Homogeneous blends of a trans-isomer of polyisoprene

Claim 2

A composition comprising an apparently homogeneous blend of from 10% to 90% by weight of trans-isomer of poly(1,4-isoprene) substantially free of depolymerized polymer, in combination with from 90% to 10% by weight of an ionomer that contains at least one mol percent of an ethylenically unsaturated carboxylic acid having one or two carboxylic acid groups, wherein at least about 10% of the carboxyl groups are neutralized by a metal having an ionic valence of from one to three, inclusive, and up to about 15% by weight of a cis-isomer of natural rubber or synthetic rubber.

Claim 3

The composition of claim 1 comprising from about 10% to about 50% by weight of the trans-isomer of poly(1,4-isoprene).

Claim 4

The composition of claim 1 wherein the ionomer is a copolymer of ethylene and methacrylic acid, wherein at least about 10% of the carboxyl groups have been neutralized by a metal ion selected from the group consisting of zinc and sodium.

Claim 5

The composition of claim 3 wherein the ionomer is formed from about 3 to about 15 mol percent methacrylic acid.

Claim 6

A process for forming a homogeneous, apparently stable blend of an ionomer that contains at least one mol percent of an ethylenically unsaturated carboxylic acid group, wherein at least about 10% of the carboxyl groups are neutralized by a metal having an ionic valence of from one to three, inclusive, and a trans-isomer and ionomer, in proportions of from 10% to 90% by weight trans-isomer and from 90% to 10% by weight ionomer, under conditions of pressure sufficiently greater than ambient to permit forming a uniform blend and at a temperature of at least about 180° F., but below the depolymerization temperature of the trans-isomer, until a uniform blend is obtained, which is substantially free from depolymerization of the trans-isomer.

Claim 7

A process for forming a homogeneous, apparently stable blend of an ionomer that contains at least one mol percent of an ethylenically unsaturated carboxylic acid group, wherein at least about 10% of the carboxyl groups are neutralized by a metal having an ionic valence of from one to three, inclusive, and a trans-isomer and ionomer, in proportions of from 10% to 90% by weight trans-isomer and from 90% to 10% by weight ionomer, under conditions of pressure sufficiently greater than ambient to permit forming a uniform blend and at a temperature of at least about 180° F., but below the depolymerization temperature of the trans-isomer, until a uniform blend is obtained, which is substantially free from depolymerization of the trans-isomer.

Claim 8

The process of claim 5 wherein the trans-isomer and ionomer are mixed in a fully-enclosed masticator and at a temperature in the range of from about 190° to about 250° F.

Claim 9

The process of claim 6 wherein the internal surfaces of the masticator in contact with the mixture are subject to cooling by heat exchange.

Claim 10

The process of claim 7 wherein the internal surfaces of the masticator are pre-heated, prior to addition of the trans-isomer and ionomer, to a temperature of at least 150° F.

Claim 11

The process of claim 6 wherein the mixing is carried out at a temperature in the range of from about 200° to about 250° F. in the masticator.

Claim 12

The process of claim 7 wherein the mixing is by internal shear at a rate sufficient to at least maintain a temperature within the mixing batch of at least about 200° F.

Claim 13

The process of claim 5 wherein the internal pressure on the trans-isomer and ionomer during mixing is at least about 25 psig.

Claim 14

The process of claim 11 wherein the internal pressure is in the range of at least about 30 psig.

Claim 15

The composition of claim 1 wherein the ionomer is present in an amount of from about 50% to about 90% by weight.

Claim 16

The process of claim 5 wherein the ionomer is mixed in an amount from about 50% to about 90% by weight of the blend.