Method of polymerizing vinyl halide with olefin polymers and copolymers and compositions thereof

Claim 2

In the process for the preparation of a vinyl chloride polymer comprising polymerizing in bulk in liquid phase vinyl chloride alone or in combination with up to 50% by weight based on the total weight of monomer of another ethylenically unsaturated monomer copolymerizable therewith, in the presence of a trunk polymer and a free radical initiator compound for said polymerization, wherein the trunk polymer is present during the polymerization only during the period which commences at 0% to about 20% conversion of the monomer or monomers to polymer and concludes with the end of the polymerization, the improvement which comprises employing as the trunk polymer about 0.05% to about 20% by weight, based upon said vinyl chloride monomer, of a trunk polymer consisting essentially of an olefin trunk polymer which is selected from the group consisting of: (A) a homopolymer of an aliphatic hydrocarbon olefin monomer of 2 to 8 carbon atoms, (B) a copolymer of two or more of said olefin monomers, and (C) a polymer of at least one of said olefin monomers and no more than 15% by weight, based on the weight of the polymer, of a non-conjugated aliphatic hydrocarbon polyene of 4 to 18 carbon atoms wherein all of the carbon-to-carbon double bonds do not form a conjugated system, said olefin polymer being soluble, partially soluble or dispersible in said monomer or monomers of the polymerization reaction, and said olefin polymer having a weight average molecular weight of about 50,000 to about 1,000,000.

Claim 3

The process of claim 1 wherein the olefin polymer is present in the polymerization after about 1% of the monomer or monomers have been converted to polymer.

Claim 4

The process of claim 2 wherein the olefin polymer is present in the polymerization after about 3% to about 15% by weight of the monomers have been converted to polymer.

Claim 5

The process of claim 3 wherein said olefin polymer containing said polyene is an olefin terpolymer.

Claim 6

The process of claim 4 wherein said olefin terpolymer contains an aliphatic hydrocarbon diene as a monomer unit.

Claim 7

The process of claim 5 wherein said diene is present in said terpolymer in the proportion of up to about 6% by weight of said terpolymer.

Claim 8

The process of claim 3 wherein said olefin polymer is selected from the group consisting of an ethylene-propylene copolymer, an ethylene-propylene diene-modified terpolymer, a propylene homopolymer, and a butene-1 ethylene copolymer.

Claim 9

The process of claim 3 wherein said olefin polymer is an ethylene-propylene copolymer.

Claim 10

The process of claim 5 wherein said olefin polymer is ethylene-propylene ethylidene norbornene terpolymer.

Claim 11

The process of claim 5 wherein said olefin polymer is ethylene-propylene 1,4-hexadiene terpolymer.

Claim 12

The process of claim 1 comprising carrying out the polymerization in a first stage wherein the reaction mixture is subjected to high speed agitation until about 3% to about 20% by weight of said monomer or monomers have been converted to polymer and further polymerizing the resultant reaction mixture together with additional monomer or monomers in a second stage during which the reaction mixture is subjected to low speed agitation until the polymerization has been completed, wherein the olefin polymer is added at the beginning of the second reaction stage.

Claim 13

The process of claim 11 wherein a portion, amounting to at least about 60% by weight, of the monomer or monomers charged to the polymerization reaction are added in the first stage, the balance of the monomer or the monomers being added at about the beginning of the second stage.

Claim 14

The process of claim 12 wherein there is added in the first stage about 60% to about 70% by weight of the monomer or monomers charged to the polymerization reaction.

Claim 15

The process of claim 13 wherein about 3% to about 15% by weight of the monomer or monomers is converted to polymer in the first reaction stage.

Claim 16

The process of claim 14 wherein about 7% to about 15% of monomer or monomers is converted to polymer in the first reaction stage.

Claim 17

The process of claim 1 wherein the olefin polymer is introduced to the polymerization reaction in admixture with a portion of the monomer or monomers used in the polymerization reaction.

Claim 18

The process of claim 16 wherein said olefin polymer has a weight average molecular weight of about 50,000 to 300,000.

Claim 19

The process of claim 16 wherein said olefin polymer is selected from the group consisting of an ethylene-propylene copolymer, and ethylene-propylene diene-modified terpolymer, a propylene homopolymer, and a butene-1 ethylene copolymer.

Claim 20

The process of claim 16 comprising carrying out the polymerization in a first stage wherein the reaction mixture is subjected to high speed agitation until about 3% to about 15% by weight of said monomer or monomers have been converted to polymer and further polymerizing the resultant reaction mixture together with additional monomer or monomers in the second stage during which the reaction mixture is subjected to low speed agitation until the polymerization has been completed wherein said mixture of olefin polymer and monomer or monomers is introduced to the polymerization reaction at the beginning of the second reaction stage.

Claim 21

The process of claim 19 wherein about 60% to about 70% of the monomer or monomers charged to the polymerization are added in the first stage with the balance being added at about the beginning of the second stage.

Claim 22

The process of claim 1 wherein the olefin polymer is an ethylene-propylene copolymer.

Claim 23

The process of claim 1 wherein the olefin polymer is polyethylene.

Claim 24

The process of claim 1 wherein the olefin polymer is polypropylene.

