IP Library Granted Patent US 8,574,478
Granted Patent B2
US 8,574,478 · App. 12/562,337 · Granted Nov 5, 2013

Slip additive composition in thermoplastic polymer processing

Inventors: Steven Burgess Tattum (Grimsargh, GB); Matthew Jackson (Warrington, GB)
Assignee: Colormatrix Europe Limited
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Quick Facts
Patent No.
US 8,574,478
App. No.
12/562,337
Granted
Nov 5, 2013
Kind
B2
Abstract

The present invention relates to the use of a fatty acid ester as a slip additive in the production of molded polyethylene terephthalate articles, to a thermoplastic molding composition comprising a polyethylene terephthalate and a fatty acid ester selected to be effective for reducing the co-efficient of friction of molded articles formed from the composition, to a molded polyethylene terephthalate article comprising a fatty acid ester selected to be effective in reducing the co-efficient of friction of the molded article, and to a process for producing a molded thermoplastic article comprising providing a thermoplastic molding composition comprising polyethylene terephthalate, admixing with the thermoplastic molding composition at least one fatty acid ester selected to be effective in reducing the co-efficient of friction of the molded article, heating the composition and molding the hot composition so as to form a molded article.

Claims (27)

1. A method of using a fatty acid ester as a slip additive in a thermoplastic moulding composition in the production of colourless moulded polyethylene terephthalate articles in the form of bottle preforms, the method comprising incorporating said fatty acid ester into a bottle preform moulded from polyethylene terephthalate, said slip additive reducing the coefficient of friction of the preform, wherein the fatty acid ester is selected from the group consisting of:

(a) acetylated glycerol fatty acid esters;

(b) sorbitan fatty acid esters; and

(c) refined rapeseed oil, montanic acid triglyceride, PEG-400 dilaurate, PEG-200 dioleate, acetylated triglyceride, and mixtures of two or more thereof;

wherein the moulded polyethylene terephthalate articles in the form of bottle preforms are colourless; and

wherein the thermoplastic moulding composition does not comprise a fatty amide.

2. A method according to claim 1 , wherein the fatty acid ester is colourless.

3. A method according to claim 1 wherein the fatty acid ester is selected from acetylated glycerol fatty acid esters.

4. A method according to claim 3 , wherein the acetylated glycerol fatty acid ester is ethoxylated glycerol monostearate.

5. A method according to claim 1 , wherein the fatty acid ester is selected from sorbitan fatty acid esters.

6. A method according to claim 5 , wherein the sorbitan fatty acid ester is selected from sorbitan monolaurate, sorbitan monooleate, sorbitan monopalmitate, sorbitan monostearate, and mixtures of two or more thereof.

7. A method according to claim 1 , wherein the fatty acid ester is selected from refined rapeseed oil, montanic acid triglyceride, PEG-400dilaurate, PEG-200 dioleate, acetylated triglyceride, and mixtures of two or more thereof.

8. A method according to claim 1 wherein the fatty acid ester is present in the moulding composition in an amount effective to reduce the coefficient of friction of a moulded article formed from the moulding composition by at least 25% relative to the coefficient of friction of a corresponding moulded article formed from the moulding composition in the absence of the slip additive.

9. The method according to claim 1 , wherein said fatty acid ester is a long chain fatty acid ester wherein the chain length is at least 12.

10. The method according to claim 1 , wherein said fatty acid ester is a long chain fatty acid ester wherein the chain length is twelve to eighteen.

11. The method according to claim 1 , wherein the amount of slip additive included in the thermoplastic moulding composition from which a said moulded article is produced is at least 0.1% w/w.

12. The method according to claim 11 , wherein the amount of slip additive is at least 0.3% w/w.

13. The method according to claim 12 , wherein the amount of slip additive is at least 0.4% w/w.

14. The method according to claim 13 wherein the amount of slip additive is no more than 0.5% w/w.

15. The method according to claim 1 , wherein said slip additive is able to withstand injection moulding at a temperature in the range 260° C. to 310° C.

16. The method of claim 1 , wherein the thermoplastic moulding composition does not comprise an oxygen scavenger.

17. The method according to claim 1 , wherein said fatty acid ester is admixed with said polyethylene terephthalate.

18. A method of using a slip additive in a thermoplastic moulding composition in the production of moulded polyethylene terephthalate articles in the form of bottle preforms, the method comprising incorporating said slip additive into a bottle preform moulded from polyethylene terephthalate, said slip additive reducing the coefficient of friction of the preform, wherein the slip additive comprises a fatty acid ester and a further slip agent, wherein said fatty acid ester is selected from the group consisting of:

(a) acetylated glycerol fatty acid esters;

(b) sorbitan fatty acid esters; and

(c) refined rapeseed oil, montanic acid triglyceride, PEG-400 dilaurate, PEG-200dioleate, acetylated triglyceride, and mixtures of two or more thereof; and

wherein said further slip agent is a mineral oil.

Assignments (2)
RELEASE OF SECURITY INTEREST Recorded Dec 29, 2011
From: GE CORPORATE FINANCE BANK SAS, AS AGENT
To: COLORMATRIX EUROPE LIMITED
Reel/Frame 027802/0644 →
AMENDMENT TO PATENT SECURITY AGREEMENT Recorded Apr 22, 2011
From: COLORMATRIX EUROPE LIMITED
To: GE CORPORATE FINANCE BANK SAS, AS AGENT
Reel/Frame 026167/0758 →
Priority Claims (1)
GB 0321131.5 · Sep 10, 2003 · national
Continuity (2)
Continuation 10571477 · Mar 10, 2006
Related Publication 20100076127A1 · Mar 25, 2010