Univation Technologies, LLC

Exxonmobil Chemical Patents Inc.

Uop Lcc

Edward F Smith

Gary David Mohr

Agapios Kyriacos Agapiou

Michael E Muhle

Zerong Lin

David Michael Glowczwski

Kevin Bruce Stavens

Keith Wesley Trapp

Michael E Sieloff

Ted A Powell

Robert Olds Hagerty

Fathi David Hussein

F David Hussein

Randall B Laird

Anthony Nicholas Speca

Jonathan Andrew Tertel

Michael D Awe

Luigi Laricchia

George Alan Vaughan

James Austin Kendrick

Scott Thomas Roger

Thomas W Towles

Stanley J Katzen

Keith W Trapp

Erick D Gamas-Castellanos

Ronald N Cooke

Ahmed H Ali

Sateesh K Rajput

James R Sollen

Mike Awe

David F Hussein

A process for reducing the loss of catalyst activity of a Ziegler-Natta catalyst is provided. The process includes preparing a Ziegler-Natta (ZN) catalyst by contacting the ZN catalyst with at least one aluminum alkyl compound to produce a reduced ZN catalyst and storing and/or transporting the reduced ZN catalyst for at least 20 days at a temperature of 25&#xb0; C. or less. The reduced ZN catalyst may be used for polymerizing polyolefin polymers.

Processes for reducing the loss of catalyst activity of a Ziegler-Natta catalyst

Processes and apparatus for preparing bimodal polymers are provided. In some embodiments, processes include introducing a monomer, a first diluent, a catalyst, hydrogen, at a first hydrogen concentration, and optional comonomer, to a first loop reactor to produce, under polymerization conditions, a first slurry of polymer solids. Processes may also include continuously discharging the first slurry of polymer solids from the loop reactor as a first polymerization effluent to a first flash tank; separating the first polymerization effluent in the first flash tank to provide a first concentrated polymer slurry with significantly lower hydrogen concentration; and transferring the first concentrated polymer slurry from the flash tank to a re-slurry mixer. Processes may further include introducing a re-slurry mixer diluent to the first concentrated polymer slurry to form a second concentrated polymer slurry in the re-slurry mixer that can be pumped to a second slurry loop reactor.

Processes and apparatus for bimodal slurry polymerization

A process and apparatus for oxidizing thiol compounds from an alkaline stream. The process includes passing a thiol rich alkaline stream and an oxygen containing gas to a low pressure oxidizing zone to oxidize at least a portion of the thiol compounds to disulfide compounds. A liquid stream comprising the alkali containing the disulfide compounds is passed through a pump to increase the pressure and form a pressurized alkaline stream. The pressurized alkaline stream and a sulfur lean liquid light hydrocarbon stream are introduced to a high pressure disulfide separation vessel to form a sulfur lean alkaline stream and a sulfur rich liquid light hydrocarbon stream.

Process for oxidizing one or more thiol compounds

A process and an apparatus for reducing the diolefin and oxygenate content of liquefied petroleum gas are disclosed. A first conduit is in fluid communication with a liquefied hydrocarbon source and a vessel. The vessel includes a solid adsorbent disposed on a support. The adsorbent is suitable for adsorbing diolefins and oxygenates. A second conduit is in fluid communication with the vessel for receiving the liquefied hydrocarbons of reduced diolefin and oxygenate content from the vessel. A steam inlet conduit is in fluid communication with a steam source and the vessel for treating the solid adsorbent containing adsorbed diolefins and oxygenates with steam to desorb the diolefins and oxygenates from the solid adsorbent. An amine absorber unit for reducing the hydrogen disulfide content of the liquefied hydrocarbon can be in fluid communication with the vessel.

Process and adsorbent for removal of diolefins and other contaminants from liquefied petroleum gas

A method of treating a gas phase fluidized bed reactor and a method of polymerizing olefins in a gas phase fluidized bed reactor in the presence of a catalyst prone to cause sheeting by introducing a chromium-containing compound into the reactor and forming a high molecular weight polymer coating on the walls of the reactor. Furthermore, a device for and method of introducing the chromium-containing compound into the fluidized bed reactor at a plurality of locations in proximity to a lower section of a bed section wall of the fluidized bed reactor, and forming a high molecular weight polymer coating on the bed section wall.

Methods and devices for polymerization

A method for treating at least one interior surface (for example, a bed wall) of a fluidized bed polymerization reactor system, including by applying a solution catalyst (preferably at least substantially uniformly and in liquid form) to each surface, and optionally (where a catalyst component of the solution catalyst comprises at least one chromium containing compound) oxidizing at least some of the applied chromium containing compound in a controlled manner.

Methods for applying solution catalysts to reactor surfaces

A method for polymerizing ethylene is provided. The method can include preparing a supported catalyst composition comprising the steps of: (a) dehydrating a chromium impregnated support; (b) at least partially dissolving a titanium-containing compound in one or more inert solvents to provide a solution comprising the titanium-containing compound; (c) contacting the dehydrated chromium impregnated support with the titanium-containing solution to provide a mixture comprising the solvent, titanium-containing compound and chromium impregnated support; (d) removing the solvent from the mixture; and (e) activating the product of step (d) at a temperature of at least 800&#xb0; F. (427&#xb0; C.) to provide a supported titanated chrome catalyst composition. The supported titanated chrome catalyst composition can be feed to a slurry reactor, and contacted with an optional co-catalyst, under polymerization conditions, with ethylene.

Method for catalyst preparation and improved polyethylene blow molding resin

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Kingwood, TX, United States of America

Edward F Smith