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:
Aug. 03, 2021

Filed:

Jun. 22, 2017
Applicant:

Dow Global Technologies Llc, Midland, MI (US);

Inventors:

Cornelis J F Hosman, Terneuzen, NL;

Nhi T. Y. Dang, Terneuzen, NL;

Otto J. Berbee, Terneuzen, NL;

Joaquin Flores, Tarragona, ES;

Assignee:

Dow Global Technologies LLC, Midland, MI (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C08F 2/34 (2006.01); B01J 12/00 (2006.01); C08F 2/01 (2006.01); B01J 3/02 (2006.01); B01J 3/04 (2006.01); C08F 6/00 (2006.01); C08F 10/02 (2006.01); A46B 11/06 (2006.01); B05C 17/005 (2006.01); C08F 2/00 (2006.01); C08F 210/02 (2006.01);
U.S. Cl.
CPC ...
C08F 2/34 (2013.01); A46B 11/06 (2013.01); B01J 3/02 (2013.01); B01J 3/042 (2013.01); B01J 3/046 (2013.01); B01J 12/00 (2013.01); B05C 17/00503 (2013.01); B05C 17/00569 (2013.01); B05C 17/00573 (2013.01); C08F 2/00 (2013.01); C08F 2/01 (2013.01); C08F 6/001 (2013.01); C08F 10/02 (2013.01); C08F 210/02 (2013.01); B01J 2203/06 (2013.01); Y02P 20/582 (2015.11);
Abstract

A high pressure polymerization, as described herein, to form an ethylene-based polymer, comprising the following steps: polymerizing a reaction mixture comprising ethylene, using a reactor system comprising at least three ethylene-based feed streams and a reactor configuration that comprises at least four reaction zones, and at least one of the following a) through c), is met: (a) up to 100 wt % of the ethylene stream to the first zone comes from a high pressure recycle, and/or up to 100 wt % of the last ethylene stream to a zone comes from the output from a Primary compressor system; and/or (b) up to 100 wt % of the ethylene stream to first zone comes from the output from a Primary compressor system, and/or up to 100 wt % of the last ethylene stream to a zone comes from a high pressure recycle; and/or (c) the ethylene stream to the first zone, and/or the last ethylene stream to a zone, each comprises a controlled composition; and wherein each ethylene stream to a zone receives an output from two or more cylinders of the last compressor stage of a Hyper compressor system.


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