Method of preparing vinyl halide polymers and copolymers with polyolefins

Claim 2

In the process for the preparation of a vinyl halide polymer which comprises polymerizing in bulk a vinyl halide monomer, in the liquid phase, either alone or in combination with up to about 50% by weight of another ethylenically unsaturated monomer copolymerizable therewith, in the initial presence of more than about 1.8% by weight based on said vinyl halide monomer of a polyolefin or mixture of polyolefins having a weight average molecular weight of at least about 50,000, the improvement which comprises removing from the polymerization mass during the thick paste state thereof from about 2% to less than about 50% by weight of the vinyl halide charged to the polymerization mass, the effective concentration of said polyolefin or mixture of polyolefins after said vinyl halide removal being above about 3.5 weight percent based on vinyl halide remaining in said polymerization mass after said removal of vinyl halide whereby a more finely divided particulate product of high impact strength is obtained.

Claim 3

The process of claim 1 wherein the polymer prepared is a vinyl halide homopolymer, the polymerization is carried out in a single stage, and the polyolefin is selected from the group consisting of: 1. halogenated polyolefins; 2. olefin homopolymers; 3. olefin copolymers and terpolymers; said polymers having 2 to 8 carbon atoms in the monomeric units thereof and a weight average molecular weight of about 150,000 to 1,000,000 and the amount of vinyl halide monomer removed is about 5% to about 40% of the vinyl halide monomer charged to the polymerization.

Claim 4

The process of claim 2 wherein the initial concentration of polyolefin or mixture of polyolefins is at least about 3% by weight based on said vinyl halide monomer and the effective concentration of said polyolefin or mixture of polyolefins after said vinyl halide removal is above about 5.3 weight percent based on vinyl halide remaining in the polymerization mass after said removal of vinyl halide.

Claim 5

The process of claim 3 wherein said vinyl halide monomer is vinyl chloride, the polymerization is a single stage bulk polymerization carried out at a temperature of about 25° to about 90° centigrade under at least autogeneous superatmospheric pressure in the presence of an initiating amount of a free radical initiator for the reaction, the thick paste state of the polymerization mass corresponds to a conversion of vinyl chloride to polymer of about 30% to about 40% by weight, and about 8% to 35% by weight of the vinyl chloride is removed by venting from said pressurized polymerization mass and said polyolefin terpolymers contain a diene as a monomeric unit.

Claim 6

The process of claim 4 wherein the vinyl chloride is vented from the polymerization mass at a rate of about 0.1 to 1.5% by weight vinyl chloride per minute based on vinyl chloride charge to the polymerization, the polymerization temperature is from about 40° to about 80° centigrade at autogenous superatmospheric pressure, the diene of the polyolefin terpolymer is selected from the group consisting of dicyclopentadiene, 1,3-butadiene and non-conjugated dienes with linear or cyclic chains and is present in said terpolymer in a proportion up to about 15% by weight of said terpolymer and the effective concentration of polyolefin in the polymerization mass is about 5.5% to about 10% by weight.

Claim 7

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

Claim 8

The process of claim 6 wherein the polymerization temperature is from about 50° to about 75° centigrade, the initiator is an organic peroxy- or azo compound added to the polymerization mass in a concentration of about 0.01% to about 1.0% based on the weight of vinyl chloride the effective concentration of polyolefin is about 6% to about 9% by weight based on vinyl chloride and the vinyl chloride is vented from the polymerization mixture at a rate of about 0.15% to 1.2% per minute, said venting commencing about 5 to about 15 minutes after onset of the thick paste state in the polymerization mass.

Claim 9

The process of claim 7 wherein the average weight average molecular weight of the polyolefin is about 150,000 to about 400,000, the initiator is an organic peroxide, and the vinyl chloride is vented from the polymerization mixture at a rate of about 0.3% to about 1.2% per minute.

Claim 10

The process of claim 8 wherein the polyolefin reactant is an olefin copolymer or terpolymer.

Claim 11

The process of claim 9 wherein the polyolefin is ethylene-propylene ethylindene norbornene terpolymer.

Claim 12

The process of claim 9 wherein the polyolefin is an ethylene-propylene 1,4-hexadiene terpolymer.

Claim 13

The process of claim 9 wherein the polyolefin is an ethylene-propylene copolymer.

Claim 14

The process of claim 9 wherein the polyolefin is a butene-1-ethylene copolymer.

Claim 15

The process of claim 8 wherein the polyolefin is an olefin homopolymer.

Claim 16

The process of claim 14 wherein the olefin homopolymer is polyethylene.

Claim 17

The process of claim 14 wherein the olefin homopolmyer is polypropylene.

Claim 18

The process of claim 8 wherein the polyolefin is a halogenated polyolefin.

Claim 19

The process of claim 17 wherein the halogenated polyolefin is chlorinated polyethylene.

Claim 20

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 polymers 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 polymerization has been completed so that the thick paste state of the polymerization and the removal therein of vinyl halide takes place in said second reaction stage.

