Process for the bulk polymerization of vinyl halide polymers showing reduced reactor scale formation

Claim 2

In the process for the preparation of a vinyl halide polymer by bulk liquid phase polymerization carried out in the presence of an initiating amount of a free radical initiator for vinyl halide polymerization, the improvement comprising the steps of: 1. admixing a vinyl halide monomer composition with about 0.02 to about 0.3% water by weight based upon total monomer, and an organic or inorganic inert fine particle size material which is solid at least at reaction temperatures, is insoluble in said monomer, and consists essentially of particles having an average particle size in the range of about 0.001 to about 50 microns, the amount of water employed being about 27 to about 83 percent by weight of the inert fine particle size additive; 2. polymerization in a first stage using high speed agitation at a temperature of from about 30° to about 80° C. until about 3% to about 20% by weight of said monomer composition has been converted to polymer particles and

Claim 3

continuing said polymerization in a second stage during which the reaction mixture is subjected to low speed agitation until at least about 30% by weight of the reaction mixture has been converted to polymer comprising said inert fine particle size material.

Claim 4

continuing said polymerization in a second stage during which the reaction mixture is subjected to low speed agitation until at least about 30% by weight of the reaction mixture has been converted to polymer comprising said inert fine particle size material.

Claim 5

The process of claim 1 wherein said water is added in said first stage, said second stage, or in both said stages.

Claim 6

In the process for the preparation of small particle size polymer of vinyl halide by bulk liquid phase polymerization carried out in the presence of an initiating amount of a free radical initiator for vinyl halide polymerization the improvement which comprises the steps of: 1. polymerization of a vinyl halide monomer composition in a first stage using high speed agitation at a temperature of from about 30 to about 70 degrees centigrade in contact with about 0.02 to about 3% water by weight based upon total monomer and at least one of: a. an additive of an inorganic or organic, inert fine particle size material which is solid at least at reaction temperature, is insoluble in said monomer, and consists essentially of particles having an average particle size in the range of about 0.001 to about 50 microns said material being present in the amount of 0.001 to 5% based upon said monomer composition in said first stage, so that the amount of water employed therein is about 27 to about 83 percent by weight of the weight of the inert fine particle size additive, and b. said additive and a surface active agent in an amount of 0.01 to 5% by weight based upon said monomer present in said first stage; until about 3% to about 20% by weight of said monomer composition has been converted to polymer particles, 2. continuing the preparation of small particle size polymers by polymerization in a second stage during which the reaction mixture is subjected to low speed agitation until about 30 to about 80% by weight of the reaction mixture has been converted to base polymer, 3. introducing additional monomer into said second stage comprising at least one vinyl halide monomer or at least one co-monomer which co-polymerizes therewith or mixtures thereof and 4. carrying out the subsequent polymerization in said second stage to provide non-porous polymer particles comprising said fine particle size inert material by increasing the second stage polymerization temperature after about 30 to about 80% by weight of said reaction mixture has been converted to polymer, from a range of about 30° to about 70° centigrade to a range of about 60° to 80° centigrade, said increase in polymerization temperature being about 10° to about 50° centigrade.

Claim 7

In the process for the preparation of small particle size polymer of vinyl halide by bulk liquid phase polymerization carried out in the presence of an initiating amount of a free radical initiator for vinyl halide polymerization the improvement which comprises the steps of: 1. polymerization of a vinyl halide monomer composition in a first stage using high speed agitation at a temperature of from about 30 to about 70 degrees centigrade in contact with about 0.02 to about 3% water by weight based upon total monomer and at least one of: a. an additive of an inorganic or organic, inert fine particle size material which is solid at least at reaction temperature, is insoluble in said monomer, and consists essentially of particles having an average particle size in the range of about 0.001 to about 50 microns said material being present in the amount of 0.001 to 5% based upon said monomer composition in said first stage, so that the amount of water employed therein is about 27 to about 83 percent by weight of the weight of the inert fine particle size additive, and b. said additive and a surface active agent in an amount of 0.01 to 5% by weight based upon said monomer present in said first stage; until about 3% to about 20% by weight of said monomer composition has been converted to polymer particles, 2. continuing the preparation of small particle size polymers by polymerization in a second stage during which the reaction mixture is subjected to low speed agitation until about 30 to about 80% by weight of the reaction mixture has been converted to base polymer, 3. introducing additional monomer into said second stage comprising at least one vinyl halide monomer or at least one co-monomer which co-polymerizes therewith or mixtures thereof and 4. carrying out the subsequent polymerization in said second stage to provide non-porous polymer particles comprising said fine particle size inert material by increasing the second stage polymerization temperature after about 30 to about 80% by weight of said reaction mixture has been converted to polymer, from a range of about 30° to about 70° centigrade to a range of about 60° to 80° centigrade, said increase in polymerization temperature being about 10° to about 50° centigrade.

