Cross-linked melt-flowable thermoplastic elastomer blend comprising EPR or EPDM, polyethylene and polypropylene

Claim 2

A cross-linked melt-flowable thermoplastic elastomer blend, comprising: a blend of a monoolefin polymer elastomer of ethylene and propylene, with or without a copolymerizable polyene, and a cross-linkable low density polyethylene, having a density of no more than about 0.929 g/cc, essentially fully cured in the presence of a polypropylene to produce a non-melt-flowable discontinuous elastomer phase of substantially completely cross-linked monoolefin polymer elastomer and polyethylene intimately dispersed in a meltflowable continuous phase of polypropylene, the weight ratio of the discontinuous elastomer phase to melt-flowable continuous phase being at least 1:1, the polymer components being respectfully present in amounts of about 20 to about 50% monoolefin polymer elastomer, about 15 to about 50% low density polyethylene and about 25 to about 50% polypropylene, based upon the total weight of the polymer compound.

Claim 3

The blend of claim 1, wherein the monoolefin polymer elastomer and cross-linkable low density polyethylene are cured with an organic peroxide curing agent, the organic peroxide curing agent being present in an amount sufficient to substantially completely cross-link all the monoolefin polymer resin and cross-linkable polyethylene in the presence of the polypropylene.

Claim 4

The blend of claim 3, wherein monoolefin polymer elastomer and cross-linkable low density polyethylene are further cross-linked in the presence of from about 0.1 to about 0.5 wt.% triallylcyanurate, based upon the total weight of the cross-linkable components.

Claim 5

The blend of claim 1, including about 0.25 to about 1.0 wt.%, based upon the weight of polypropylene, of a compound capable of preventing degradation of polypropylene with the monoolefin polymer elastomer and cross-linkable low density polyethylene being fully cured in the presence thereof, said compound being selected from the group consisting of sulfur, triallylcyanurate, triallylphosphate, and tris (2,3-dibromopropyl) phosphate, and mixtures thereof.

Claim 6

The blend of claim 1, wherein the monoolefin polymer elastomer has a Mooney viscosity of from about 20 to about 120, ML 1+8' at 212° F., and contains from about 40 to about 90% by weight ethylene, said elastomer being selected from the group consisting of a saturated ethylene-propylene copolymer elastomer, an ethylene-propylene-unconjugated diene terpolymer elastomer, having an unconjugated diene content of from about 2.5 to about 10% by weight, and mixtures thereof.

Claim 7

The blend of claim 1, wherein the cross-linkable low density polyethylene has a density of from about 0.915 to about 0.929 g/cc and a melt index of from about 2 to about 30.

Claim 8

The blend of claim 1, wherein the polypropylene is an isotactic polypropylene of greater than 90% hot heptane insolubles having a melt flow rate of from about 0.5 to about 30.

Claim 9

The blend of claim 1, wherein the polymer components are respectively present in amounts of about 40 to about 45% monoolefin polymer elastomer, about 15 to about 20% low density polyethylene and about 30 to about 35% polypropylene, based upon the total weight of the polymer components.

Claim 10

A method for preparing the cross-linked melt-flowable thermoplastic elastomer blend of claim 1, comprising: mixing a monoolefin polymer elastomer of ethylene and propylene, with or without a copolymerizable polyene, a cross-linkable low density polyethylene, having a density of no more than about 0.929 g/cc, and a curing agent therefor with a polypropylene resin and heating the resulting mixture to an elevated temperature for a sufficient period of time to fully cure the monoolefin polymer elastomer and polyethylene components to produce a non-melt-flowable discontinuous elastomer phase of substantially fully cross-linked monoolefin polymer elastomer and low density polyethylene intimately dispersed within a melt-flowable continuous phase of polypropylene, the elastomer, low density polyethylene and polypropylene polymeric components being present in amounts sufficient to provide a weight ratio of discontinuous elastomer phase to melt-flowable continuous phase of at least 1:1.

Claim 11

The method of claim 10, wherein the respective polymer components are mixed in amounts within the range of about 20 to about 50% monoolefin polymer elastomer, about 15 to about 40% cross-linkable low density polyethylene and about 20 to about 50% polypropylene, based upon the total weight of said polymer components.

Claim 12

The method of claim 10, wherein the curing agent is an organic peroxide, said curing agent being employed in an amount sufficient to provide substantially complete cross-linking of all the monoolefin polymer elastomer and cross-linkable low density polyethylene components in the presence of the polypropylene.

Claim 13

The method of claim 12, wherein about 0.1 to about 0.5 wt.% triallylcyanurate, based upon the weight of the monoolefin polymer elastomer and low density polyethylene present, is added to the mixture prior to subjecting the mixture to the elevated curing temperature.

Claim 14

The method of claim 13, wherein the monoolefin polymer elastomer, low density polyethylene, curing agent and triallylcyanurate are intimately mixed at an elevated temperature insufficient to cause curing of the polymer component prior to mixing with the polypropylene.

Claim 15

The method of claim 10, wherein a compound capable of preventing degradation of the polypropylene during curing of the cross-linkable polymer components is added to the mixture prior to subjecting the mixture to the elevated curing temperature, the compound being added in an amount of from about 0.1 to about 1.0 wt.%, based upon the weight of polypropylene, and being selected from the group consisting of sulfur, triallylcyanurate, triallylphosphate, tris (2,3-dibromopropyl) phosphate and mixtures thereof.

Claim 16

The method of claim 15, wherein the compound capable of preventing degradation of polypropylene is intimately mixed with the polypropylene at an elevated temperature prior to mixing the polypropylene with the monoolefin polymer elastomer and low density polyethylene.

Claim 17

The method of claim 10, wherein the monoolefin polymer elastomer has a Mooney viscosity of from about 20 to about 120, ML 1+8' at 212° F., and contains from about 40 to about 80% by weight ethylene, said elastomer being selected from the group consisting of a saturated ethylenepropylene copolymer elastomer, an ethylene-propylene-unconjugated diene terpolymer elastomer, having an unconjugated diene content of from about 2.5 to about 10% by weight, and mixtures thereof.

Claim 18

The method of claim 10, wherein the cross-linkable low density polyethylene has a density of from about 0.915 to about 0.929 g/cc and a melt index of from about 2 to about 30.

Claim 19

The method of claim 10, wherein the polypropylene is an isotactic polypropylene of greater than 99% hot heptane insolubles having a melt flow rate of from about 0.5 to about 30.

Claim 20

The method of claim 10, wherein the polymer components of the blend are present in respective amounts within the range of from about 40 to about 45% monoolefin polymer elastomer, about 15 to about 20% cross-linkable polyethylene and from about 30 to about 35% polypropylene, based upon the total weight of polymer components of the mixture.

Claim 21

The method of claim 20, wherein the monoolefin polymer elastomer and low density polyethylene are initially intimately mixed with an organic peroxide curing agent present in an amount sufficient to provide substantially complete cross-linking thereof and from about 0.1 to about 0.5 wt.% triallylcyanurate, based upon the weight of the polymer components, at an elevated temperature insufficient to cause cross-linking of said polymer components.

Claim 22

The method of claim 21, wherein a compound capable of preventing degradation of the polypropylene during curing of the elastomer and polyethylene polymer components is intimately mixed with the polypropylene prior to mixing the polypropylene with the elastomer, low density polyethylene, curing agent and triallylcyanurate mixture at an elevated temperature, said compound being added to the polypropylene in an amount of from about 0.25 to about 1.0% by weight of the polypropylene and being selected from the group consisting of sulfur, triallylcyanurate, triallylphosphate, tris (2,3-dibromopropyl) phosphate and mixtures thereof.