IP Library Granted Patent US 8,648,148
Granted Patent B2
US 8,648,148 · App. 11/992,875 · Granted Feb 11, 2014

Low gloss mass polymerized rubber-modified monovinylidene aromatic copolymer composition

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Quick Facts
Patent No.
US 8,648,148
App. No.
11/992,875
Granted
Feb 11, 2014
Kind
B2
Abstract

Disclosed is a mass polymerized rubber-modified monovinylidene aromatic copolymer composition with an excellent balance of aesthetic, physical and mechanical properties, in particular good impact with low consistent gloss across an injection molded textured part, and a method for preparing such a composition.

Claims (40)

1. A mass polymerized rubber-modified monovinylidene aromatic copolymer composition comprising:

(i) a continuous matrix phase comprising a copolymer of a monovinylidene aromatic monomer and an ethylenically unsaturated nitrile monomer and a comonomer that is N-phenyl malelmide having a weight average molecular weight of equal to or less than 150 kg/mole and

(ii) a rubber component dispersed as discrete rubber particles in the matrix comprising polybutadiene content of at least 12 weight percent as determined by infrared analysis,

wherein the rubber-modified monovinylidene aromatic copolymer has a storage modulus (G′) of between 2,000 to 5,000 Pascals, and has an average rubber particle size between 1.5 to 2 microns as determined by Coulter Counter, wherein when the composition is molded or extruded it exhibits a tensile modulus of at least 1,400 MPa as determined by ISO 527-2, and a notched Charpy at 23° C as determined by DIN 53453 of at least 11 kJ/m 2 , and a delta grain gloss of between 0.3 and 0.9 as determined by 60° Gardner gloss by ISO 2813.

2. The mass polymerized rubber-modified monovinylidene aromatic copolymer composition of claim 1 wherein the ethylenically unsaturated nitrile is from about 10 to about 35 weight percent of the copolymer.

3. The mass polymerized rubber-modified monovinylidene aromatic copolymer composition of claim 1 wherein the monovinylidene aromatic monomer is styrene and the ethylenically unsaturated nitrile monomer is acrylonitrile.

4. The mass polymerized rubber-modified monovinylidene aromatic copolymer composition of claim 1 wherein:

(iii) the copolymer is present in an amount from about 60 to 90.5 weight percent and

(iv) the rubber component is present in an amount from about 40 to 9.5 weight percent,

wherein weight percents are based on the total weight of the rubber-modified monovinylidene aromatic copolymer.

5. The mass polymerized rubber-modified monovinylidene aromatic copolymer composition of claim 1 wherein the polybutadiene rubber comprises a 1,3-butadiene homopolymer.

6. The mass polymerized rubber-modified monovinylidene aromatic copolymer composition of claim 1 wherein the rubber component comprises a styrene and 1,3-butadiene block copolymer rubber.

7. The mass polymerized rubber-modified monovinylidene aromatic copolymer composition or claim 1 Wherein the rubber particles have an average particle size from about 1.5 micrometers to about 1.9 micrometers.

8. The mass polymerized rubber-modified monovinyildene aromatic copolymer composition of claim 1 wherein the rubber particles have an average particle size from about 1.6 micrometers to about 2 micrometers.

9. The mass polymerized rubber-modified monovinylidene aromatic copolymer composition of claim 1 wherein the G′ is between 2,000 to 4,500 Pascals.

10. The mass polymerized rubber-modified monovinylidene aromatic copolymer composition of claim 1 wherein continuous matrix phase has a weight average molecular weight of equal to or less than 135 kg/mole.

11. The mass polymerized rubber-modified monovinylidene aromatic copolymer composition of claim 1 further comprising a polycarbonate resin.

12. The mass polymerized rubber-modified monovinylidene aromatic copolymer composition of claim 11 is a polycarbonate PC)/acrylonitrlle-butadiene-styrene (ASSABS) blend.

13. A method for preparing a mass polymerized rubber-modified monovinylidene aromatic copolymer composition comprising the steps of:

(a) polymerizing by bulk, mass-solution or mass-suspension polymerization techniques in the presence of a dissolved rubber component a monovinylidene aromatic monomer and an ethylenically unsaturated nitrile monomer and a comonomer that is N-phenylmaeimide, optionally in the presence of an inert solvent, forming a continuous matrix phase to the desired degree of conversion wherein

(i) the continuous matrix phase has a weight average molecular weight of equal to or less than 150 kg/mole and

(ii) the rubber component is dispersed as discrete rubber particles in the matrix comprising a polybutadiene content of at least 12 weight percent as determined by infrared analysis,

(b) subjecting the resultant mixture to conditions sufficient to remove any unreacted monomers and to cross-link the rubber, and

(c) isolating the rubber-modified monovinylidene aromatic copolymer composition,

wherein the rubber-modified monovinylidene aromatic copolymer has a storage modulus (G′) of between 2,000 to 5,000 Pascals, the average rubber particle size is between 1.5 to 2 microns as determined by Coulter Counter, a tensile modulus of at least 1,400 MPa as determined by ISO 527-2, and a notched Charpy at 23° C. as determined by DIN 53453 of at least 11 KJ/m 2 and a delta grain gloss of between 0.3 and 0.9 as determined by 60° Gardner gloss by ISO 2813.

