IP Library Granted Patent US 8,865,041
Granted Patent B2
US 8,865,041 · App. 12/736,147 · Granted Oct 21, 2014

Extruder and process for extruding a polymer

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Quick Facts
Patent No.
US 8,865,041
App. No.
12/736,147
Granted
Oct 21, 2014
Kind
B2
Abstract

Process for extrusion of polymer by feeding a polymer feedstock to the feed port of an extruder having (i) two or more barrel sections arranged sequentially from (a) an upstream feed barrel section to which polymer feedstock to be extruded is fed, the upstream feed barrel section containing two screws each having a diameter of X, to (b) a downstream barrel section from which melted polymer is passed to a die and extruded, and (ii) a feed port for feeding polymer feedstock to be extruded into the extruder at its upstream end. The polymer feedstock is in the form of a powder, and the feed port area is a rectangular shape with width limited by the width of the upstream feed barrel section to 2*X and with a length greater than 2.5*X. The total area of the feed ports through which polymer feedstock is introduced is greater than 5*X 2 .

Claims (14)

1. A process for extrusion of polymer comprising feeding a polymer feedstock to a feed port of an extruder, said extruder comprising:

(i) two or more barrel sections arranged sequentially from:

(a) an upstream feed barrel section to which polymer feedstock to be extruded is fed, the upstream feed barrel section containing two screws each having a diameter of X; to

(b) a downstream barrel section from which melted polymer is passed to a die and extruded; and

(ii) the feed port for feeding polymer feedstock to be extruded into the extruder at its upstream end,

wherein (a) the polymer feedstock is a polymer of ethylene or propylene and is in the form of a powder having a flowability ratio of from at least 1 to less than 6, said flowability ratio of the polymer powder being measured using the instantaneous shear test described in ASTM D 6773-02 at a consolidation pressure of 2000 Pa and at a temperature that is equal to the temperature of the polymer powder at the feed port during the extrusion process,

(b) the diameter of the screws in the feed port barrel section of extruder is 200 mm or greater, and

(c) the feed port area is a rectangular shape with width limited by the width of the upstream feed barrel section to up to 2*X and with a length greater than 2.5*X and the total area of the feed port through which polymer feedstock is introduced is greater than 5*X 2 .

2. A process according to claim 1 wherein the polymer feedstock has a flowability ratio of less than 4.

3. A process according to claim 1 wherein the extruder comprises three or more barrel sections.

4. A process according to claim 1 wherein the extruder has a single feed port which has an area greater than 5*X 2 .

5. A process according to claim 1 wherein the total area of feed ports through which polymer is introduced is greater than 6*X 2 .

6. A process according to claim 1 wherein the ratio of the screw pitch to screw diameter within the upstream feed barrel section of the extruder is at least 1 and no greater than 2.5.

7. A process according to claim 2 wherein the polymer feedstock has a flowability ratio of less than 2.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 5, 2014
From: INEOS COMMERCIAL SERVICES UK LIMITED
To: INEOS SALES (UK) LIMITED
Reel/Frame 032388/0553 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 4, 2011
From: INEOS EUROPE LIMITED
To: INEOS COMMERCIAL SERVICES UK LIMITED
Reel/Frame 027060/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 15, 2010
From: PITMAN, GARY LINDSAY
To: INEOS EUROPE LIMITED
Reel/Frame 025003/0157 →