Claim 21

The process of claim 19 wherein a portion, amounting to at least about 50% 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 22

The process of claim 20 wherein there is added in the first stage about 50% to about 60% by weight of the monomer or monomers charged to the polymerization reaction.

Claim 23

The process of claim 21 wherein about 3% to about 15% by weight of the monomer or monomers is converted to polymer in the first reaction stage.

Claim 24

The process of claim 22 wherein about 7% to about 15% of monomer or monomers is converted to polymer in the first reaction stage.

Claim 25

The process of claim 23 wherein the monomer reactant is vinyl chloride.

Claim 26

In the process for the preparation of a vinyl halide polymer which comprises polymerizing in bulk a vinyl halide monomer, in the liquid phase, either alone or in combination with up to about 50% by weight of another ethylenically unsaturated monomer copolymerizable therewith, in the initial presence of more than about 1.8% by weight based on said vinyl halide monomer of a polyolefin or mixture of polyolefins having a weight average molecular weight of at least about 50,000, said polyolefin or mixture of polyolefins being 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 removing from the polymerization mass during the thick paste state thereof from about 2% to less than about 50% by weight of the vinyl halide changed to the polymerization mass, the effective concentration of said polyolefin or mixture of polyolefins after said vinyl halide removal being above about 3.5 weight percent based on vinyl halide remaining in said polymerization mass after said removal of vinyl halide whereby a more finely divided particulate product of high impact strength is obtained.

Claim 27

In the process for the preparation of a vinyl halide polymer which comprises polymerizing in bulk a vinyl halide monomer, in the liquid phase, either alone or in combination with up to about 50% by weight of another ethylenically unsaturated monomer copolymerizable therewith, in the initial presence of more than about 1.8% by weight based on said vinyl halide monomer of a polyolefin or mixture of polyolefins having a weight average molecular weight of at least about 50,000, said polyolefin or mixture of polyolefins being 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 removing from the polymerization mass during the thick paste state thereof from about 2% to less than about 50% by weight of the vinyl halide changed to the polymerization mass, the effective concentration of said polyolefin or mixture of polyolefins after said vinyl halide removal being above about 3.5 weight percent based on vinyl halide remaining in said polymerization mass after said removal of vinyl halide whereby a more finely divided particulate product of high impact strength is obtained.

Claim 28

The process of claim 25 wherein the polymer prepared is a vinyl halide homopolymer, the polymerization is carried out in a single stage, and the polyolefin is selected from the group consisting of: 1. halogenated polyolefins; 2. olefin homopolymers; 3. olefin copolymers and terpolymers; said polymers having 2 to 8 carbon atoms in the monomeric units thereof and a weight average molecular weight of about 50,000 to 1,000,000 and the amount of vinyl halide monomer removed is about 5% to about 40% of the vinyl halide monomer charged to the polymerization mass.

Claim 29

The process of claim 26 wherein the olefin polymer is present in the polymerization after about 1% of the monomer or monomers have been converted to polymer.

Claim 30

The process of claim 27 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 31

The process of claim 28 wherein the initial concentration of polyolefin or mixture of polyolefins is at least about 3% by weight based on said vinyl halide monomer and the effective concentration of said polyolefin or mixture of polyolefins after said vinyl halide removal is above about 5.3 weight percent based on vinyl halide remaining in the polymerization mass after said removal of vinyl halide.

Claim 32

The process of claim 29 wherein said vinyl halide monomer is vinyl chloride, the polymerization is a single stage bulk polymerization carried out at a temperature of about 25° to about 90° centigrade under at least autogeneous superatmospheric pressure in the presence of an initiating amount of a free radical initiator for the reaction, the thick paste state of the polymerization mass corresponds to a conversion of vinyl chloride to polymer of about 30% to about 40% by weight, and about 8% to 35% by weight of the vinyl chloride is removed by venting from said presurized polymerization mass and said polyolefin terpolymers contain a diene as a monomeric unit.

Claim 33

The process of claim 30 wherein the vinyl chloride is vented from the polymerization mass at a rate of about 0.1 to 1.5% by weight vinyl chloride per minute based on vinyl chloride charged to the polymerization, the polymerization temperature is from about 40° to about 80° centigrade at autogeneous superatmospheric pressure, the diene of the polyolefin terpolymer is selected from the group consisting of dicyclopentadiene, 1,3-butadiene and non-conjugated dienes with linear or cyclic chains and is present in said terpolymer in a proportion up to about 15% by weight of said terpolymer and the effective concentration of polyolefin in the polymerization mass is about 5.5% to about 10% by weight.

Claim 34

The process of claim 31 wherein the diene of the polyolefin terpolymer is present in said terpolymer in a proportion up to about 6% by weight of said terpolymer.

