公开(公告)号：AU2014241542B2

公开(公告)日：2017-09-14

申请号：AU2014241542

申请日：2014-03-26

Applicant: UOP LLC

Inventor： VETTER MICHAEL J ,  KRISHNAMURTHY SUJAY ,  LEONARD LAURA E ,  SECHRIST PAUL A ,  FURFARO ANGELO P ,  YUAN QUAN

IPC: B01J8/02 ,  B01J8/06 ,  B01J8/08

Abstract: An inclined baseplate for a radial bed reactor improves solids flow from the bottom of the reactor. Gas flow can be improved by utilizing an aerated baseplate or by providing a non-porous section of outer perforated cylinder in the area below the level of the bottom of the inner perforated cylinder.

公开(公告)号：MY159876A

公开(公告)日：2017-02-15

申请号：MYPI2011002472

申请日：2009-12-08

Applicant: UOP LLC

Inventor： BRICKER MAUREEN L ,  LEONARD LAURA E

IPC: C07C31/20 ,  B01J19/00

Abstract: A METHOD AND APPARATUS FOR CONVERTING GLYCEROL INTO PROPYLENE GLYCOL BY DIRECTING A BASIC GLYCEROL CONTAINING FEED AND A HYDROGEN CONTAINING GAS INTO A REACTION ZONE INCLUDING A FIXED BED OF CATALYST THAT IS OPERATING AT GLYCEROL CONVERSION CONDITIONS WHERE THE REACTOR INCLUDES AND AT LEAST ONE QUENCH ZONE AND DIRECTING A QUENCH MATERIAL INTO THE QUENCH ZONE.

公开(公告)号：CA2862873C

公开(公告)日：2016-12-06

申请号：CA2862873

申请日：2013-03-06

Applicant: UOP LLC

Inventor： LEONARD LAURA E ,  GAJDA GREGORY J ,  KOZUP STEVEN C

IPC: B01J38/10 ,  B01J38/02

Abstract: A process is presented for the management of sulfur on a catalyst. The catalyst is a dehydrogenation catalyst, and sulfur accumulates during the dehydrogenation process. Sulfur compounds are stripped from the spent catalyst and the catalyst is cooled before the regeneration process. The process includes controlling the amount of sulfur that needs to be removed from the catalyst before regeneration.

公开(公告)号：CA2852512C

公开(公告)日：2016-09-20

申请号：CA2852512

申请日：2013-02-27

Applicant: UOP LLC

Inventor： EGOLF BRYAN J ,  LEONARD LAURA E ,  CARACOTSIOS MICHAEL

IPC: B01J38/18 ,  B01J38/20 ,  B01J38/34 ,  B01J38/42

Abstract: A process for a continuous regeneration of a catalyst wherein the regeneration section includes at least two separate zones. The regeneration includes an upper combustion zone, and an lower combustion zone, where the process utilizes at least two independent regeneration gas loops for control of the amount of oxygen to regenerate the catalyst. The upper combustion zone can be divided into multiple zones, and the combustion zone can be divided into multiple zones.

公开(公告)号：BRPI0923468A2

公开(公告)日：2016-01-12

申请号：BRPI0923468

申请日：2009-12-08

Applicant: UOP LLC

Inventor： LEONARD LAURA E ,  BRICKER MAUREEN L

IPC: B01J8/04 ,  C07C29/60 ,  C07C31/20

公开(公告)号：CL2015000355A1

公开(公告)日：2015-07-03

申请号：CL2015000355

申请日：2015-02-16

Applicant: UOP LLC

Inventor： BEDARD ROBERT L ,  NAUNHEIMER CHRISTOPHER ,  TOWLER GAVIN P ,  LEONARD LAURA E ,  DUDEBOUT RODOLPHE ,  WOODCOCK GREGORY O ,  MITTENDORF DONALD L ,  KEETON TONY J

IPC: C07C11/24

公开(公告)号：SG11201500520UA

公开(公告)日：2015-02-27

申请号：SG11201500520U

申请日：2013-08-16

Applicant: UOP LLC

Inventor： BEDARD ROBERT L ,  NAUNHEIMER CHRISTOPHER ,  TOWLER GAVIN P ,  LEONARD LAURA E ,  DUDEBOUT RODOLPHE ,  WOODCOCK GREGORY O ,  MITTENDORF DONALD L ,  KEETON TONY J

IPC: C07C11/24 ,  B01J19/10 ,  C07C2/76 ,  C10G9/00

Abstract: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

公开(公告)号：ES2526749R1

公开(公告)日：2015-02-02

申请号：ES201490092

申请日：2013-03-06

Applicant: UOP LLC

Inventor： LEONARD LAURA E ,  GAJDA GREGORY J ,  KOZUP STEVEN C

IPC: B01J23/96 ,  B01J38/10 ,  C07C5/333

公开(公告)号：SG193243A1

公开(公告)日：2013-10-30

申请号：SG2013065321

申请日：2012-05-03

Applicant: UOP LLC

Inventor： LEONARD LAURA E ,  HAIZMANN ROBERT

Abstract: One exemplary embodiment can be a process for alkylating benzene. The process can include obtaining at least a portion of a stream from a transalkylation zone, combining the at least the portion of the stream from the transalkylation zone with a fuel gas stream, and providing at least a portion of the combined stream to a benzene methylation zone. Typically, the fuel gas stream includes an effective amount of one or more alkanes for alkylating at least partially from a hydrogen purification process tail gas.