Process for preparing dynamically vulcanized alloys

Patent metadata

Field	Value
Publication number	US-9546251-B2
Application number	US-201514682784-A
Country	US
Kind code	B2
Filing date	Apr 9, 2015
Priority date	Dec 20, 2012
Publication date	Jan 17, 2017
Grant date	Jan 17, 2017

Abstract

This invention relates to the preparation of a dynamically vulcanized alloy comprising at least one elastomer and at least one thermoplastic resin, having a G′ at 1% strain and 100° C. as determined according to ASTM D7605 of about 4,500 to about 7,500 kPa. More specifically, the process produces dynamically vulcanized alloys with unique morphological features which have good impermeability and low temperature flexibility. In the process, the thermoplastic resin is added into the extruder in two stages with an intermediate addition of a compatibilizer. Also during the final addition of thermoplastic resin, the elastomeric curatives are added to the extruder.

First claim

What is claimed is:

1. A process for producing a dynamically vulcanized alloy, the alloy comprising at least one elastomer and at least one thermoplastic resin, the process comprising the following consecutive steps of:
a) feeding the elastomer and a first portion of the thermoplastic resin into the initial feed throat of an extruder;
b) mixing the elastomer and the first portion of thermoplastic resin;
c) feeding a compatibilizer into the extruder;
d) mixing the elastomer, the first portion of thermoplastic resin, and the compatibilizer to begin interfacial grafting of the elastomer with the thermoplastic resin without any significant curing of the elastomer;
e) feeding a second portion of the thermoplastic resin into the extruder; and
f) subsequent to the interfacial grafting, mixing the contents of the extruder under shear conditions to mix and cure the elastomer until the elastomer is dispersed as particles in a matrix of the thermoplastic resin and the elastomer particles achieve at least 80% cure forming a dynamically vulcanized alloy wherein the average elastomeric particle size for the majority of the elastomeric particles is defined by a diameter in the range of 100 to 1,000 nanometers;
wherein the alloy has an elastomer shear modulus, G′, at 1% strain and 100° C. as determined according to ASTM D7605 of about 4,500 to about 7,500 kPa.

2. The process as claimed in claim 1 , wherein said elastomer is added directly into the feed throat without any prior mixing of the elastomer with any other components of the dynamically vulcanized alloy.

3. The process as claimed in claim 1 , wherein at least one curative is fed into the extruder with the second portion of the thermoplastic resin.

4. The process as claimed in claim 3 , further comprising the step of pelletizing the at least one curative with portions of the second portion of thermoplastic resin prior to feeding the curative into the extruder, wherein the amount of the curative added is about 2 to about 3 phr based on the alloy.

5. The process as claimed in claim 1 , wherein after step e) and after initiation of cure of the elastomer particles, additional compatibilizer or at least one viscosity modifier is fed into the extruder.

6. The process as claimed in claim 1 , wherein during step a), c), or e) at least one stabilizer is also fed into the extruder.

7. The process as claimed in claim 1 , wherein the second portion of thermoplastic resin added in step e) is 10 to 75 wt % of the total thermoplastic resin in the alloy.

8. The process as claimed in claim 1 , wherein the second portion of thermoplastic resin is fed into the extruder at a location anywhere between 30% to 60% of an L/D ratio of the extruder wherein L is the screw length of the extruder and D is the maximum bore width of the extruder barrel.

9. The process as claimed in claim 1 , further comprising the step of feeding a secondary elastomer into the initial feed throat of the extruder.

10. The process of claim 9 , wherein the secondary elastomer is maleic anhydride-modified copolymer.

11. The process as claimed in claim 1 , wherein the thermoplastic resin is selected from the group consisting of polyamides, polyimides, polycarbonates, polyesters, polysulfonates, polyactones, polyacetals, acrylonitrile-butadiene-styrene resins, polyphenyleneoxide, polyphenylene sulfide, polystyrene, styrene-acrylonitrile resins, styrene maleic anhydride resins, aromatic polyketones, and mixtures thereof.

12. The process as claimed in claim 1 , wherein the thermoplastic resin is a polyamide selected from the group consisting of nylon-6, nylon-12, nylon-6,6, nylon-6,9, nylon-6,10, nylon-6,12, nylon 6,66 copolymer, nylon-11, and mixtures thereof.

13. The process as claimed in claim 1 , wherein the elastomer is an isobutylene derived elastomer.

14. The process as claimed in claim 1 , wherein the elastomer is a copolymer of an isobutylene and an alkystyrene.

15. The process as claimed in claim 1 , wherein the elastomer is present in the alloy in an amount in the range of from about 2 to about 90 wt % based on the total alloy blend weight or the thermoplastic resin is present in the alloy in an amount in the range of from 10 to 98 wt % based on the total alloy blend weight.

16. The process as claimed in claim 1 , wherein the thermoplastic resin is present in the alloy in an amount of 40 to 80 phr.

17. The process as claimed in claim 1 , wherein the alloy has an elastic stiffness modulus, S′, at 200% strain and 215° C. as determined according to ASTM D7605 of about 4 to about 7 dNm.

18. The process as claimed in claim 1 , wherein the extruder temperature is reduced by 5° to 50° C. after the second portion of the thermoplastic resin is fed into the extruder.

19. A film formed from a dynamically vulcanized alloy manufactured by the process in accordance with claim 1 .

20. The film as claimed in claim 19 , wherein the film has a permeability coefficient of not more than 0.16 cc-mm/m 2 -day-mmHg.

21. The film as claimed in claim 19 , wherein the alloy has a G′ at 1% strain and 100° C. as determined according to ASTM D7605 of about 4,500 to about 7,500 kPa.

Assignees

• Exxonmobil Chemical Patents Inc

Inventors

• Nadella Hari P
• Ellul Maria D
• Deyoung Ronald

Classifications

• B29K2105/0044

  Stabilisers, e.g. against oxydation, light or heat · CPC title

• C08J2321/00

  Characterised by the use of unspecified rubbers · CPC title

• C08J2347/00

  Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds; Derivatives of such polymers (C08J2345/00 takes precedence; of conjugated diene rubbers C08J2309/00 - C08J2321/00) · CPC title

• C08J2377/02

  Polyamides derived from omega-amino carboxylic acids or from lactams thereof (C08J2377/10 takes precedence) · CPC title

• C08J3/005 Primary

  Processes for mixing polymers · CPC title