Claim 25

The process of claim 1 wherein the olefin polymer is an ethylene-propylene diene modified terpolymer.

Claim 26

The process of claim 1 wherein the weight average molecular weight of said olefin polymer is about 50,000 to 300,000.

Claim 27

The process of claim 24 wherein the weight average molecular weight of said olefin polymer is about 50,000 to 300,000.

Claim 28

The product of the process of claim 1.

Claim 29

The product of the process of claim 4.

Claim 30

The product of the process of claim 11.

Claim 31

The product of the process of claim 20.

Claim 32

The product of the process of claim 21.

Claim 33

The product of the process of claim 22.

Claim 34

The product of the process of claim 23.

Claim 35

The product of the process of claim 24.

Claim 36

The product of claim 29 wherein the proportion of olefin polymer in the product is about 0.1% to about 10% by weight based on the vinyl chloride monomer units thereof.

Claim 37

The product of the process of claim 14 wherein the olefin polymer in said product is present as a rubber and graft polymer disperse phase having a particle diameter of about 0.1 to about 0.5 microns, the proportion of olefin polymer in said product being about 1% to about 20% by weight based on vinyl chloride monomer units thereof to impart high impact strength to said product.

Claim 38

The product of claim 36 wherein the proportion of olefin polymer is about 1% to about 10% by weight.

Claim 39

The product of claim 36 wherein the monomer reactant of the polymerization consists of vinyl chloride.

Claim 40

The product of claim 38 wherein said olefin polymer is ethylene-propylene rubber.

Claim 41

The product of claim 38 wherein said olefin polymer is polypropylene.

Claim 42

The product of claim 38 wherein the olefin polymer is an ethylene-propylene diene modified rubber.

Claim 43

The product of claim 38 wherein said olefin polymer is polyethylene.

Claim 44

The product of claim 38 wherein the weight average molecular weight of the olefin polymer is about 50,000 to 300,000.

Claim 45

In the process for the preparation of a vinyl chloride polymer comprising polymerizing in bulk in liquid phase vinyl chloride monomer alone or in combination with up to about 50% by weight based on the total weight of monomer of another ethylenically unsaturated monomer copolymerizable therewith, in the presence of a trunk polymer and a free radical initiator for the polymerization, wherein the trunk polymer is present during the polymerization only during the period which commences at 0% to about 20% conversion of the monomer or monomers to polymer and concludes with the end of the polymerization, said polymerization being carried out in a first stage wherein the reaction mixture is subjected to high speed agitation until about 3% to about 20% by weight of said monomer or monomers have been converted to polymer, and further polymerizing the resultant reaction mixture together with additional monomer or monomers in a second stage during which the reaction mixture is subjected to low speed agitation until the polymerization has been completed, the improvement which comprises employing as the trunk polymer about 0.05% to about 20% by weight, based upon said vinyl chloride monomer, of a trunk polymer consisting essentially of an olefin trunk polymer which is selected from the group consisting of: (A) a homopolymer of an aliphatic hydrocarbon olefin monomer of 2 to 8 carbon atoms, (B) a copolymer of two or more of said olefin monomers, and (C) a polymer of at least one of said olefin monomers and no more than 15% by weight, based on the weight of the polymer, of a non-conjugated aliphatic hydrocarbon polyene of 4 to 18 carbon atoms wherein all of the carbon-to-carbon double bonds do not form a conjugated system, said olefin polymer being soluble, partially soluble or dispersible in said monomer or monomers of the polymerization reaction, and said olefin polymer having a weight average molecular weight of about 50,000 to about 1,000,000.

Claim 46

In the process for the preparation of a vinyl chloride polymer comprising polymerizing in bulk in liquid phase vinyl chloride monomer alone or in combination with up to about 50% by weight based on the total weight of monomer of another ethylenically unsaturated monomer copolymerizable therewith, in the presence of a trunk polymer and a free radical initiator for the polymerization, wherein the trunk polymer is present during the polymerization only during the period which commences at 0% to about 20% conversion of the monomer or monomers to polymer and concludes with the end of the polymerization, said polymerization being carried out in a first stage wherein the reaction mixture is subjected to high speed agitation until about 3% to about 20% by weight of said monomer or monomers have been converted to polymer, and further polymerizing the resultant reaction mixture together with additional monomer or monomers in a second stage during which the reaction mixture is subjected to low speed agitation until the polymerization has been completed, the improvement which comprises employing as the trunk polymer about 0.05% to about 20% by weight, based upon said vinyl chloride monomer, of a trunk polymer consisting essentially of an olefin trunk polymer which is selected from the group consisting of: (A) a homopolymer of an aliphatic hydrocarbon olefin monomer of 2 to 8 carbon atoms, (B) a copolymer of two or more of said olefin monomers, and (C) a polymer of at least one of said olefin monomers and no more than 15% by weight, based on the weight of the polymer, of a non-conjugated aliphatic hydrocarbon polyene of 4 to 18 carbon atoms wherein all of the carbon-to-carbon double bonds do not form a conjugated system, said olefin polymer being soluble, partially soluble or dispersible in said monomer or monomers of the polymerization reaction, and said olefin polymer having a weight average molecular weight of about 50,000 to about 1,000,000.