Claim 8

The process of claim 3 wherein 1 to 200% by weight of said additional monomer based upon the weight of the resultant converted base polymer or copolymer is added all at once.

Claim 9

The process of claim 4 wherein the monomer composition polymerized in said first stage is vinyl chloride and the monomer added in said second stage is vinyl chloride.

Claim 10

The process of claim 5 wherein a polyolefin is present in the proportion of about 0.05 to about 2.5 percent by weight based upon said vinyl halide monomer or monomers.

Claim 11

The process of claim 5 wherein said additive consists of a fumed silica.

Claim 12

The process of claim 5 wherein said surface active agent is octyl phenoxy polyethoxyethanol.

Claim 13

In a process for the preparation of a polymer of vinyl halide by bulk liquid phase polymerization comprising the steps of: 1. polymerization of a vinyl halide monomer in a first stage with high speed agitation at a temperature of from about 30° to about 80° centigrade until about 3% to about 20% by weight of said monomer has been converted to polymer, and 2. continuing the preparation of said polymer in said second stage with low speed agitation until about 30 to about 95% by weight of said reaction mixture has been converted to polymer and then introducing at least one comonomer copolymerizable therewith in the presence of said polymers; the improvement which comprises conducting said polymerization in contact with at least one of a. water and an additive of an organic or inorganic inert fine particle size material which is solid at least at reaction temperature, is insoluble in said monomer; and consists essentially of particles having an average particle size in the range of about 0.001 to about 50 microns, b. water, said additive, and a polyolefin; or c. water, said additive, a surface active agent and a polyolefin, the amount of water employed in each of (a), (b) and (c) being about 27 to about 83 percent by weight of the inert fine particle size additive.

Claim 14

In a process for the preparation of a polymer of vinyl halide by bulk liquid phase polymerization comprising the steps of: 1. polymerization of a vinyl halide monomer in a first stage with high speed agitation at a temperature of from about 30° to about 80° centigrade until about 3% to about 20% by weight of said monomer has been converted to polymer, and 2. continuing the preparation of said polymer in said second stage with low speed agitation until about 30 to about 95% by weight of said reaction mixture has been converted to polymer and then introducing at least one comonomer copolymerizable therewith in the presence of said polymers; the improvement which comprises conducting said polymerization in contact with at least one of a. water and an additive of an organic or inorganic inert fine particle size material which is solid at least at reaction temperature, is insoluble in said monomer; and consists essentially of particles having an average particle size in the range of about 0.001 to about 50 microns, b. water, said additive, and a polyolefin; or c. water, said additive, a surface active agent and a polyolefin, the amount of water employed in each of (a), (b) and (c) being about 27 to about 83 percent by weight of the inert fine particle size additive.

Claim 15

The process of claim 9 wherein said polyolefin is present in the proportion of about 0.05 to about 2.5% by weight based upon said vinyl halide monomer.

Claim 16

The process of claim 9 wherein the monomer composition polymerized in the first stage is vinyl chloride and the co-monomer added in said second stage is an acrylate monomer or mixtures thereof, the homopolymers of which have a glass transition temperature of 10° C or below.

Claim 17

A process for the preparation of a vinyl halide polymer comprising bulk polymerizing in liquid phase a first component comprising at least one vinyl halide monomer and at least one ethylenically unsaturated comonomer copolymerizable therewith in contact with (1) a second component comprising a polyolefin and an additive of an organic or inorganic inert fine particle size material which is solid at least at reaction temperature, which is insoluble in said monomer and which consists essentially of particles having an average particle size in the range of about 0.001 to about 50 microns and water, or water and said additive, wherein said water is present in the amount of about 0.02 to about 0.3% by weight based on said monomer and of about 27 to about 83 percent by weight of the inert fine particle size additive, and (2) a vinyl halide based polymer seed in powder form produced by bulk, suspension or emulsion polymerization processess.

Claim 18

A process for the preparation of a vinyl halide polymer comprising bulk polymerizing in liquid phase a first component comprising at least one vinyl halide monomer and at least one ethylenically unsaturated comonomer copolymerizable therewith in contact with (1) a second component comprising a polyolefin and an additive of an organic or inorganic inert fine particle size material which is solid at least at reaction temperature, which is insoluble in said monomer and which consists essentially of particles having an average particle size in the range of about 0.001 to about 50 microns and water, or water and said additive, wherein said water is present in the amount of about 0.02 to about 0.3% by weight based on said monomer and of about 27 to about 83 percent by weight of the inert fine particle size additive, and (2) a vinyl halide based polymer seed in powder form produced by bulk, suspension or emulsion polymerization processess.

Claim 19

The process of claim 12 wherein said polyolefin is present in a proportion of about 0.05 to about 2.5% by weight based upon said vinyl halide monomer or monomers.

Claim 20

The process of claim 12 wherein said vinyl halide monomer is vinyl chloride and said comonomer is an acrylate monomer or mixtures thereof, the homopolymers of which have a glass transition temperature of 10° C or below.