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:
Jul. 27, 2021

Filed:

Jun. 26, 2018
Applicant:

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

Inventors:

Cornelis J F Hosman, Ijzendijke, NL;

Nhi T. Y. Dang, Terneuzen, NL;

Assignee:

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

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C08F 10/02 (2006.01); C08F 2/01 (2006.01); B01J 4/00 (2006.01); B01J 19/00 (2006.01); B01J 19/24 (2006.01);
U.S. Cl.
CPC ...
C08F 10/02 (2013.01); B01J 4/001 (2013.01); B01J 19/0013 (2013.01); B01J 19/2415 (2013.01); C08F 2/01 (2013.01); B01J 2204/002 (2013.01);
Abstract

A process to form an ethylene-based polymer in a reactor system, said process comprising at least the following steps: a) injecting a first initiator mixture into the tubular reactor at location L along the reactor, b) injecting a compressed make-up CTA system at the location L, at a distance (L−L) from 145*Dto 1000*D, upstream from L, and wherein D=the inner diameter of the pre-heater in meter (m); and wherein Lis located in the preheater, and c) optionally, injecting one or more additional compressed make-up CTA system(s) into the preheater, at one or more location: LL, L(2≤i and 2≤n), upstream from L, and each location is, independently, at a distance from 145*Dto 1000*D, and wherein n equals the total number of injection locations of the make-up CTA system(s) injected into the preheater, upstream from L, and wherein (L−L) is less than each (L−L), (L−L), (L−L); and d) polymerizing a reaction mixture comprising at least ethylene, the first initiator mixture, and the compressed make-up CTA system of step b), and wherein the process has a log coefficient of variation (log(CoV)), at L, that meets the relationships described herein.


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