公开(公告)号：WO2011084354A3

公开(公告)日：2011-07-14

申请号：PCT/US2010/059849

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 ,  C10G11/16 ,  B01J38/00

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.

公开(公告)号：WO2011123494A3

公开(公告)日：2011-10-06

申请号：PCT/US2011/030439

申请日：2011-03-30

Applicant: UOP LLC ,  STINE, Laurence O.

Inventor： STINE, Laurence O.

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

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.

公开(公告)号：WO2011084355A2

公开(公告)日：2011-07-14

申请号：PCT/US2010/059856

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: 提供了使用多个移动床径向流动反应器的烃烷基化系统和方法。 可以在每个反应器之前通过提供将烯烃与烃进料或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混合器来提供烯烃注入点。 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。 移动床径向流动反应器可堆叠在一个或多个反应堆中。

公开(公告)号：WO2011084352A2

公开(公告)日：2011-07-14

申请号：PCT/US2010/059841

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 ,  C10G47/02 ,  B01J38/00 ,  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: 提供了用于烃类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流反应器。 可以在每个反应器之前提供氢注入点，通过提供将氢气与烃类进料混合的混合器，或与来自上游反应器的流出物料流一起产生反应器进料流。 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。 移动床反应器可以堆叠在一个或多个反应器堆叠中。

公开(公告)号：WO2014204739A1

公开(公告)日：2014-12-24

申请号：PCT/US2014/041855

申请日：2014-06-11

Applicant: UOP LLC

Inventor： STINE, Laurence O. ,  VORA, Bipin V. ,  IBRAHIM, Malek Y.S. ,  WEI, Daniel H.

IPC: B01J8/18 ,  B01J8/24 ,  B01J19/26 ,  C07C4/00

CPC classification number: C07C5/48 ,  C07C2521/04 ,  C07C11/06

Abstract: A process of oxidative dehydrogenation in a fluidized riser reactor is described. Hydrocarbon feed and catalyst are fed to the bottom of the fluidized riser reactor. Part of the hydrogen produced in the dehydrogenation reaction is oxidized using oxygen introduced into the riser reactor through oxygen injection ports to produce the heat required for the dehydrogenation reaction.

Abstract translation: 描述了在流化提升管反应器中的氧化脱氢过程。 烃进料和催化剂进料到流化提升管反应器的底部。 在脱氢反应中产生的一部分氢气通过氧气注入口引入提升管反应器中的氧气被氧化，以产生脱氢反应所需的热量。