Graft polymers of polymerizable monomers and olefin polymers

• US 4,806,581 A
• Filed: 03/10/1987
• Issued: 02/21/1989
• Est. Priority Date: 10/12/1983
• Status: Expired due to Fees

• Current Assignee: Occidental Chemical Corporation (Occidental Petroleum Corporation)
• Original Assignee: Occidental Chemical Corporation (Occidental Petroleum Corporation)
• Inventors: Walker, Leigh E.
• Primary Examiner(s): SECCURO JR, CARMAN J
• Application Number:
  US07/024,197
• Time in Patent Office: 714 Days
• Field of Search: 525/317, 525/324, 525/322, 525/242, 525/290, 525/301, 525/302, 525/308, 524/178
• US Class Current: 524/178
• CPC Class Codes: C08F 2/02 Polymerisation in bulk
• CPC Class Codes: C08F 291/00 Macromolecular compounds obtained by polymerising monomers on to macromolecular compounds according to more than one of the groups C08F251/00 - C08F289/00

Abstract

Graft polymers are prepared by reacting an ethylenically unsaturated polymerizable monomer with a polymer of an olefin of 2 to about 8 carbon atoms in a process wherein the olefin polymer is substantially insoluble in the monomer but is capable of absorbing the monomer. In a preferred aspect, a vinyl halide polyolefin graft polymer is produced by reacting a solid polyolefin particle with a vinyl halide monomer in which the polyolefin is substantially insoluble, but is capable of absorbing the monomer. The solid particles can be contacted with the monomer in one step or in stages. When the stage-wise reaction is continued until the proportion of polyolefin in the polymer product is about 2 to about 20 weight percent, the resulting product can be formed to a transparent or translucent article. When a small proportion of solid polyolefin is employed in the polymerization process, both a graft polymer and a polymer of the unsaturated monomer are simultaneously produced in the same reactor and can be readily mechanically separated into the individual products.

Claims

1. A vinyl halide polyolefin graft polymer wherein the vinyl halide alone or in combination with up to 50 percent by weight based on the total weight of monomer of an ethylenically unsaturated compound copolymerizable therewith, and in the liquid state, is polymerized with a single polymer of an aliphatic hydrocarbon monoolefin of 2 to about 8 carbon atoms which is in the solid state in particulate form and is substantially insoluble in the monomer but absorbs a substantial amount of the monomer, and remains as a free flowing particle that does not agglomerate or fuse, wherein the proportion of monoolefin polymer in said graft polymer is about 20 to about 80 weight percent based on the weight of said monomer.

2. The graft polymer of claim 1 wherein the single polymer is an ethylene-propylene copolymer.

3. The graft polymer of claim 1 wherein the single polymer is an ethylene propylene polyene modified polymer.

4. The graft polymer of claim 1 wherein the single polymer is low density polyethylene.

5. The graft polymer of claim 1 wherein the single polymer is a copolymer comprising less than about 90 weight percent of an individual 1-olefin monomer.

6. The graft polymer of claim 1 wherein the single polymer is an ethylene copolymer comprising less than about 80 weight percent ethylene.

7. The graft polymer of claim 1 wherein the single polymer is a copolymer comprising about 30 to 75 weight percent of an individual 1-olefin monomer of 2 to 8 carbon atoms.

8. The graft polymer of claim 1 wherein the single polymer is an ethylene 1-olefin copolymer comprising about 30 to 75 weight percent of ethylene.

9. The graft polymer of claim 1 wherein the single polymer is an ethylene propylene copolymer comprising about 30 to 75 weight percent of ethylene.

10. The graft polymer of claim 1 wherein the single polymer is an ethylene propylene copolymer comprising about 50 to 75 weight percent of ethylene.

11. The graft polymer of claim 1 wherein the single polymer is a copolymer of ethylene and vinyl acetate.

12. The graft polymer of claim 1 wherein the single polymer is a copolymer of ethylene and methyl acrylate.

13. The graft polymer of claim 1 wherein the single polymer is a copolymer of ethylene and ethyl acrylate.

14. The graft polymer of claim 1 wherein the single polymer is a copolymer of ethylene and vinyl chloride.

15. The graft polymer of claim 1 wherein the single polymer is a copolymer of ethylene acrylic acid.

16. The graft polymer of claim 1 wherein the single polymer is a copolymer of ethylene and methacrylic acid.

17. The graft polymer of claim 1 wherein the single polymer is a copolymer comprising about 40 to 95 weight percent of a 1-olefin monomer and about 5 to 60 weight percent of a polar comonomer.

18. The graft polymer of claim 17 wherein the 1-olefin monomer is ethylene.

19. The graft polymer of claim 18 wherein the polar monomer is selected from vinyl acetate, methyl acrylate, ethyl acrylate, vinyl chloride, acrylic acid and methacrylic acid.

20. The graft polymer of claim 1 wherein the weight average molecular weight of the monoolefin polymer is in the range of about 10,000 to about 1,000,000.

21. The graft polymer of claim 1 wherein the weight average molecular weight of the monoolefin polymer is in the range of about 80,000 to about 300,000.

22. The graft polymer of claim 1 wherein the proportion of monoolefin polymer in said graft polymer is about 30 to about 50 weight percent based on the weight of said monomer.

