Univation Technologies, LLC

Exxonmobil Chemical Patents Inc.

Saudi Basic Industries Corporation

Saudi Yanbu Petrochemical Company

D Brett Fischbuch

Robert Olds Hagerty

James McLeod Farley

Kevin Bruce Stavens

Marc L DeChellis

Diwaker Singh

Sandy Clay Hinds

Douglas R Holroyd

Ai Vey Ng

The present invention relates to a continuous gas phase process comprising passing a recycle stream through a fluidized bed in a gas phase fluidized bed reactor, wherein the recycle stream comprises a low molecular weight dew point increasing component and a high molecular weight component, polymerizing an alpha-olefin monomer in the presence of a catalyst, and controlling an amount of the low molecular weight dew point increasing component in the recycle stream such that a dew point approach temperature of the recycle stream is less than the dew point approach temperature when operating with the higher molecular weight dew point increasing component alone.

Low molecular weight induced condensing agents

The present invention relates to a continuous gas phase process comprising polymerizing one or more hydrocarbon monomer(s) in a fluidized bed reactor in the presence of a Ziegler-Natta-type catalyst system and a condensable fluid for a period of at least 12 hours where the bed temperature is less than the Critical Temperature and the dew point temperature of the gas composition in the reactor is within 25&#xb0; C. of the bed temperature.

Polymerization process

Processes for reducing the ultra high molecular weight polymeric material content of a high density polyethylene produced with a bis-triarylsilyl chromate catalyst system are provided. Processes for reducing the gel content of articles produced from high density polyethylene are also provided. The gel content of the articles is reduced by using the high density polyethylene with reduced ultra high molecular weight polymeric material content to produce the articles. The processes described reduce the content of ultra high molecular weight polymeric material in comparison to conventional high density polyethylene by introducing at least one catalyst deactivator into a recycle gas line containing a recycle gas stream associated with the fluidized bed reactor. The at least one catalyst deactivator has a boiling point lower than the maximum temperature within the recycle gas line. In certain embodiments, the at least one catalyst deactivator is introduced in the portion of the recycle gas line upstream of a recycle gas cooler at a ratio of 0.0075 mole of the at least one catalyst deactivator per 1 million moles of make-up ethylene to about 0.12 mole of the at least one catalyst deactivator per 1 million moles of make-up ethylene in the reaction system. In certain embodiments, the at least one catalyst deactivator is oxygen.

Processes for producing high density polyethylene

The present invention relates to a continuous gas phase process comprising polymerizing one or more hydrocarbon monomer(s) in a fluidized bed reactor in the presence of catalyst system or polymerization catalyst and a condensable fluid for a period of at least 12 hours where the bed temperature is less than the Critical Temperature and the dew point temperature of the gas composition in the reactor is within 25&#xb0; C. of the bed temperature.

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Kingwood, TX, United States of America

D Brett Fischbuch