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:
Oct. 25, 2016

Filed:

Dec. 12, 2012
Applicant:

Borealis Ag, Vienna, AT;

Inventors:

Pauli Leskinen, Helsinki, FI;

Sameli Hakola, Helsinki, FI;

Kauno Alastalo, Porvoo, FI;

Klaus Nyfors, Porvoo, FI;

Assignee:

Borealis AG, , AT;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C08F 110/06 (2006.01); C08F 2/01 (2006.01); C08F 2/14 (2006.01); B01J 19/00 (2006.01); B01J 19/24 (2006.01); C08F 10/00 (2006.01); C08F 2/38 (2006.01); C08F 210/06 (2006.01);
U.S. Cl.
CPC ...
C08F 110/06 (2013.01); B01J 19/0033 (2013.01); B01J 19/0053 (2013.01); B01J 19/245 (2013.01); B01J 19/2435 (2013.01); B01J 19/2455 (2013.01); C08F 10/00 (2013.01); B01J 2219/0004 (2013.01); B01J 2219/00049 (2013.01); C08F 210/06 (2013.01);
Abstract

Method for preparing olefin polymer in a loop reactor, said loop reactor comprises a first outlet for withdrawing polymer slurry from the loop reactor, and a second outlet for withdrawing a polymer slurry from the loop reactor, wherein the first outlet is located such that polymer slurry is withdrawn having a concentration of polymer which is equal or higher than the average concentration of polymer in the loop reactor, and the second outlet is located such that polymer slurry is withdrawn having a concentration of polymer which is lower than the average concentration of polymer in the loop reactor, the method comprises the steps of supplying olefin monomers and a catalytic system to the loop reactor to form a polymer slurry in the loop reactor, and controlling the total amount of polymer and/or the total amount of polymer slurry withdrawn from the loop reactor by adjusting the ratio of polymer slurry withdrawn through the first outlet and polymer slurry withdrawn through the second outlet.


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