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:
May. 06, 2025

Filed:

Apr. 06, 2020
Applicant:

Borealis Ag, Vienna, AT;

Inventors:

Apostolos Krallis, Porvoo, FI;

Vasileios Kanellopoulos, Linz, AT;

Erno Elovainio, Porvoo, FI;

Klaus Nyfors, Linz, AT;

Joana Kettner, Linz, AT;

Assignee:

BOREALIS AG, Vienna, AT;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C08F 10/02 (2005.12); B01J 8/08 (2005.12); B01J 8/18 (2005.12); B01J 8/24 (2005.12); B01J 19/24 (2005.12); C07F 3/02 (2005.12); C07F 7/28 (2005.12); C08F 2/00 (2005.12); C08F 2/01 (2005.12); C08F 210/06 (2005.12);
U.S. Cl.
CPC ...
B01J 8/24 (2012.12); B01J 8/08 (2012.12); B01J 8/1827 (2012.12); B01J 8/1854 (2012.12); B01J 19/2435 (2012.12); C07F 3/02 (2012.12); C07F 7/28 (2012.12); C08F 2/001 (2012.12); C08F 2/01 (2012.12); C08F 210/06 (2012.12); B01J 2219/1943 (2012.12); C08F 10/02 (2012.12);
Abstract

A process for the production of polyolefins comprising: feeding a slurry comprising at least one polymerization catalyst, at least one carrier liquid, first olefin monomer(s) and optionally at least one first comonomer into at least one loop reactor; polymerizing the first olefin monomer(s) and optionally the at least one first comonomer yielding a first polyolefin; withdrawing the first polyolefin from the loop reactor; feeding the first polyolefin to a gas-solids olefin polymerization reactor, wherein the gas-solids olefin polymerization reactor comprises: a top zone; a middle zone, which comprises a top end in direct contact with said top zone and which is located below said top zone, the middle zone having a generally cylindrical shape; and a bottom zone, which is in direct contact with a bottom end of the middle zone and which is located below the middle zone; introducing a fluidization gas stream into the bottom zone of the gas-solids olefin polymerization reactor; polymerizing second olefin monomer(s) and optionally at least one second comonomer in the presence of the polymerization catalyst and the first polyolefin to a second polyolefin in a dense phase formed by particles of said second polyolefin suspended in an upwards flowing stream of the fluidization gas in the middle zone; introducing a jet gas stream through one or more jet gas feeding ports in a jet gas feeding area of the middle zone at the dense phase in the middle zone of the gas-solids olefin polymerization reactor; withdrawing the second polyolefin from the gas-solids olefin polymerization reactor.


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