公开(公告)号：WO2011123494A2

公开(公告)日：2011-10-06

申请号：PCT/US2011030439

申请日：2011-03-30

Applicant: UOP LLC ,  STINE LAURENCE O

Inventor： STINE LAURENCE O

IPC: C10G47/30 ,  B01J38/00 ,  C10G45/20

CPC classification number: B01J8/226 ,  B01J8/0055 ,  B01J8/007 ,  B01J8/12 ,  B01J8/125 ,  B01J8/1827 ,  B01J8/1854 ,  B01J8/34 ,  B01J8/386 ,  C10G49/16

Abstract: One exemplary embodiment can be a hydroprocessing method. The hydroprocessing method can include providing a feed and a stream including hydrogen to a vessel. The vessel may have a catalyst collector and an internal riser. Generally, a catalyst circulates within the vessel by at least partially rising within the internal riser.

Abstract translation: 一个示例性实施方案可以是加氢处理方法。 加氢处理方法可以包括向容器提供包含氢的进料和流。 容器可以具有催化剂收集器和内部提升管。 通常，催化剂在容器内通过在内部提升管内部至少部分升高而循环。

公开(公告)号：WO2011084354A2

公开(公告)日：2011-07-14

申请号：PCT/US2010059849

申请日：2010-12-10

Applicant: UOP LLC ,  SADLER CLAYTON C ,  WIER MARY JO ,  STINE LAURENCE O ,  NAUNHEIMER CHRISTOPHER

Inventor： SADLER CLAYTON C ,  WIER MARY JO ,  STINE LAURENCE O ,  NAUNHEIMER CHRISTOPHER

IPC: C10G35/10 ,  B01J38/00 ,  C10G11/16

CPC classification number: C07C2/58 ,  C07C9/16

Abstract: Systems and processes for hydrocarbon conversion are provided that utilize a plurality of moving bed reactors. The reactors may be moving bed radial flow reactors. Optional mixers that mix a portion of a second hydrocarbon feed with the effluent stream from an upstream reactor, to produce reactor feed streams may be employed, and the reactor feed streams may be introduced at injection points prior to each reactor. Catalyst can be provided from the reaction zone of one reactor to the reaction zone of a downstream reactor through catalyst transfer pipes, and can be regenerated after passing through the reaction zones of the reactors. The moving bed reactors can be stacked in one or more reactor stacks.

Abstract translation: 提供了利用多个移动床反应器的烃转化系统和方法。 反应器可以是移动床径向流动反应器。 可以使用将一部分第二烃进料与来自上游反应器的流出物流混合以产生反应器进料流的任选混合器，并且可以在每个反应器之前的注入点处引入反应器进料流。 催化剂可以通过催化剂输送管从一个反应器的反应区提供到下游反应器的反应区，并且可以在通过反应器的反应区后再生。 移动床反应器可堆叠在一个或多个反应堆中。

公开(公告)号：WO2011084352A3

公开(公告)日：2011-10-06

申请号：PCT/US2010059841

申请日：2010-12-10

Applicant: UOP LLC ,  SADLER CLAYTON C ,  WIER MARY JO ,  STINE LAURENCE O ,  NAUNHEIMER CHRISTOPHER

Inventor： SADLER CLAYTON C ,  WIER MARY JO ,  STINE LAURENCE O ,  NAUNHEIMER CHRISTOPHER

IPC: C10G47/24 ,  B01J38/00 ,  C10G47/02 ,  C10G65/02

CPC classification number: C10G47/28 ,  B01J8/085 ,  B01J8/125 ,  B01J8/22 ,  B01J2208/00548 ,  B01J2219/0004 ,  C10G65/10 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/301 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/06

Abstract: Systems and processes for the hydroprocessing of a hydrocarbonaceous feed are provided that utilize a plurality of moving bed reactors. The reactors may be moving bed radial flow reactors. A hydrogen injection point can be provided prior to each reactor by providing a mixer that mixes hydrogen with a hydrocarbonaceous feed, or with the effluent stream from an upstream reactor, to produce a reactor feed stream. Catalyst can be provided from the reaction zone of one reactor to the reaction zone of a downstream reactor through catalyst transfer pipes, and can be regenerated after passing through the reaction zones of the reactors. The moving bed reactors can be stacked in one or more reactor stacks.

Abstract translation: 提供了用于含烃进料的加氢处理的系统和方法，其利用多个移动床反应器。 反应器可以是移动床径向流动反应器。 可以在每个反应器之前通过提供将氢气与含烃原料或与来自上游反应器的流出物流混合以产生反应器原料流的混合器来提供氢气注入点。 催化剂可以通过催化剂输送管从一个反应器的反应区提供到下游反应器的反应区，并且可以在通过反应器的反应区后再生。 移动床反应器可堆叠在一个或多个反应堆中。

公开(公告)号：WO2011084355A3

公开(公告)日：2011-10-06

申请号：PCT/US2010059856

申请日：2010-12-10

Applicant: UOP LLC ,  SADLER CLAYTON C ,  WIER MARY JO ,  STINE LAURENCE O ,  NAUNHEIMER CHRISTOPHER

Inventor： SADLER CLAYTON C ,  WIER MARY JO ,  STINE LAURENCE O ,  NAUNHEIMER CHRISTOPHER

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

CPC classification number: C07C2/58 ,  C07C11/02

Abstract: Systems and processes for the alkylation of a hydrocarbon are provided that utilize a plurality of moving bed radial flow reactors. An olefin injection point can be provided prior to each reactor by providing a mixer that mixes olefin with a hydrocarbon feed, or with the effluent stream from an upstream reactor, to produce a reactor feed stream. Catalyst can be provided from the reaction zone of one reactor to the reaction zone of a downstream reactor through catalyst transfer pipes, and can be regenerated after passing through the reaction zones of the reactors. The moving bed radial flow reactors can be stacked in one or more reactor stacks.

Abstract translation: 提供用于烷基化烃的系统和方法，其利用多个移动床径流反应器。 可以在每个反应器之前提供烯烃注入点，通过提供将烯烃与烃进料或来自上游反应器的流出物流混合以产生反应器进料流的混合器。 催化剂可以通过催化剂转移管从一个反应器的反应区提供到下游反应器的反应区，并且可以在通过反应器的反应区之后再生。 移动床径向流动反应器可以堆叠在一个或多个反应器堆叠中。