Claim 35

The process of claim 32 wherein the polymerization temperature is from about 50° to about 75° centigrade, the initiator is an organic peroxy- or azo compound added to the polymerization mass in a concentration of about 0.01% to about 1.0% based on the weight of vinyl chloride, the effective concentration of polyolefin is about 6% to about 9% by weight based on vinyl chloride and the vinyl chloride is vented from the polymerization mixture at a rate of about 0.15% to 1.2% per minute, said venting commencing about 5 to about 15 minutes after onset of the thick paste state in the polymerization.

Claim 36

The process of claim 33 wherein the initiator is an organic peroxide, and the vinyl chloride is vented from the polymerization mixture at a rate of about 0.3% to about 1.2% per minute.

Claim 37

The process of claim 34 wherein the polyolefin is an olefin copolymer or terpolymer.

Claim 38

The process of claim 35 wherein the polyolefin is ethylene-propylene ethylidene norbornene terpolymer.

Claim 39

The process of claim 35 wherein the polyolefin is an ethylene-propylene 1,4-hexadiene terpolymer.

Claim 40

The process of claim 35 wherein the polyolefin is an ethylene-propylene copolymer.

Claim 41

The process of claim 35 wherein the polyolefin is a butene-1-ethylene copolymer.

Claim 42

The process of claim 34 wherein the polyolefin is an olefin homopolymer.

Claim 43

The process of claim 40 wherein the olefin homopolymer is polyethylene.

Claim 44

The process of claim 40 wherein the olefin homopolymer is polypropylene.

Claim 45

The process of claim 34 wherein the halogenated polyolefin is chlorinated polyolefin.

Claim 46

The process of claim 43 wherein the halgenated polyolefin is chlorinated polyethylene.

Claim 47

The process of claim 25 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 polymers 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 polymerization has been completed, said polyolefin or mixture of polyolefins being introduced to the reaction mixture at the beginning of the second reaction stage so that the thick paste state of the polymerization and the removal therein of vinyl halide takes place in said second reaction stage.

Claim 48

The process of claim 45 wherein a portion, amounting to at least about 50% by weight, of the monomer or monomers charged to the polymerization reaction are added in the first stage, the balance of the monomer or monomers being added at about the beginning of the second stage.

Claim 49

The process of claim 45 wherein there is added in the first stage about 50% to about 60% by weight of the monomer or monomers charged to the polymerization reaction.

Claim 50

The process of claim 47 wherein about 3% to about 15% by weight of the monomer or monomers is converted to polymer in the first reaction stage.

Claim 51

The process of claim 48 wherein about 7% to about 15% of monomer or monomers is converted to polymer in the first reaction stage.

Claim 52

The process of claim 49 wherein the monomer reactant is vinyl chloride.

Claim 53

The process of claim 26 wherein the weight average molecular weight of the polyolefin reactant is about 50,000 to about 150,000.

Claim 54

The process of claim 26 wherein the weight average molecular weight of the polyolefin reactant is about 150,000 to about 1,000,000.

Claim 55

In the process for the preparation of a vinyl halide polymer which comprises polymerizing in bulk a vinyl halide monomer, in the liquid phase, either along or in combination with up to about 50% be weight of another ethylenically unsaturated monomer copolymerizable therewith in the initial presence of more than about 1.8% by weight based on said vinyl halide monomer of a polyolefin or mixture of polyolefins having a weight average molecular weight of at least about 50,000, said polyolefin or mixture of polyolefins being 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 removing from the polymerization mass during the thick paste state thereof from about 2% to less than about 50% by weight of the vinyl halide charged to the polymerization mass, the effective concentration of said polyolefin or mixture of polyolefins after said vinyl halide removal being above about 3.5 weight percent based on vinyl halide remaining in said polymerization mass after said removal of vinyl halide whereby a more finely divided particulate product of high impact strength is obtained.

Claim 56

In the process for the preparation of a vinyl halide polymer which comprises polymerizing in bulk a vinyl halide monomer, in the liquid phase, either along or in combination with up to about 50% be weight of another ethylenically unsaturated monomer copolymerizable therewith in the initial presence of more than about 1.8% by weight based on said vinyl halide monomer of a polyolefin or mixture of polyolefins having a weight average molecular weight of at least about 50,000, said polyolefin or mixture of polyolefins being 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 removing from the polymerization mass during the thick paste state thereof from about 2% to less than about 50% by weight of the vinyl halide charged to the polymerization mass, the effective concentration of said polyolefin or mixture of polyolefins after said vinyl halide removal being above about 3.5 weight percent based on vinyl halide remaining in said polymerization mass after said removal of vinyl halide whereby a more finely divided particulate product of high impact strength is obtained.

Claim 57

A high impact strength polyvinyl halide prepared by the process of claim 1.

Claim 58

A high impact strength polyvinyl halide prepared by the process of claim 25.

Claim 59

A high impact strength polyvinyl halide prepared by the process of claim 53.

Claim 60

The process of claim 45 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 61

The process of claim 68 wherein about 50% to about 60% 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.