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:
Jun. 08, 2021

Filed:

Apr. 08, 2016
Applicant:

Borealis Ag, Vienna, AT;

Inventors:

Hermann Braun, Linz, AT;

Rebeca Reguillo Carmona, Linz, AT;

Sascha Kaltenbacher, Linz, AT;

Katja Klimke, Abu Dhabi, AE;

Udo Muster, Salzburg, AT;

Hermann Prokschi, Wartberg ob der Aist, AT;

Assignee:

BOREALIS AG, Vienna, AT;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C08J 3/12 (2006.01); B29C 48/29 (2019.01); C08F 210/06 (2006.01); C08L 23/14 (2006.01); B29B 7/48 (2006.01); C08F 255/02 (2006.01); B29B 7/88 (2006.01); B29B 7/72 (2006.01); B29B 7/84 (2006.01); B29B 9/12 (2006.01); B29C 48/285 (2019.01); B29C 48/05 (2019.01); B29C 48/76 (2019.01); C08F 236/06 (2006.01); B29B 9/06 (2006.01);
U.S. Cl.
CPC ...
C08J 3/12 (2013.01); B29B 7/48 (2013.01); B29B 7/726 (2013.01); B29B 7/845 (2013.01); B29B 7/88 (2013.01); B29B 9/12 (2013.01); B29C 48/05 (2019.02); B29C 48/297 (2019.02); B29C 48/767 (2019.02); C08F 210/06 (2013.01); C08F 236/06 (2013.01); C08F 255/02 (2013.01); C08L 23/14 (2013.01); B29B 7/728 (2013.01); B29B 9/06 (2013.01);
Abstract

The present invention is directed to a process for producing a modified olefin polymer having increased melt strength in an extruder. The process comprising the steps of: (A) contacting a stream comprising particles of an olefin polymer with a vapour stream of a functionally unsaturated compound in vapour phase thereby producing a first mixed stream; (B) passing the first mixed stream to an extruder; (C) melting the polymer particles of the first mixed stream in the extruder; (D) introducing a stream of a free radical generator either into the first mixed stream or into the extruder; and (E) extruding the first mixed stream and the free radical generator at a temperature which is greater than the decomposition temperature of the free radical generator and the melting temperature of the olefin polymer but less than the decomposition temperature of the olefin polymer thereby producing the modified olefin polymer in the extruder.


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