IP Library Granted Patent US 11,555,116
Granted Patent B2
US 11,555,116 · App. 17/041,326 · Granted Jan 17, 2023

Use of a copolymer of ethylene and of acrylate(s) prepared in a tubular reactor for modifying the melt rheology of a thermoplastic composition

Inventors: Paul Coupillaud (Serquigny, FR); Sebastien Quinebeche (Serquigny, FR); Alain Bouilloux (Serquigny, FR)
Assignee: SK Global Chemical Co., Ltd.
C08L77/02B29C45/0001B29C48/022C08F2/01C08F220/1804C08L23/08C08L2207/04
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Quick Facts
Patent No.
US 11,555,116
App. No.
17/041,326
Granted
Jan 17, 2023
Kind
B2
Abstract

Provided herein is a copolymer of ethylene and acrylate(s) having a melt flow index (MFI) greater than or equal to 50 g/10 minutes, obtained by free-radical copolymerisation under high pressure carried out in a tubular reactor, and methods of using the same. Also provided herein is a thermoplastic composition, particularly intended to be extruded or injection moulded, having one or more copolymers of ethylene and acrylate(s) at a content ranging from 0.1 to 20 wt. %, and one or more thermoplastic polymers.

Claims (21)

1. A thermoplastic composition comprising:

at least one thermoplastic polymer; and

at least one copolymer of an ethylene and one or more acrylates, obtained by a process of free-radical copolymerisation under high pressure performed in a tubular reactor, in a content ranging from 0.1 wt. % to 20 wt. % calculated relative to the total weight of the composition, the copolymer having a melt flow index (MFI) greater than or equal to 50 g/10 minutes measured at a temperature of 190° C. under a load of 2160 g.

2. The composition according to claim 1 , wherein the thermoplastic polymer is selected from the group consisting of polyamides, polyesters, polycarbonates, phenylene polysulfides, polyacetals and mixtures thereof.

3. The composition according to claim 2 , wherein the thermoplastic polymer is a polyamide.

4. A process of preparing a thermoplastic composition comprising mixing:

at least one thermoplastic polymer; and

at least one copolymer of an ethylene and one or more acrylates, obtained by a process of free-radical copolymerisation under high pressure performed in a tubular reactor, in a content ranging from 0.1 wt. to 20 wt. % calculated relative to the total weight of the mixture, the copolymer having a melt flow index (MFI) greater than or equal to 50 g/10 minutes measured at a temperature of 190° C. under a load of 2160 g.

5. The process according to claim 4 , wherein the mixing step is an extrusion step.

6. A process for modifying melt rheology of a thermoplastic composition, comprising adding to the thermoplastic composition a copolymer of an ethylene and one or more acrylates, obtained by a process of free-radical copolymerisation under high pressure performed in a tubular reactor, the copolymer having a melt flow index (MFI) greater than or equal to 50 g/10 minutes measured at a temperature of 190° C. under a load of 2160 g.

7. The process according to claim 6 , wherein the copolymer has a melt flow index (MFI) varying from 300 to 600 g/10 minutes.

8. The process according to claim 6 , wherein the one or more acrylates are selected from the group consisting of alkyl (meth)acrylates, arylalkyl (meth)acrylates and (meth)acrylates.

9. The process according to claim 8 , wherein the alkyl (meth)acrylate comprises a C 1 -C 30 alkyl (meth)acrylate.

10. The process according to claim 8 , wherein the (meth)acrylate comprises an epoxy group.

11. The process according to claim 6 , wherein the acrylate is selected from the group consisting of methyl acrylate, butyl acrylate, ethyl-2-hexyl acrylate, and mixtures thereof.

12. The process according to claim 6 , wherein the copolymer is a copolymer of ethylene and butyl acrylate.

13. The process according to claim 6 , wherein content by weight of the ethylene ranges from 50 wt. % to 95 wt. % relative to the total weight of the copolymer.

14. The process according to claim 6 , wherein the content by weight of the ethylene ranges from 55 wt. % to 80 wt. % relative to the total weight of the copolymer.

15. The process according to claim 6 , wherein the content by weight of the one or more acrylates ranges from 5 wt. % to 50 wt. % relative to the total weight of the copolymer.

16. The process according to claim 6 , wherein the content by weight of the one or more acrylates ranges from 15 wt. % to 40 wt. % relative to the total weight of the copolymer.

17. The process according to claim 6 , wherein the copolymer increases melt fluidity of the thermoplastic composition.

Assignments (3)
CHANGE OF ADDRESS Recorded Jul 10, 2023
From: SK GEO CENTRIC CO., LTD.
To: SK GEO CENTRIC CO., LTD.
Reel/Frame 064236/0095 →
CHANGE OF NAME Recorded Jul 10, 2023
From: SK GLOBAL CHEMICAL CO., LTD.
To: SK GEO CENTRIC CO., LTD.
Reel/Frame 064236/0105 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 6, 2022
From: COUPILLAUD, PAUL; QUINEBECHE, SEBASTIEN; BOUILLOUX, ALAIN
To: SK GLOBAL CHEMICAL CO., LTD.
Reel/Frame 061994/0062 →
Priority Claims (1)
FR 1852598 · Mar 26, 2018 · national
Continuity (1)
Related Publication 20210163739A1 · Jun 3, 2021