Mohamed F Shakur718 34Th St, Ocala, FL 34471

2012014, Jun 14, 2012

Dec 10, 2010

12/965425

Steven Lee Krupa - Fox River Grove IL, US
Christian D. Freet - South Elgin IL, US
Mohamed Shakur - Hoffman Estates IL, US

UOP, LLC - Des Plaines IL

C07C 2/06
C07C 2/16
B01J 19/00
C07C 2/08

585304, 422134

One exemplary embodiment can be a process for oligomerizing one or more hydrocarbons. Usually, the process includes providing a feed including one or more C3 and C4 hydrocarbons to a separation zone, separating a first stream including an effective amount of C3 olefins for oligomerizing, separating a second stream including an effective amount of one or more C4 olefins for oligomerizing, providing at least a portion of the first stream to a first oligomerization zone for producing at least one of a C9 and a C12 hydrocarbon, and providing at least a portion of the second stream to a second oligomerization zone for producing at least one of a C8 and a C12 hydrocarbon.

2012014, Jun 14, 2012

Dec 10, 2010

12/965596

Steven Lee Krupa - Fox River Grove IL, US
Christian D. Freet - South Elgin IL, US
Mohamed Shakur - Hoffman Estates IL, US

UOP, LLC - Des Plaines IL

C07C 2/06
B01J 8/00

585304, 422131, 585700

One exemplary embodiment can be a process for oligomerizing one or more hydrocarbons. The process can include providing a feed including one or more C3 and C4 hydrocarbons to a separation zone, separating at least a portion of C3 olefins, sending the C3 olefins to a first oligomerization zone for producing one or more C9 hydrocarbons, and returning at least a portion of an effluent from the first oligomerization zone to the separation zone.

2012014, Jun 14, 2012

Dec 10, 2010

12/965565

Steven Lee Krupa - Fox River Grove IL, US
Christian D. Freet - South Elgin IL, US
Mohamed Shakur - Hoffman Estates IL, US

UOP, LLC - Des Plaines IL

C07C 7/04
C07C 2/02

585504, 585800

One exemplary embodiment can be a process for separating at least one oligomerized effluent. The process can include providing an effluent from at least one of a first oligomerization zone for producing at least one of a C9 and a C12 hydrocarbon and a second oligomerization zone for producing at least one of a C8 and a C12 hydrocarbon, providing at least a portion of the effluent to a separation zone, and providing at least one stream from the separation zone to a hydrotreatment zone.

2012027, Oct 25, 2012

Apr 20, 2011

13/090783

Paul A. Sechrist - South Barrington IL, US
Gregory Werba - Arlington Heights IL, US
Mohamed Shakur - Hoffman Estates IL, US
Steven Lankton - Wheeling IL, US
Steven Kozup - Chicago IL, US
Bing Sun - South Barrington IL, US

UOP LLC - Des Plaines IL

C07C 4/00
C07C 5/327

585315, 585654

Embodiments of processes for producing propylene from paraffins are provided. The process comprises the steps of combining an effluent that comprises propylene and propane from a paraffin dehydrogenation reactor with an offgas stream that comprises propane to form a combined effluent stream. The combined effluent stream is separated into a propylene product stream and a propane-rich recycle stream. The propane-rich recycle stream is introduced to the paraffin dehydrogenation reactor operating at dehydrogenation conditions to convert propane in the propane-rich recycle stream to propylene.

2018011, May 3, 2018

Oct 27, 2017

15/796730

- Des Plaines IL, US
Mohamed S. Shakur - Hoffman Estates IL, US

B01J 38/42
B01J 38/18
B01J 38/26
B01J 8/26
B01J 27/32
B01J 38/72

A process for regenerating catalyst particles is disclosed. The process includes the steps: (a) withdrawing a regeneration zone effluent comprising halogen from a regeneration zone, wherein the regeneration zone contains catalyst particles comprising halogen; (b) contacting a first portion of the regeneration zone effluent with adsorbent in a first adsorption zone, removing halogen from the first portion of the regeneration zone effluent, and withdrawing from the first adsorption zone a first adsorption zone effluent; (c) contacting the first adsorption zone effluent with a water removing material to create a first water-depleted stream; and (d) passing the first water-depleted stream to the regeneration zone. Other embodiments include different orders of the steps.

2016017, Jun 23, 2016

Sep 29, 2015

14/869235

- Des Plaines IL, US
Mohamed S. Shakur - Hoffman Estates IL, US

B01J 38/42

A process for regenerating catalyst particles is disclosed. The process includes the steps: (a) withdrawing a regeneration zone effluent comprising halogen from a regeneration zone, wherein the regeneration zone contains catalyst particles comprising halogen; (b) contacting a first portion of the regeneration zone effluent with adsorbent in a first adsorption zone, removing halogen from the first portion of the regeneration zone effluent, and withdrawing from the first adsorption zone a first adsorption zone effluent; (c) contacting the first adsorption zone effluent with a water removing material to create a first water-depleted stream; and (d) passing the first water-depleted stream to the regeneration zone. Other embodiments include different orders of the steps.

2015029, Oct 15, 2015

Apr 14, 2014

14/252237

- Des Plaines IL, US
Ka Lok - Buffalo Grove IL, US
Mary J. Wier - Schaumburg IL, US
Mohamed S. Shakur - Hoffman Estates IL, US
Michael A. Moore - Des Plaines IL, US
Alexander Sabitov - Wilmette IL, US

UOP LLC - Des Plaines IL

B01J 38/44
B01J 27/32
B01J 27/13
B01J 38/42
B01J 38/20

A process for regenerating a catalyst used in a reaction zone. In a regeneration zone, the catalyst may be cooled before passing into a chloride rich zone. The regeneration zone may also receive a heated ambient oxygen in a catalyst heating zone. The regeneration zone may also receive recovered chloride from a chloride recovering zone which removes and recovers chloride from regeneration gas taken from the regeneration zone. Heated ambient oxygen may also be introduced into a chlorination zone.

2015017, Jun 25, 2015

Dec 20, 2013

14/135750

- Des Plaines IL, US
Mohamed S. Shakur - Hoffman Estates IL, US

UOP LLC - Des Plaines IL

C07C 5/27
B01J 19/24

Methods and apparatuses are provided for isomerizing a hydrocarbon stream. The method includes isomerizing a hydrocarbon stream in a reactor to produce an intermediate isomerized stream. The intermediate isomerized stream is fractionated to produce an off gas stream and a heavy isomerized stream, where the off gas stream includes an off gas recycle stream. The off gas recycle stream is dried in an off gas dryer to produce a hydrogen recycle stream, where the off gas drier includes an off gas dryer membrane separating the off gas recycle stream from an off gas purge stream. The off dryer membrane includes a perfluorosulfonated ionomer. The hydrogen recycle stream is then fed into the reactor.