.
    发明授权
    Multi-stage fluidized bed reactor for dehydrogenation of hydrocarbons 有权
    用于烃脱氢的多级流化床反应器

    公开(公告)号：US08282887B2

    公开(公告)日：2012-10-09

    申请号：US12749542

    申请日：2010-03-30

    Applicant: David N. Myers ,  Lev Davydov

    Inventor： David N. Myers ,  Lev Davydov

    IPC: B01J8/18 ,  F27B15/00 ,  B01J19/00 ,  B01J8/02 ,  B01J35/02 ,  C10G35/10

    CPC classification number: B01J8/36 ,  B01J8/1836 ,  B01J2208/00292 ,  B01J2208/00707 ,  B01J2208/00991 ,  C10G45/00 ,  C10G2300/1081 ,  C10G2400/20

    Abstract: A reactor design and process for the dehydrogenation of hydrocarbons is presented. The reactor design includes a multibed catalytic reactor, where each of the reactor beds are fluidized. The catalyst in the reactor cascades through the reactor beds, with fresh catalyst input into the first reactor bed, and the spent catalyst withdrawn from the last reactor bed. The hydrocarbon feedstream is input to the reactor beds in a parallel formation, thereby decreasing the thermal residence time of the hydrocarbons when compared with a single bed fluidized reactor, or a series reactor scheme.

    Abstract translation: 提出了一种用于烃脱氢的反应器设计和方法。 反应器设计包括多载体催化反应器，其中每个反应器床都被流化。 反应器中的催化剂层叠通过反应器床，新鲜的催化剂输入到第一反应器床中，并将废催化剂从最后的反应器床中取出。 碳氢化合物原料流以平行形式输入反应器床，从而​​降低烃与单床流化反应器或串联反应器方案相比的热停留时间。

    Multi-Stage Fluidized Bed Reactor for Dehydrogenation of Hydrocarbons
    4.
    发明申请
    Multi-Stage Fluidized Bed Reactor for Dehydrogenation of Hydrocarbons 有权
    用于氢化脱氢的多级流化床反应器

    公开(公告)号：US20110245557A1

    公开(公告)日：2011-10-06

    申请号：US12749544

    申请日：2010-03-30

    Applicant: David N. Myers ,  Lev Davydov

    Inventor： David N. Myers ,  Lev Davydov

    IPC: C07C5/32

    CPC classification number: C07C5/3335 ,  C07C2521/04 ,  C07C2521/12 ,  C07C11/06 ,  C07C11/08

    Abstract: A reactor design and process for the dehydrogenation of hydrocarbons is presented. The reactor design includes a multibed catalytic reactor, where each of the reactor beds are fluidized. The catalyst in the reactor cascades through the reactor beds, with fresh catalyst input into the first reactor bed, and the spent catalyst withdrawn from the last reactor bed. The hydrocarbon feedstream is input to the reactor beds in a parallel formation, thereby decreasing the thermal residence time of the hydrocarbons when compared with a single bed fluidized reactor, or a series reactor scheme.

    Abstract translation: 提出了一种用于烃脱氢的反应器设计和方法。 反应器设计包括多载体催化反应器，其中每个反应器床都被流化。 反应器中的催化剂层叠通过反应器床，新鲜的催化剂输入到第一反应器床中，并将废催化剂从最后的反应器床中取出。 碳氢化合物原料流以平行形式输入反应器床，从而​​降低烃与单床流化反应器或串联反应器方案相比的热停留时间。

    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

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

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

    IPC: B01J8/22 ,  B01J8/00

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

    Abstract: 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.

    Abstract translation: 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。

    Process for dehydrogenation of hydrocarbons in a multi-stage fluidized bed reactor
    6.
    发明授权
    Process for dehydrogenation of hydrocarbons in a multi-stage fluidized bed reactor 有权
    在多级流化床反应器中烃的脱氢方法

    公开(公告)号：US08895797B2

    公开(公告)日：2014-11-25

    申请号：US12749544

    申请日：2010-03-30

    Applicant: David N. Myers ,  Lev Davydov

    Inventor： David N. Myers ,  Lev Davydov

    IPC: C07C5/333

    CPC classification number: C07C5/3335 ,  C07C2521/04 ,  C07C2521/12 ,  C07C11/06 ,  C07C11/08

    Abstract: A reactor design and process for the dehydrogenation of hydrocarbons is presented. The reactor design includes a multibed catalytic reactor, where each of the reactor beds are fluidized. The catalyst in the reactor cascades through the reactor beds, with fresh catalyst input into the first reactor bed, and the spent catalyst withdrawn from the last reactor bed. The hydrocarbon feedstream is input to the reactor beds in a parallel formation, thereby decreasing the thermal residence time of the hydrocarbons when compared with a single bed fluidized reactor, or a series reactor scheme.

    Abstract translation: 提出了一种用于烃脱氢的反应器设计和方法。 反应器设计包括多载体催化反应器，其中每个反应器床都被流化。 反应器中的催化剂层叠通过反应器床，新鲜的催化剂输入到第一反应器床中，并将废催化剂从最后的反应器床中取出。 碳氢化合物原料流以平行形式输入反应器床，从而​​降低烃与单床流化反应器或串联反应器方案相比的热停留时间。

    Vapor-Liquid Contacting Apparatuses Having a Secondary Absorption Zone with Vortex Contacting Stages
    9.
    发明申请
    Vapor-Liquid Contacting Apparatuses Having a Secondary Absorption Zone with Vortex Contacting Stages 有权
    具有涡旋接触阶段的二次吸收区的气液接触装置

    公开(公告)号：US20110239862A1

    公开(公告)日：2011-10-06

    申请号：US12752033

    申请日：2010-03-31

    Applicant: Lev Davydov

    Inventor： Lev Davydov

    IPC: B01D53/14 ,  B01D53/18

    CPC classification number: B01D53/18 ,  B01D53/1462

    Abstract: Vapor-liquid contacting apparatuses comprising both a primary absorption zone and a secondary absorption zone comprising a plurality of vortex contacting stages are described. The apparatuses provide improved heat and mass transfer between vapor and liquid phases in processes such as absorption, to selectively solubilize contaminants (e.g., acid gases) from an impure vapor (e.g., sour natural gas). Vortex contacting stage(s) in a zone of vapor-liquid contacting, such as a secondary or finishing absorption zone, are used following bulk absorption in a primary or main absorption zone.

    Abstract translation: 描述了包括主吸收区和包括多个涡流接触级的二次吸收区两者的气 - 液接触装置。 这些装置在诸如吸收的过程中提供蒸汽和液相之间的改进的热和质量传递，以选择性地从不纯的蒸气（例如酸性天然气）中溶解污染物（例如酸性气体）。 在初级吸收区或主吸收区的体积吸收之后，使用气 - 液接触区中的涡流接触阶段，例如次级或整理吸收区。

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