Branched polyphosphonates

• US 7,816,486 B2
• Filed: 02/24/2004
• Issued: 10/19/2010
• Est. Priority Date: 02/24/2003
• Status: Active Grant

• Current Assignee: FRX Polymers, Inc.
• Original Assignee: FRX Polymers, Inc.
• Inventors: Rice, Norman, Vinciguerra, Michael A., Lusignea, Richard, Freitag, Dieter
• Primary Examiner(s): Gulakowski; Randy
• Assistant Examiner(s): Fang; Shane
• Application Number:
  US10/546,668
• Publication Number:
  US 20070032633A1
• Time in Patent Office: 2,429 Days
• Field of Search: 528/398
• US Class Current: 528/398
• CPC Class Codes: C08G 79/04 Phosphorus linked to oxygen or to oxygen and carbon
• CPC Class Codes: C08L 2666/22 Macromolecular compounds not provided for in C08L2666/16 - C08L2666/20
• CPC Class Codes: C08L 67/00 Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain of polyester-amides C08L77/12; of polyester-imides C08L79/08; Compositions of derivatives of such polymers
• CPC Class Codes: C08L 85/02 containing phosphorus

Abstract

Disclosed are branched polyphosphonates produced using a polycondensation process, that result in polyphosphonates having a T_g of at least 100° C., and which can be further processed to have improved hydrolytic stability compared to other polyphosphonates. The method and polyphosphonate compositions may be made from readily available starting materials providing lower cost fire retardant materials. Also disclosed are polymer compositions that comprise these branched polyphosphonates and at least one other polymer, wherein the resulting polymer compositions exhibit flame retardant properties.

Claims

1. A method of making branched polyphosphonates comprising:

combining a phosphonium catalyst, phosphonic acid diaryl ester and bisphenol in a ratio to form a polyphosphonate to form a reaction mixture; and

heating said reaction mixture at a reduced pressure to form the polyphosphonate.

2. The method of claim 1, wherein said reaction mixture further comprises a branching agent.

3. The method of claim 1, wherein said bisphenol forms branching agent in situ.

4. The method of claim 1, wherein at least a portion of said phosphonium catalyst is removed during said heating.

5. The method of claim 1, wherein phosphonic acid diaryl ester and bisphenol are combined in a non-stoichiometric ratio.

6. The method of claim 1, wherein said bisphenol is a mixture of 2,2-bis(4-hydroxyphenyl) propane and a bisphenol of formula (XV):

7. The method of claim 1, wherein said heating is stopped when substantially all generated hydroxy aromatic compound is removed.

8. The method of claim 1, further comprising:

heating the polyphosphonate at reduced pressure in the presence of a removable phosphonium catalyst to form a hydrolytically stable polyphosphonate.

9. The method of claim 8, wherein less than 0.5 g of hydrolytically stable polyphosphonate is soluble in 100 ml volume of methylene chloride at about 23°

C.

10. The method of claim 8, wherein said polyphosphonate has a polydispersity of greater than about 2.3.

11. The method of claim 8, wherein said polyphosphonate comprises monomer derived units derived from 2,2-bis(4-hydroxyphenyl) propane.

12. The method of claim 8, wherein said phosphonium catalyst comprises tetraphenylphosphonium phenolate.

13. The method of claim 8, wherein at least a portion of the phosphonium catalyst is removed by the heating.

41. The method of claim 1, wherein the bisphenol is 2,2-bis(4-hydroxyphenyl) propane.

42. The method of claim 1, wherein the phosphonic acid diaryl ester comprises methyl-phosphonic acid diphenyl ester.

43. The method of claim 1, wherein the phosphonium catalyst is tetraphenylphosphonium phenolate.

44. The method of claim 8, wherein phosphonium catalyst is added to the polyphosphonate before heating.

14. A composition comprising:

a polyphosphonate 2,2-bis(4-hydroxyphenyl) propane comprising monomer derived units and having a T_g of at least 100°

C., a relative viscosity of greater than 1.1 when measured on a 0.5 percent solution in methylene chloride, an M_W of at least 10,000 g/mol, and a polydispersity of 2.3 or greater.

15. A composition comprising:

a polyphosphonate having a T_g of at least 100°

C. made by heating phosphonic acid diaryl ester and 2,2-bis(4-hydroxyphenyl) propane with a removable phosphonium catalyst at a reduced pressure.

16. The composition of claim 15, wherein said phosphonic acid diaryl ester comprises methyl-phosphonic acid diphenyl ester.

17. The composition of claim 15, further comprising bisphenols of formula (XV):

18. A composition comprising:

a polyphosphonate 2,2-bis(4-hydroxyphenyl) propane having derived repeat units, wherein said polyphosphonate has a T_g of at least 100°

C., a relative viscosity of greater than 1.15 when measured on a 0.5 percent solution in methylene chloride, an M_W of at least 15,000 g/mol, a polydispersity of 2.3 or greater, and which is hydrolytically stable.

