The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Jul. 19, 2016

Filed:

Dec. 14, 2011
Applicants:

Andrew David Bell, Carry-le-Rouet, FR;

Jean-louis Chamayou, Carry-le-Rouet, FR;

Kevin Peter Ramsay, West Lothian, GB;

Inventors:

Andrew David Bell, Carry-le-Rouet, FR;

Jean-Louis Chamayou, Carry-le-Rouet, FR;

Kevin Peter Ramsay, West Lothian, GB;

Assignee:

INEOS SALES (UK) LIMITED, Lyndhurst, Hampshire, GB;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C08F 2/34 (2006.01); B01J 8/24 (2006.01); B01J 8/44 (2006.01); C08F 10/00 (2006.01); C08F 110/02 (2006.01);
U.S. Cl.
CPC ...
C08F 2/34 (2013.01); C08F 10/00 (2013.01); C08F 110/02 (2013.01);
Abstract

Process for gas phase polymerization of olefins in a fluidized bed reactor by (a) passing a fluidizing gas containing at least one olefin monomer through a fluidized bed of polymer particles in the presence of a polymerization catalyst to produce polymer at a polymer production rate of C Tonnes/hour, (b) withdrawing a first gaseous stream containing solid particles from the top of the reactor, (c) passing the first gaseous stream to a gas/solids separator, separating solid particles therefrom, and forming a second gaseous stream containing residual solid particles, (d) passing a portion of the second gaseous stream to at least one heat exchanger to remove heat of reaction whereby residual solid particles contact the heat exchanger, and (e) recycling a portion of the cooled stream from step (d) as the fluidizing gas in step (a). The heat exchangers have a heat exchange surface area which totals less than 120×C m.


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