IP Library Granted Patent US 10,279,527
Granted Patent B2
US 10,279,527 · App. 15/099,916 · Granted May 7, 2019

Thermoplastic vulcanizates comprising propylene-based elastomers and methods for making the same

Inventors: Randal H. Kerstetter, III (Wadsworth, OH); Porter C. Shannon (Seabrook, TX); Joseph M. Tomei (Akron, OH); Eugene R. Uhl (Massillon, OH)
Assignee: ExxonMobil Chemical Patents Inc.
B29C47/0004B29C35/02C08J3/24C08L23/0815C08L23/16B29K2021/003B29K2023/16B29L2031/00C08J2323/16C08J2423/12C08J2423/16
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Quick Facts
Patent No.
US 10,279,527
App. No.
15/099,916
Granted
May 7, 2019
Kind
B2
Abstract

Described herein are thermoplastic vulcanizates comprising propylene-based elastomers and methods for producing the same. The thermoplastic vulcanizates comprise rubber, at least 10 wt % of thermoplastic resin, from 1 to 9 wt % of propylene-based elastomer, oil, and at least 5 wt % of one or more fillers. The thermoplastic vulcanizates are made by a method where the propylene-based elastomer is introduced to the extrusion reactor before the curative is introduced to the extrusion reactor.

Claims (14)

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

a. introducing rubber to an extrusion reactor;

b. introducing at least 10 wt % of thermoplastic resin, based on a total weight of the thermoplastic vulcanizate, to the extrusion reactor;

c. introducing from 1 wt % to 9 wt % of propylene-based elastomer, based on the total weight of the thermoplastic vulcanizate, to the extrusion reactor;

d. introducing at least 5 wt % of one or more fillers, based on the total weight of the thermoplastic vulcanizate, to the extrusion reactor;

e. introducing a first amount of process oil to the extrusion reactor at a first oil injection location;

f. introducing curative to the extrusion reactor at a location that is downstream of the first oil injection location and that is downstream of the location at which the propylene-based elastomer is introduced to the extrusion reactor;

g. introducing a second amount of process oil to the extrusion reactor at a second oil injection location, where the second oil injection location is downstream of the location where the curative is introduced to the extrusion reactor; and

h. dynamically vulcanizing the rubber with the curative in the presence of the thermoplastic resin and the propylene-based elastomer to form the thermoplastic vulcanizate;

wherein the thermoplastic vulcanizate comprises a rubber phase that is dispersed and at least partially cross-linked within a continuous thermoplastic component that comprises the thermoplastic resin and the propylene-based elastomer.

2. The method of claim 1 , wherein the extrusion reactor is a multi-screw extruder.

3. The method of claim 2 , wherein the extrusion reactor operates at an extrusion rate greater than about 90 kg/hr.

4. The method of claim 1 , wherein 55 to 70 wt % of the total amount of oil in the thermoplastic vulcanizate is introduced at the first oil injection location.

5. The method of claim 1 , wherein 25 to 40 wt % of the total amount of oil in the thermoplastic vulcanizate is introduced at the second oil injection location.

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 Jun 21, 2016
From: KERSTETTER, RANDAL H., III; SHANNON, PORTER C.; TOMEI, JOSEPH M.; UHL, EUGENE R.
To: EXXONMOBIL CHEMICAL PATENTS INC.
Reel/Frame 038966/0733 →
Continuity (2)
Provisional Application 62165386 · May 22, 2015
Related Publication 20160340480A1 · Nov 24, 2016
Cited By (1)
US 12,545,777