Robert Joseph Noel Bernier - Flemington NJ Robert Lorenz Boysen - Blairstown NJ Robert Cecil Brown - Danbury CT Mark Gregory Goode - Hurricane WV John Henry Moorhouse - Kendall Park NJ Robert Darrell Olson - Charleston WV Leonard Sebastian Scarola - Basking Ridge NJ Thomas Edward Spriggs - Cross Lanes WV Gary Harry Williams - Flemington NJ Kevin Joseph Cann - Rocky Hill NJ Maria Angelica Apecetche - Piscataway NJ Natarajan Muruganandam - Somerville NJ Gregory George Smith - Belle Mead NJ
Assignee:
Union Carbide Chemicals Plastics Technology Corporation - Danbury CT
A process for producing polymer in a gas phase reactor by introducing a stream of monomer and gas into a polymerization zone while providing at least one liquid component in the polymerization zone.
Molecular Weight Control Of Gas Phase Polymerized Polybutadiene When Using A Rare Earth Catalyst
Natarajan Muruganandam - Belle Meade NJ Kevin Joseph Cann - Rocky Hill NJ Maria Angelica Apecetche - Piscataway NJ John Henry Moorhouse - Kendall Park NJ
Assignee:
Union Carbide Chemicals Plastics Technology Corporation - Danbury CT
International Classification:
C08F 234
US Classification:
526 60, 526153, 526164, 526 3404, 526901, 524856
Abstract:
A process for controlling the molecular weight (Mw) and molecular weight distribution (MWD) of polybutadiene polymerized in an otherwise gas phase process using a rare earth catalyst is provided.
Robert Joseph Noel Bernier - Flemington NJ Robert Lorenz Boysen - Blairstown NJ Robert Cecil Brown - Danbury CT Mark Gregory Goode - Hurricane WV John Henry Moorhouse - Kendall Park NJ Robert Darrell Olson - Charleston WV Leonard Sebastian Scarola - Basking Ridge NJ Thomas Edward Spriggs - Cross Lanes WV Gary Harry Williams - Flemington NJ Kevin Joseph Cann - Rocky Hill NJ Maria Angelica Apecetche - Piscataway NJ Natarajan Muruganandam - Somerville NJ Gregory George Smith - Belle Mead NJ
Assignee:
Union Carbide Chemicals Plastics Technology Corporation - Danbury CT
International Classification:
C08F 234
US Classification:
526137, 526142, 5261691, 526335, 5263404, 526901
Abstract:
A process for producing polymer in a gas phase reactor by introducing a stream of monomer and gas into a polymerization zone while providing at least one liquid component in the polymerization zone.
Supported Chromium Oxide Catalyst For The Production Of Broad Molecular Weight Polyethylene
Kevin J. Cann - Rocky Hill NJ, US Minghui Zhang - Hillsborough NJ, US Jose Fernando Cevallos-Candau - Charleston WV, US John Moorhouse - Kendall Park NJ, US Mark Gregory Goode - Hurricane WV, US Maria Apecetche - Piscataway NJ, US
Assignee:
Univation Technologies, LLC - Houston TX
International Classification:
B01J 31/00
US Classification:
502150, 502154, 526104, 526901
Abstract:
The present invention is directed to the use of aluminum alkyl activators and co-catalysts to improve the performance of chromium-based catalysts. The aluminum alkyls allow for the variable control of polymer molecular weight, control of side branching while possessing desirable productivities, and may be applied to the catalyst directly or separately to the reactor. Adding the alkyl aluminum compound directly to the reactor (in-situ) eliminates induction times.
Catalyst Compositions Comprising Small Silica Support Materials And Methods Of Use In Polymerization Reactions
Improved catalyst compositions, and polymerization processes using such improved catalyst compositions, are provided. An example of an improved catalyst composition is a supported catalyst system that includes at least one titanium compound, at least one magnesium compound, at least one electron donor compound, at least one activator compound, and at least one silica support material, the at least one silica support material having a median particle size in the range of from 20 to 50 microns with no more than 10% of the particles having a size less than 10 microns and no more than 10% of the particles having a size greater than 50 microns and average pore diameter of at least
Broad molecular weight polyethylene and polyethylene having a bimodal molecular weight profile can be produced with chromium oxide based catalyst systems employing alkyl silanols. The systems may also contain various organoaluminum compounds. Catalyst activity and molecular weight of the resulting polyethylene may also be tuned using the present invention.
Catalyst Compositions Comprising Small Silica Support Materials And Methods Of Use In Polymerization Reactions
Improved catalyst compositions, and polymerization processes using such improved catalyst compositions, are provided. An example of an improved catalyst composition is a supported catalyst system that includes at least one titanium compound, at least one magnesium compound, at least one electron donor compound, at least one activator compound, and at least one silica support material, the at least one silica support material having a median particle size in the range of from 20 to 50 microns with no more than 10% of the particles having a size less than 10 microns and no more than 10% of the particles having a size greater than 50 microns and average pore diameter of at least ≧220 angstroms.
Hindered Polyalicyclic Alkyl Catalysts And Their Use In A Gas-Phase Polymerization Reactor
Maria A. Apecetche - Bridgewater NJ, US John Moorhouse - Kendall Park NJ, US Mark G. Goode - Hurricane WV, US Ronald S. Eisinger - Charleston WV, US Kevin J. Cann - Rocky Hill NJ, US
Embodiments of the present invention include a method of polymerizing olefins comprising contacting olefins with a catalyst composition made by the process of combining a hindered polyalicyclic alkyl catalyst precursor with a particulate inorganic oxide for a deposition time greater than 2 hours to form a catalyst composition. Embodiments of the present invention also include catalyst compositions comprising a hindered polyalicyclic alkyl catalyst precursor made by the process of combining the hindered polyalicyclic alkyl catalyst precursor with a particulate inorganic oxide for a deposition time greater than 2 hours to form the catalyst composition. In one embodiment, the hindered polyalicyclic alkyl catalyst precursor is formed by first combining an acid, a compound having the formula RX, and a metal oxide selected from the group consisting of Group 3 to Group 10 oxide compounds to produce a catalyst precursor; characterized in that R is selected from the group consisting of hindered polyalicyclic alkyls, and substituted derivatives thereof, and X is selected from the group consisting of any suitable leaving group.