23. The graft polymer of claim 1 prepared in a mass polymerization process.

24. The graft polymer of claim 1 prepared in a polymerization process in the presence of an inert diluent.

25. The graft polymer of claim 1 wherein in a polymerization process in the presence of water.

26. The graft polymer of claim 1 wherein the monomer is a single compound.

27. The graft polymer of claim 26 wherein the monomer is vinyl chloride.

28. The graft polymer of claim 1 wherein the monomer is two or more compounds.

29. The graft polymer of claim 28 wherein the monomer is a mixture of compounds.

30. The graft polymer of claim 29 wherein the vinyl halide is vinyl chloride.

31. The graft polymer of claim 28 wherein the monomers are reacted sequentially to the monoolefin polymer.

32. The graft polymer of claim 31 wherein vinyl chloride is first reacted with the monoolefin polymer, followed by methyl methacrylate.

33. The graft polymer of claim 1 and a stabilizer.

34. The graft polymer of claim 33 wherein the stabilizer is a dialkyltin maleate.

35. The graft polymer of claim 33 wherein the stabilizer is a dioctyltin maleate mixed with an alcohol.

36. A process for preparing a vinyl halide polyolefin graft copolymer which comprises:

(1) mixing a monomer component comprising vinyl halide alone or in combination with up to 50 percent by weight based on the total weight of monomer of an ethylenically unsaturated monomer copolymerizable therewith, in the liquid state, with a solid polyolefin comprising a single polymer of an aliphatic hydrocarbon monoolefin of 2 to about 8 carbon atoms, which polymer is in particulate form and substantially insoluble in the monomer or monomers, but absorbs a substantial amount of the monomer or monomers, and remains as a free flowing particle that does not agglomerate or fuse; and

an initiator, and

(2) heating the resulting mixture at a temperature in the range of about 30 to about 90 degrees Celsius.

37. The process of claim 36 wherein the proportion of monoolefin polymer in the graft polymer is about 20 to about 80 weight percent based on the weight of vinyl halide.

38. The process of claim 36 wherein the proportion of monoolefin polymer in the graft polymer is about 30 to about 50 weight percent based on the weight of vinyl halide.

39. The process of claim 36 conducted in a mass polymerization process.

40. The process of claim 36 conducted in the presence of an inert diluent.

41. The process of claim 36 conducted in the presence of water.

42. The process of claim 36 wherein a stabilizer is introduced at the beginning of the reaction.

43. The process of claim 42 wherein the stabilizer is a dialkyltin maleate.

44. The process of claim 43 wherein the stabilizer is a dioctyltin maleate mixed with an alcohol.

45. A process for producing a vinyl halide polyolefin graft copolymer which comprises reacting vinyl halide alone or in combination with up to 50 percent by weight based on the total weight of monomer of an ethylenically unsaturated monomer copolymerizable therewith, in the liquid state with a solid polyolefin of an aliphatic hydrocarbon monoolefin of 2 to about 8 carbon atoms in particulate form, that is substantially insoluble in the monomer but absorbs a substantial amount of the monomer, and remains as a free flowing particle that does not agglomerate or fuse, in the presence of an initiator for the reaction.

46. The process of claim 45 wherein the monomer is vinyl chloride.

47. The process of claim 45 wherein the proportion of monoolefin polymer in the polymer product is about 20 to about 80 weight percent based on the weight of said monomer.

48. The process of claim 45 wherein the proportion of monoolefin polymer in the polymer product is about 30 to about 50 weight percent based on the weight of said monomer.

49. The process of claim 45 conducted in a mass polymerization process.

50. The process of claim 45 conducted in the presence of an inert diluent.

51. The process of claim 45 conducted in the presence of water.

52. The process of claim 45 wherein a stabilizer is introduced at the beginning of the reaction.

53. The process of claim 52 wherein the stabilizer is a dialkyltin maleate.

54. The process of claim 52 wherein the stabilizer is a dioctyltin maleate mixed with an alcohol.

55. A process for preparing a vinyl halide polyolefin graft copolymer which comprises:

(1) mixing a monomer component comprising vinyl halide alone or in combination with up to 50 percent by weight based on the total weight of monomer of an ethylenically unsaturated monomer copolymerizable therewith, in the liquid state, with a solid polyolefin comprising a single polymer of an aliphatic hydrocarbon monoolefin of 2 to about 8 carbon atoms, wherein the polyolefin is in particulate form and substantially insoluble in the monomer or monomers, but absorbs a substantial amount of the monomer or monomers, and remains as a free flowing particle that does not agglomerate or fuse; and

an initiator, and

(2) heating the resulting mixture at a temperature in the range of about 30 to about 90 degrees Celsius,

(3) mixing additional monomer component with the product of step (2), and

(4) heating the resulting mixture at a temperature in the range of about 30 to about 90 degrees Celsius.

56. The process of claim 55 wherein the proportion of polyolefin in the polymer product of the process is in the range of about 20 to about 80 weight percent based on the weight of vinyl halide.

57. The process of claim 55 wherein the monomer of step (2) is different than the monomer of step (4).

58. The process of claim 57 wherein the polymer product of step (4) has a lighter color than the polymer product of step (2).

59. The process of claim 55 wherein the monomer of step (3) is different than the monomer of step (1).

60. The process of claim 55 wherein the polymer product of step (4) has a lighter color than the polymer product of step (2).

61. The process of claim 55 wherein steps (3) and (4) are repeated sequentially one or more times.