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. 15, 2019

Filed:

Apr. 19, 2017
Applicant:

Nova Chemicals (International) S.a., Fribourg, CH;

Inventors:

Zengrong Zhang, Calgary, CA;

Niousha Kazemi, Calgary, CA;

Stephen Salomons, Calgary, CA;

Monika Kleczek, Calgary, CA;

Mehdi Keshtkar, Calgary, CA;

Brian Molloy, Airdrie, CA;

Qinyan Wang, Calgary, CA;

Peter Zoricak, Calgary, CA;

Charles Carter, Calgary, CA;

XiaoChuan Wang, Calgary, CA;

Christopher Dobbin, Calgary, CA;

Fazle Sibtain, Calgary, CA;

Kenneth Taylor, Sarnia, CA;

Lawrence VanAsseldonk, Sarnia, CA;

Hamidreza Khakdaman, Houston, TX (US);

Assignee:
Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C08F 210/16 (2006.01); C08J 5/18 (2006.01); C08F 210/14 (2006.01); C08F 2/06 (2006.01); C08L 23/06 (2006.01); C08L 23/08 (2006.01); C08F 4/659 (2006.01); C08F 4/6592 (2006.01);
U.S. Cl.
CPC ...
C08L 23/0815 (2013.01); C08F 210/16 (2013.01); C08J 5/18 (2013.01); C08F 4/6592 (2013.01); C08F 4/65908 (2013.01); C08F 4/65912 (2013.01); C08F 4/65927 (2013.01); C08F 2420/04 (2013.01); C08J 2323/08 (2013.01); C08J 2423/06 (2013.01); C08J 2423/08 (2013.01); C08L 2203/16 (2013.01); C08L 2205/025 (2013.01); C08L 2205/03 (2013.01); C08L 2207/07 (2013.01); C08L 2314/06 (2013.01);
Abstract

A continuous solution polymerization process is disclosed wherein at least two homogeneous catalyst formulations are employed. A first homogeneous catalyst formulation is employed in a first reactor to produce a first ethylene interpolymer and a second homogeneous catalyst formulation is employed in a second reactor to produce a second ethylene interpolymer. Optionally a third ethylene interpolymer is formed in a third reactor. The resulting ethylene interpolymer products possess desirable properties in a variety of end use applications, for example in film applications. A means for increasing the molecular weight of the first ethylene interpolymer is disclosed and/or a means for increasing the temperature of the first reactor, relative to the third homogeneous catalyst formulation. A means for reducing the (α-olefin/ethylene) weight ratio in the first reactor is disclosed and/or reducing the density of the first ethylene interpolymer, relative to the third homogeneous catalyst formulation.


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