# US 2014/0155513 A1 · Methods of Forming Compositions and Articles

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- Number: US 2014/0155513 A1
- Document ID: US20140155513A1
- Status: Published application
- Kind: A1
- Application number: 13/691,252
- Filed: 2012-11-30
- Published: 2014-06-05
- Earliest claimed: 2012-11-30
- Assignees: ExxonMobil Chemical Patents Inc.
- Inventors: Sunny Jacob; Michael J. Goncy; Peter D. Hartwell; Bruce R. Lundmark
- Web page: https://patentgrep.com/patent/US20140155513A1

## CPC

- C08L 23/16: Ethylene-propylene or ethylene-propylene-diene copolymers
- C08F 255/02: on to polymers of olefins having two or three carbon atoms
- C08F 255/06: on to ethylene-propylene-diene terpolymers {(C08F255/023 takes precedence)}
- C08L 23/12: Polypropene
- C08K 5/0025: {Crosslinking or vulcanising agents; including accelerators}
- C08K 5/103: with polyalcohols
- C08K 5/34924: {containing cyanurate groups; Tautomers thereof}
- C08K 5/526: with hydroxyaryl compounds
- C08L: COMPOSITIONS OF MACROMOLECULAR COMPOUNDS (compositions based on polymerisable monomers C08F, C08G; artificial filaments or fibres D01F; textile treating compositions D06)
- C08F: MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08K: Use of inorganic or non-macromolecular organic substances as compounding ingredients (paints, inks, varnishes, dyes, polishes, adhesives C09)

## Abstract

A method for forming a composition comprising a propylene-based polymer and a co-agent is provided. The method comprises introducing a propylene-based polymer to an extruder and introducing the co-agent to the extruder at a position within the extruder where the temperature is from 23° C. to 125° C.

## Claims

### Claim 1

A method of forming a composition, comprising:
introducing to an extruder a propylene-based polymer containing from 5 wt % to 40 wt % of ethylene and/or C4-C20 α-olefins derived units and having a heat of fusion, as determined by DSC, of from 0.5 J/g to 80 J/g;
introducing to the extruder a co-agent selected from multifunctional acrylates, multifunctional methacrylates, functionalized polybutadiene resins, functionalized cyanurate, allyl isocyanurate, and combinations thereof, wherein the co-agent is introduced at a position within the extruder where the temperature is from 23° C. to 125° C.; and
forming the composition.

### Claim 2 (depends on 1)

The method of claim 1, wherein the co-agent is introduced at a position within the extruder where the temperature is from 50° C. to 100° C.

### Claim 3 (depends on 1)

The method of claim 1, wherein the co-agent is introduced to the extruder using a pump selected from a progressive cavity pump, a diaphragm pump, and a peristaltic pump.

### Claim 4 (depends on 3)

The method of claim 3, wherein the pump is operated at shear rate of less than 100 sec−1.

### Claim 5 (depends on 1)

The method of claim 1, wherein the co-agent is introduced to the extruder downstream of where the propylene-based polymer is introduced to the extruder.

### Claim 6 (depends on 1)

The method of claim 1, wherein the co-agent is introduced at a distance within 0.30 L from the feed throat of the extruder where the propylene-based polymer is introduced to the extruder, wherein L is the distance from said feed throat to the end of the extruder.

### Claim 7 (depends on 1)

The method of claim 1, wherein the co-agent is introduced is introduced at a distance within 0.15 L from the feed throat of the extruder where the propylene-based polymer is introduced to the extruder, wherein L is the distance from said feed throat to the end of the extruder.

### Claim 8 (depends on 1)

The method of claim 1, wherein the extruder is a single screw extruder or a twin screw extruder.

### Claim 9 (depends on 1)

The method of claim 1, wherein the propylene-based polymer has a melting point of 100° C. or less.

### Claim 10 (depends on 1)

The method of claim 1, wherein the propylene-based polymer has a triad tacticity, as determined by 13C NMR, of from 75% to 99%.

### Claim 11 (depends on 1)

The method of claim 1, wherein the propylene-based polymer comprises units derived from at least one of ethylene, butene, hexene, and octene.

### Claim 12 (depends on 1)

The method of claim 1, wherein the propylene-based polymer comprises from 0.2 wt % to 24 wt % of one or more diene derived units based on the weight of the propylene-based polymer.

### Claim 13 (depends on 1)

The method of claim 1, wherein the propylene-based polymer comprises from 0.5 wt % to 10 wt % of 5-ethylidene-2-norbornene based on the weight of the propylene-based polymer.

### Claim 14 (depends on 1)

The method of claim 1, wherein the composition comprises from 0.1 wt % to 15 wt % of the co-agent based on the weight of the composition.

### Claim 15 (depends on 1)

The method of claim 1, wherein the co-agent is a multifunctional methacrylate.

### Claim 16 (depends on 1)

The method of claim 1 further comprising introducing to the extruder an antioxidant selected from the group consisting of hindered phenols, phosphites, hindered amines, and combinations thereof.

### Claim 17 (depends on 16)

The method of claim 16, wherein the antioxidant is introduced to the extruder upstream of where the co-agent is introduced.

### Claim 18 (depends on 16)

The method of claim 16, wherein the composition comprises from 0.1 wt % to 5 wt % of the antioxidant based on the weight of the composition.

### Claim 19 (depends on 1)

The method of claim 1 further comprising introducing to the extruder at least one of a secondary elastomeric component or a polyolefinic thermoplastic resin.

### Claim 20 (depends on 1)

The method of claim 1 further comprising crosslinking the composition using electron beam radiation having an e-beam dosage of about 200 kGy or less.

### Claim 21 (depends on 1)

A composition made by the method of claim 1.

### Claim 22

A method of forming a film, a nonwoven, or a molded article, the method comprising:
(a) introducing to an extruder (i) a propylene-based polymer containing from 5 wt % to 40 wt % of ethylene and/or C4-C20 α-olefins derived units and having a heat of fusion, as determined by DSC, of from 0.5 J/g to 80 J/g; and (ii) an antioxidant selected from hindered phenols, phosphites, hindered amines, and combinations thereof; and (iii) a co-agent selected from multifunctional acrylates, multifunctional methacrylates, functionalized polybutadiene resins, functionalized cyanurate, allyl isocyanurate, and combinations thereof; where the co-agent is introduced at a position within the extruder where the temperature is from 23° C. to 125° C.;
(b) forming and extruding a composition comprising the propylene-based polymer, the antioxidant, and the co-agent; and
(c) forming the film, nonwoven, or molded article comprising the composition.

### Claim 23 (depends on 22)

The method of claim 22, wherein the co-agent is introduced at a position within the extruder where the temperature is from 50° C. to 100° C.

### Claim 24 (depends on 22)

The method of claim 22, wherein the co-agent is introduced using a pump selected from a progressive cavity pump, a diaphragm pump, and a peristaltic pump.

### Claim 25 (depends on 22)

The method of claim 22, wherein the composition is not pelletized before being introduced to an apparatus for forming the film, nonwoven, or molded article.
