IP Library Granted Patent US 8,367,783
Granted Patent B2
US 8,367,783 · App. 12/295,855 · Granted Feb 5, 2013

Process for improving the polymerization of ethylene and one or more optional comonomer(s) in a polymerization loop reactor

Inventor: Daan Dewachter (Mechelen, BE)
Assignee: Total Petrochemicals Research Feluy
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Quick Facts
Patent No.
US 8,367,783
App. No.
12/295,855
Granted
Feb 5, 2013
Kind
B2
Abstract

The present invention relates to a process for improving the polymerization of ethylene and one or more optional co-monomer(s) in a polymerization loop reactor characterized in that said process comprises the step of controlling the hydrogen/monomer ratio along the path of the reactor by multiple, spatially separated, feeding of hydrogen along the path of the loop reactor. In particular, the invention provides a process for controlling, and preferably narrowing, the molecular weight distribution of the produced polymer particles. In another aspect, the invention relates to a polymerization loop reactor suitable for the polymerization process of ethylene and an optional olefin co-monomer, wherein the molecular weight distribution of the produced ethylene polymer can be controlled.

Claims (9)

1. A process for the polymerization of ethylene monomer comprising:

feeding ethylene monomer, one or more optional olefin co-monomers and a diluent into a double loop reactor comprising a first loop reactor and a second loop reactor arranged in series;

controlling a hydrogen:monomer ratio along a path of a loop reactor by feeding hydrogen into the loop reactor at multiple, spatially separated points disposed along the path of the loop reactor;

reducing the variation in the hydrogen:monomer ratio between the ratio at the reactor inlet and the ratio at the reactor outlet to a variation that is lower than 40%;

polymerizing the ethylene monomer and the optional co-monomers to produce a polymer slurry comprising essentially liquid diluent and solid ethylene polymer particles; and

discharging the polymer slurry out of the double loop reactor.

2. The process of claim 1 , wherein the hydrogen:monomer ratio is controlled in the first loop reactor, the second loop reactor or combinations thereof.

3. The process of claim 1 , wherein the multiple, spatially separated points are disposed at equidistant points along the path of the loop reactor.

4. The process of claim 1 , wherein the polymerization catalyst comprises a metallocene catalyst.

Assignments (3)
CHANGE OF NAME Recorded Oct 17, 2014
From: TOTAL PETROCHEMICALS RESEARCH FELUY
To: TOTAL RESEARCH & TECHNOLOGY FELUY
Reel/Frame 034013/0808 →
CORRECTIVE ASSIGNMENT TO CORRECT THE ATTY. DKT. NO. SHOULD BE F-990 ASSIGNOR: SHOULD BE DEWACHTER, DAAN PREVIOUSLY RECORDED ON REEL 025166 FRAME 0951. ASSIGNOR(S) HEREBY CONFIRMS THE ATTY. DKT. NO. F-992; ASSIGNOR: RIBOUR, DAVID; SPITZ, ROGER; GROMADA, JEROME IS THE INCORRECT INFORMATION. Recorded Jan 18, 2011
From: DEWACHTER, DAAN
To: TOTAL PETROCHEMICALS RESEARCH FELUY
Reel/Frame 025647/0923 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 20, 2010
From: RIBOUR, DAVID; SPITZ, ROGER; GROMADA, JEROME
To: TOTAL PETROCHEMICALS RESEARCH FELUY
Reel/Frame 025166/0951 →
Priority Claims (1)
EP 06112155 · Apr 3, 2006 · regional
Continuity (1)
Related Publication 20090326170A1 · Dec 31, 2009