Thermoplastic molding compounds with an optimized residual monomer content

Patent metadata

Field	Value
Publication number	US-10189932-B2
Application number	US-201515307122-A
Country	US
Kind code	B2
Filing date	Apr 24, 2015
Priority date	Apr 30, 2014
Publication date	Jan 29, 2019
Grant date	Jan 29, 2019

Abstract

The present invention relates to a process for the production of styrene graft copolymers comprising addition and graft copolymerization of styrene monomers A1 and vinyl cyanide monomers A2 to a graft base B where the ratio by mass of A1 to A2 in the monomer feed at the end of the monomer feed time is lower than the ration by mass integrated over the entire monomer feed time. The present invention further relates to a graft copolymer obtainable by a process according to the invention, a molding composition comprising such a graft copolymer, and a molding obtained from such a molding composition.

First claim

What is claimed is:

1. A process for the production of styrene graft copolymers comprising the following steps:
(i) provision and agglomeration of the graft base B present in an emulsion;
(ii) addition of styrene monomers A1 and vinyl cyanide monomers A2 to the graft base B over a defined monomer feed time; and
(iii) simultaneous graft copolymerization of the added styrene monomers A1 and of the vinyl cyanide monomers A2 onto the agglomerated graft base B,
where, in step (ii), the ratio by mass of styrene monomers A1 to vinyl cyanide monomers A2 in the monomer feed at the end of the monomer feed time is lower than the ratio by mass of the components of the monomer feed integrated over the entire monomer feed time,
where step (iii) is followed by the following step (iv), which comprises:
(iv) addition of vinyl cyanide monomers A2 and graft copolymerization of these onto the agglomerated graft base B, where no styrene monomers A1 are added.

2. The process as claimed in claim 1 , where the graft base B is a rubber-containing graft base.

3. The process as claimed in claim 1 , where the styrene monomers A1 are selected from the group consisting of styrene, α-methylstyrene, C 1 -C 8 -alkyl-ring-sybstituted styrene, and mixtures of two or more thereof.

4. The process as claimed in claim 1 , where the vinyl cyanide monomers A2 are acrylonitrile, methacrylonitrile, or mixtures thereof.

5. The process as claimed in claim 1 , where the ratio by mass of styrene monomers A1 to vinyl cyanide monomers A2 integrated over the entire monomer feed time is from 50:50 to 95:5.

6. The process as claimed in claim 1 , where, in step (ii), the ratio by mass of styrene monomers A1 to vinyl cyanide monomers A2 in the monomer feed in the final fifth of the monomer feed time is lower by at least 10% than the ratio by mass integrated over the entire monomer feed time.

7. The process as claimed in claim 1 , where in step (ii), the ratio by mass of styrene monomers A1 to vinyl cyanide monomers A2 decreases progressively over the monomer feed time.

8. The process as claimed in claim 1 , where the ratio by mass of graft base B to graft shell made of styrene monomers A1 and of vinyl cyanide monomers A2 is from 80:20 to 20:80.

9. The process as claimed in claim 1 , where, after polymerization of the styrene monomers A1 and vinyl cyanide monomers A2, the resultant styrene graft copolymers are brought into contact with aqueous salt solution.

10. The process as claimed in claim 9 , where the unpolymerized vinyl cyanide monomers A2 are then removed from the aqueous salt solution, and the vinyl cyanide monomers A2 removed are optionally reused for addition in step (ii) or (iv).

11. A styrene graft copolymer obtainable by a process as claimed in claim 1 .

12. A molding composition comprising a styrene graft copolymer as claimed in claim 11 , and also at least one other thermoplastic polymer component.

13. The molding composition as claimed in claim 12 , where the molding composition also comprises at least one polycarbonate, at least one polyester, or at least one polyimide.

14. A molding obtained from a molding composition as claimed in claim 12 .

15. The process as claimed in claim 2 , where the graft base B comprises more than 50% by weight, based on solids content, of polybutadiene.

16. The process as claimed in claim 3 , where the styrene monomers A1 are styrene.

17. The process as claimed in claim 4 , where the vinyl cyanide monomers A2 are acrylonitrile.

18. The process as claimed in claim 5 , where the ratio by mass of styrene monomers A1 to vinyl cyanide monomers A2 integrated over the entire monomer feed time is from 70:30 to 85:15.

19. The process as claimed in claim 6 , where, in step (ii), the ratio by mass of styrene monomers A1 to vinyl cyanide monomers A2 in the monomer feed in the final fifth of the monomer feed time lower by at least 25% than the ratio by mass integrated over the entire monomer feed time.

20. The process as claimed in claim 8 , where the ratio by mass of graft base B to graft shell made of styrene monomers A1 and of vinyl cyanide monomers A2 is from 58:42 to 62:38.

Assignees

• Ineos Styrolution Group Gmbh

Inventors

• Walker Roland
• Michels Gisbert
• Banaszak Brian J

Classifications

• C08L25/12

  with unsaturated nitriles · CPC title

• C08L55/02

  ABS [Acrylonitrile-Butadiene-Styrene] polymers · CPC title

• C08F279/04 Primary

  Vinyl aromatic monomers and nitriles as the only monomers · CPC title

• C08F279/02 Primary

  on to polymers of conjugated dienes · CPC title

• C08F212/08

  Styrene · CPC title