14. The method of claim 13 wherein the monovinylidene aromatic monomer is styrene and the ethylenically unsaturated nitrile monomer is acrylonitrile.

15. A method for producing a molded or extruded article of a mass polymerized rubber-modified monovinylidene aromatic copolymer composition comprising the steps of:

(A) preparing a mass polymerized rubber-modified monovinylidene aromatic copolymer composition by:

(a) polymerizing by bulk, mass-solution or mass-suspension polymerization techniques in the presence of a dissolved rubber component a monovinylidene aromatic monomer and an ethylenically unsaturated nitrile monomer and a comonomer of N-phenyl maleimide, optionally in the presence of an inert solvent, forming a continuous matrix phase to the desired degree of conversion wherein

(i) the continuous matrix phase has a weight average molecular weight of equal to or less than 150 kg/mole and

(ii) the rubber component is dispersed as discrete rubber particles in the matrix comprising a polybutadiene content of at least 12 weight percent as determined by infrared analysis,

(b) subjecting the resultant mixture to conditions sufficient to remove any unreacted monomers and to cross-link the rubber, and

(c) isolating the rubber-modified monovinylidene aromatic copolymer composition,

wherein the rubber-modified monovinylidene aromatic copolymer has a storage modulus (G′) of between 2,000 to 5,000 Pascals, the average rubber particle size is between 1.5 to 2 microns as determined by Coulter Counter, a tensile modulus of at least 1,400 MPa as determined by ISO 527-2, and a notched Charpy at 23° C. as determined by DIN 53453 of at least 11 kJ/m 2 and a delta grain gloss of between 0.3 and 0.9 as determined by 60° Gardner gloss by ISO 2813; and

(B) molding or extruding said rubber-modified monovinyllidene aromatic copolymer composition into a molded or extruded article.

16. The method of claim 15 wherein the molded or extruded article is an automotive part, an information technology equipment part, or a sheet.

17. The composition of claim 1 in the form of a molded or extruded article.

18. The molded or extruded article of claim 17 is an automotive part, an information technology equipment part, or a sheet.

19. The composition of claim 1 , wherein the continuous matrix phase is obtained from polymerization with a chain transfer agent selected from the group consisting of mercaptans and thiols.

20. The composition of claim 19 , wherein the chain transfer agent is n-dodecylmercaptan.

Assignments (15)
PATENT SECURITY AGREEMENT Recorded Apr 27, 2026
From: TRINSEO EUROPE GMBH
To: ALTER DOMUS (US) LLC
Reel/Frame 075480/0402 →
PATENT SECURITY AGREEMENT Recorded Sep 6, 2017
From: TRINSEO EUROPE GMBH
To: DEUTSCHE BANK AG NEW YORK BRANCH, AS COLLATERAL AGENT
Reel/Frame 043773/0138 →
TERMINATION AND RELEASE OF SECURITY INTEREST IN PATENTS RECORDED AT REEL 036303, FRAME 0749 Recorded Sep 6, 2017
From: DEUTSCHE BANK AG NEW YORK BRANCH
To: TRINSEO EUROPE GMBH
Reel/Frame 043773/0059 →
PATENT SECURITY AGREEMENT Recorded Aug 6, 2015
From: TRINSEO EUROPE GMBH
To: DEUTSCHE BANK AG NEW YORK BRANCH, AS COLLATERAL AGENT
Reel/Frame 036303/0749 →
CHANGE OF NAME Recorded Jun 25, 2015
From: STYRON EUROPE GMBH
To: TRINSEO EUROPE GMBH
Reel/Frame 036024/0806 →
CHANGE OF NAME Recorded Jun 12, 2015
From: STYRON EUROPE GMBH
To: TRINSEO EUROPE GMBH
Reel/Frame 036007/0670 →
TERMINATION AND RELEASE OF SECURITY INTEREST IN PATENTS Recorded May 21, 2015
From: DEUTSCHE BANK AG NEW YORK BRANCH
To: STYRON EUROPE GMBH
Reel/Frame 035751/0001 →
SECURITY AGREEMENT Recorded Jan 28, 2011
From: STYRON EUROPE GMBH
To: DEUTSCHE BANK AG NEW YORK BRANCH
Reel/Frame 025709/0681 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 11, 2010
From: STYRON LLC
To: STYRON EUROPE GMBH
Reel/Frame 025118/0681 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 15, 2010
From: THE DOW CHEMICAL COMPANY; DOW GLOBAL TECHNOLOGIES INC.
To: STYRON LLC
Reel/Frame 024686/0395 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 12, 2010
From: THE DOW CHEMICAL COMPANY; DOW GLOBAL TECHNOLOGIES INC.
To: STYRON LLC
Reel/Frame 024672/0019 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 4, 2009
From: DOW BENELUX B.V.
To: THE DOW CHEMICAL COMPANY
Reel/Frame 023194/0796 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 4, 2009
From: THE DOW CHEMICAL COMPANY
To: DOW GLOBAL TECHNOLOGIES INC.
Reel/Frame 023194/0832 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 4, 2009
From: JONES, MARY A.; TRAUGOTT, THOMAS D.
To: DOW GLOBAL TECHNOLOGIES INC.
Reel/Frame 023194/0859 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 4, 2009
From: SHIELDS, NIGEL; MAES, DOMINIQUE
To: DOW BENELUX B.V.
Reel/Frame 023194/0767 →