Conductive polyphenylene ether-polyamide blend
View Patent ↗The present invention relates to a thermoplastic resin composition and a method for making the same. The composition comprises the reaction product of about 10 wt % to about 50 wt % polyphenylene ether, about 35 wt % to about 65 wt % polyamide, preferably about 0.4 wt % to about 3.0 wt % carbon fibrils, and optionally about 5 wt % to about 40 wt % talc, up to about 10 wt % compatibilizing agent and up to about 20 wt % impact modifier. The method comprises forming a carbon masterbatch with polyamide and introducing the masterbatch and the polyamide subsequent to compounding the polyphenylene ether with a compatibilizing agent.
1. A method of manufacturing a thermoplastic resin composition comprising:
melt blending a first mixture comprising a polyphenylene ether, and a compatibilizing agent to form a first melt mixture;
adding a first polyamide, a carbon fibril masterbatch and a filler masterbatch to the first melt mixture and melt mixing to form a second melt mixture wherein the second melt mixture comprises based on the total weight of the second melt mixture, about 10 to about 50 wt % of the polyphenylene ether, about 35 to about 65 wt % of the polyamide, and about 0.4 to about 3 wt % of thin carbon fibrils.
2. The method of claim 1 wherein the carbon fibril masterbatch comprises carbon fibrils and a second polyamide.
3. The method of claim 2 wherein the second polyamide is a low viscosity polyamide.
4. The method of claim 1 wherein the first mixture further comprises an impact modifier.
5. A method for manufacturing a thermoplastic resin composition comprising:
melt blending a first mixture comprising a polyphenylene ether, an impact modifier, and a compatibilizing agent to form a first melt mixture;
adding a first polyamide, carbon fibril masterbatch and a filler masterbatch to the first melt mixture and melt mixing to form a second melt mixture wherein the second melt mixture comprises, based on the total weight of the second molt mixture, about 10 to about 50 wt % of the polyphenylene ether, about 35 to about 65 wt % of the polyamide, about 0.4 to about 3 wt % of the carbon fibrils and about 1 to about 15 wt % of the impact modifier.
6. The method according to claim 2 , wherein the carbon fibrils and the second polyamide are present in the masterbatch in a ratio of about 10 to about 30 wt. % of the carbon fibrils to about 90 to about 70 wt. % of the second polyamide.
7. The method according to claim 6 , wherein the ratio is about 15 to about 25 wt. % of the carbon fibrils to about 85 to about 75 wt. % of the second polyamide.
8. The method according to claim 1 , wherein the first polyamide has a viscosity of about 90 ml/g to about 350 ml/g, as measured in a 0.5 wt % solution in 96 wt % sulphuric acid in accordance with ISO 307.
9. The method according to claim 1 , wherein the filler masterbatch comprises talc and a third polyamide.
10. The method according to claim 9 , wherein the talc and the third polyamide are present in the masterbatch in a ratio of about 5 to about 50 wt. % of the talc to about 95 to about 50 wt. % of the third polyamide.
11. The method according to claim 1 , wherein the polyphenylene ether has an intrinsic viscosity of about 0.1 dl/g to about 0.60 dl/g, as measured in chloroform at 25 20 C.
12. The method according to claim 1 , wherein the compatibilizing agent is selected from the group consisting of liquid diene polymers, epoxy compounds, oxidized polyolefin wax, quinones, organosilane compounds, polyfunctional compounds, and combinations comprising at least one of the foregoing.
13. The method according to claim 4 , wherein the impact modifier is selected from the group consisting of A-B diblock copolymers, A-B-A triblock copolymers, partially hydrogenated A-B diblock copolymers, partially hydrogenated A-B-A triblock copolymers, selectively hydrogenated A-B diblock copolymers, selectively hydrogenated A-B-A triblock copolymers, and combinations comprising at least one of the foregoing.
14. The method according to claim 1 , wherein the first mixture further comprises additives.
15. The method according to claim 1 , wherein the polyphenylene ether comprises two polyphenylene ether components having different intrinsic viscosities.
16. The method according to claim 5 , wherein the carbon fibril masterbatch comprises about 10 to about 30 wt. % of the carbon fibrils and about 90 to about 70 wt. % of a second polyamide.
17. The method according to claim 16 , wherein the carbon fibril masterbatch comprises about 15 to about 25 wt. % of the carbon fibrils and about 85 to about 75 wt. % of the second polyamide.
18. The method according to claim 5 , wherein the filler masterbatch comprises about 5 to about 50 wt. % of talc and about 95 to about 50 wt. % of a third polyamide.
19. The method according to claim 5 , wherein the impact modifier is selected from the group consisting of A-B diblock copolymers, A-B-A triblock copolymers, partially hydrogenated A-B diblock copolymers, partially hydrogenated A-B-A triblock copolymers, selectively hydrogenated A-B diblock copolymers, selectively hydrogenated A-B-A triblock copolymers, and combinations comprising at least one of the foregoing.
20. The method according to claim 5 , wherein the first mixture further comprises additives.
21. The method according to claim 5 , wherein the polyphenylene ether comprises two polyphenylene ether components having different intrinsic viscosities.
22. The method according to claim 1 wherein the polyphenylene ether comprises a copolymer derived from copolymerization fo 2,6-dimethylphenol with 2,3,6-trimethylphenol.
23. method according to claim 5 wherein the polyphenylene ether comprises a copolymer derived from copolymerization fo 2,6-dimethylphenol with 2,3,6-trimethylphenol.
24. The method of claim 16 , wherein the second polyamide is a low viscosity polyamide.
25. The method of claim 18 , wherein the third polyamide is a low viscosity polyamide.