19. A composition comprising:

a hydrolytically stable polyphosphonate having a T_g of at least 100°

C. made by heating at reduced pressure a polyphosphonate and a removable phosphonium catalyst.

20. The composition of claim 19, wherein less than 0.5 g of said hydrolytically stable polyphosphonate is soluble in 100 milliliters of methylene chloride at about 23°

C.

21. The composition of claim 19, wherein less than 5% degradation product are formed when the polyphosphonate is heated in boiling water for 6 hours.

22. The composition of claim 19, wherein said hydrolytically stable polyphosphonate is transparent.

23. The composition of claim 19, wherein said polyphosphonate comprises repeating units derived from 2,2-bis(4-hydroxyphenyl) propane.

24. A method for producing branched polyphosphonates, comprising:

combining one or more phosphonic acid diaryl ester, 2,2-bis(4-hydroxyphenyl) propane or a mixture of 2,2-bis(4-hydroxyphenyl) propane and other bisphenols, and a phosphonium catalyst to form a reaction mixture wherein said one or more phosphonic acid diaryl ester is in a stiochiometric equivalent amount or excess amount of said 2,2-bis(4-hydroxyphenyl) propane or 2,2-bis(4-hydroxyphenyl) propane and other bisphenols;

heating said mixture; and

removing phenol generated by the heating to form a polyphosphonate.

25. The method of claim 24, wherein said reaction mixture further comprises a branching agent.

26. The method of claim 24, wherein the number of moles of reactive groups of the phosphonic acid diaryl ester is within about ±

20% of the number of moles of reactive groups from said bisphenol.

27. The method of claim 24, wherein the phosphonium catalyst is tetraphenylphosphonium phenolate.

28. The method of claim 25, wherein the branching agent comprises 1,1,1-tris(4-hydroxyphenyl)ethane.

29. The method of claim 24, wherein the one or more phosphonic acid diaryl ester is of formula (XIII):

30. The method of claim 24, wherein the phosphonic acid diaryl ester comprises methyl-phosphonic acid diphenyl ester.

31. The method of claim 24, further comprising a phosphoric triaryl ester.

32. The method of claim 24, wherein said other bisphenols are of formula (XV):

33. The method of claim 24, wherein the other bisphenols are selected from 2,2-bis(3-chloro-4-hydroxyphenyl)propane;

2,2-bis(3-bromo-4-hydroxyphenyl)propane;

2,2-bis(4-hydroxy-3-isopropylphenyl)propane;

1,1-bis(4-hydroxyphenyl)cyclohexane;

1,1-bis(4-hydroxy-3-methylphenyl)cyclohexane;

4,4′

-dihydroxydiphenyl;

4,4′

-dihydroxydiphenylether;

4,4′

-dihydroxydiphenylsulfide;

4,4′

dihydroxydiphenylsulfone, 9,9-dihydroxy-diphenylfluorene;

1,1-bis(4-hydroxyphenyl)-3,3-dimethyl-5-methyl cyclohexane, or a combination of these.

34. A method of making polyphosphonates comprising:

heating a polyphosphonate and a phosphonium catalyst in a vessel to form a hydrolytically stable polyphosphonate.

35. A polyphosphonate prepared by a method comprising:

combining one or more phosphonic acid diaryl ester, 2,2-bis(4-hydroxyphenyl) propane or 2,2-bis(4-hydroxyphenyl) propane and other bisphenols, and a phosphonium catalyst wherein said phosphonic acid diaryl ester is in a stiochiometric equivalent amount or excess amount of said bisphenol to form a reaction mixture;

heating the reaction mixture at reduced pressure to form a polyphosphonate; and

removing material generated by the heating;

wherein the polyphosphonate exhibits a T_g of at least 100°

C.

36. The polyphosphonate of claim 35, wherein the polyphosphonate has a relative viscosity of at least 1.1 when measured on a 0.5 percent solution in methylene chloride at 23°

C., and a polymer dispersity of 2.3 or greater.

37. The polyphosphonate of claim 35, wherein the other bisphenols are selected from 2,2-bis(3-chloro-4-hydroxyphenyl)propane;

2,2-bis(3-bromo-4-hydroxyphenyl)propane;

2,2-bis(4-hydroxy-3-isopropylphenyl)propane;

1,1-bis(4-hydroxyphenyl)cyclohexane;

1,1-bis(4-hydroxy-3-methylphenyl)cyclohexane;

4,4′

-dihydroxydiphenyl;

4,4′

-dihydroxydiphenylether;

4,4′

-dihydroxydiphenylsulfide;

4,4′

dihydroxydiphenylsulfone, 9,9-dihydroxy-diphenylfluorene;

1,1-bis(4-hydroxyphenyl)-3,3-dimethyl-5-methyl cyclohexane, or a combination of these.

38. The polyphosphonate of claim 35, wherein the one or more phosphonic acid diaryl esters are of formula (XIII):

39. A composition comprising:

a polyphosphonate and a tetraphenylphosphonium catalyst in a reaction vessel heated at reduced pressure whereby a hydrolytically stable polyphosphonate is formed.

40. The composition of claim 39, wherein said polyphosphonate forms less than 5% degradation product when heated in boiling water for 6 hours.