IP Library Granted Patent US 8,865,838
Granted Patent B2
US 8,865,838 · App. 12/953,552 · Granted Oct 21, 2014

Process for forming thermoplastic vulcanizates

Inventors: Stephen F. Roche (Cwmbran, GB); Randal H. Kerstetter (Wadsworth, OH)
Assignee: ExxonMobil Chemical Patents Inc.
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 8,865,838
App. No.
12/953,552
Granted
Oct 21, 2014
Kind
B2
Abstract

Provided are methods for producing a thermoplastic vulcanizate. One method includes charging vulcanizable rubber to a reactor; charging a masterbatch of thermoplastic resin and a catalyst for a phenolic resin curative to the reactor; charging a phenolic resin curative to the reactor; and dynamically vulcanizing the rubber with the phenolic resin curative in the presence of the catalyst. Also provided are thermoplastic vulcanizates made by the methods of the invention.

Claims (24)

1. A method for making a thermoplastic vulcanizate, the method comprising the steps of:

charging vulcanizable rubber and a first thermoplastic resin to a reactor to form a molten mass, wherein the first thermoplastic resin is substantially devoid of a catalyst for the phenolic resin;

charging a masterbatch consisting essentially of a second thermoplastic resin and a catalyst for a phenolic resin curative to the molten mass in the reactor, wherein the masterbatch contains ≧10 wt% and ≦90 wt% of the catalyst based on the total weight of the masterbatch and wherein the masterbatch contains less than 1 wt% of material other than the catalyst or the second thermoplastic resin based on the weight of the masterbatch;

charging a phenolic resin curative to the molten mass reactor; and

dynamically vulcanizing the rubber with the phenolic resin curative in the presence of the catalyst.

2. The method of claim 1 , further comprising the step of mixing the vulcanizable rubber and the masterbatch above the melt temperature of the first thermoplastic resin.

3. The method of claim 1 , where the catalyst is stannous chloride.

4. The method of claim 1 , where the catalyst is anhydrous stannous chloride.

5. The method of claim 1 , where the masterbatch includes ≧ 20 wt% and 70 wt% stannous chloride based on the total weight of the masterbatch.

6. The method of claim 1 , where the masterbatch is charged to the reactor in the form of pellets.

7. The method of claim 1 , where the first thermoplastic resin includes polypropylene.

8. A method for making a thermoplastic vulcanizate, the method comprising the steps of:

a. mixing a vulcanizable rubber and a first thermoplastic resin above the melt temperature of the thermoplastic resin to form a molten mass;

b. adding a masterbatch consisting of a second thermoplastic resin and catalyst to the molten mass;

c. melting the second thermoplastic resin of the masterbatch to thereby disperse the catalyst within the molten mass;

d. adding a phenolic curative to the molten mass; and

e. dynamically vulcanizing the rubber with the phenolic resin in the presence of the catalyst.

9. The method of claim 8 , where the vulcanizable rubber is a poly(ethylene-propylene-diene)copolymer, the first thermoplastic resin is polypropylene, and the second thermoplastic resin is polypropylene.

10. The method of claim 8 , where the catalyst is anhydrous stannous chloride.

11. The method of claim 8 , where said dynamic vulcanization is effected in the presence of ≧10 wt% and ≦70 wt% stannous chloride based on the total weight of the masterbatch.

12. A method for making a thermoplastic vulcanizate, the method comprising the steps of: charging a poly(ethylene-propylene-diene)copolymer to a twin-screw extruder through the feed throat of the extruder; charging polypropylene to the twin-screw extruder through the feed throat of the extruder; mixing, within an initial mix zone, the poly(ethylene-propylene-diene)copolymer and the polypropylene at a temperature above the melt temperature of the polypropylene to form a molten mass; charging pellets that include a blend of polypropylene and anhydrous stannous chloride to the twin-screw extruder through an inlet in a barrel downstream of the initial mix zone, wherein the pellets include less than 1% of material other than the stannous chloride or the polypropylene based on the weight of the pellet; heating the pellets above the melt temperature of the polypropylene and mixing the molten polypropylene with the molten mass; charging a phenolic resin curative to the twin-extruder through an inlet in a barrel downstream of the barrel where the pellets are charged; mixing the phenolic resin with the molten mass while transferring the molten mass through a cure zone where dynamic vulcanization of the rubber takes place to thereby form a thermoplastic vulcanizate; removing the thermoplastic vulcanizate from the twin-screw extruder; cooling the thermoplastic vulcanizate; and pelletizing the thermoplastic vulcanizate.

13. A thermoplastic vulcanizate made by the method of claim 1 .

14. A thermoplastic vulcanizate made by the method of claim 8 .

15. A thermoplastic vulcanizate made by the method of claim 13 .

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 25, 2022
From: EXXONMOBIL CHEMICAL PATENTS INC.
To: SANTOPRENE PRODUCTION PENSACOLA LLC
Reel/Frame 059248/0456 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 25, 2022
From: SANTOPRENE PRODUCTION PENSACOLA LLC
To: CELANESE INTERNATIONAL CORPORATION
Reel/Frame 059248/0673 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 25, 2011
From: ROCHE, STEPHEN F.; KERSTETTER, RANDAL H., III
To: EXXONMOBIL CHEMICAL PATENTS INC.
Reel/Frame 025690/0018 →
Continuity (2)
Provisional Application 61291244 · Dec 30, 2009
Related Publication 20110160402A1 · Jun 30, 2011