Process for the manufacture of aqueous ethylene/vinyl chloride/vinyl alkanoate and/or alkyl acrylate copolymer dispersions having a non-uniform particle size distribution

Claim 2

Aqueous ethylene/vinyl chloride/vinyl alkanoate and/or alkyl acrylate copolymer dispersions having a non-uniform particle size, in which one particle size distribution maximum is at 0.03 to 0.2μ and a second maximum is at 0.15 to 1μ where said second maximum particle size range differs from the first by at least 0.1μ and wherein the mass of particles in the particle size distribution curve of the second maximum is from 5% to 60% of the total mass of particles, said dispersion having a solids content of between 20% and 70% by weight and an emulsifier content of from 0.5% to 10% by weight, based on the total amount of monomers, said copolymer consisting of: from 20% to 92% by weight of vinyl chloride units, from 5% to 60% by weight of ethylene units, from 3% to 75% by weight of monomer units selected from the group consisting of: (1) vinyl esters of unbranched alkanoic acids having from 1 to 18 carbon atoms, (2) vinyl esters of branched alkanoic acids having from 4 to 18 carbon atoms, (3) acrylic acid esters of unbranched alkanols having from 1 to 12 carbon atoms, (4) acrylic acid esters of branched alkanols having from 3 to 12 carbon atoms, and (5) mixtures thereof, and from 0 to 15% by weight of other monomer units copolymerizable with ethylene and vinyl chloride.

Claim 3

The aqueous copolymer dispersion of claim 1 wherein said copolymer consists of: from 45% to 85% by weight of said vinyl chloride units, from 5% to 30% by weight of said ethylene units, and from 5% to 35% by weight of said monomer units,

Claim 4

The aqueous copolymer dispersion of claim 2 wherein said emulsifier content is from 2% to 6% by weight, based on the total amount of monomers.

Claim 5

The aqueous copolymer dispersion of claim 2 having a further content of from 1.5% to 4% by weight, based on the weight of monomers, of water-soluble auxilliary monomer units copolymerizable with vinyl chloride and ethylene.

Claim 6

The aqueous copolymer dispersion of claim 4 wherein said monomer units are vinyl acetate units.

Claim 7

A process for the production of an aqueous ethylene/vinyl chloride/vinyl alkanoate and/or alkyl acrylate copolymer dispersion wherein said copolymer consists of: from 20% to 92% by weight of vinyl chloride units, from 5% to 60% by weight of ethylene units, from 3% to 75% by weight of monomer units selected from the group consisting of: (1) vinyl esters of unbranched alkanoic acids having from 1 to 18 carbon atoms, (2) vinyl esters of branched alkanoic acids having from 4 to 18 carbon atoms, (3) acrylic acid esters of unbranched alkanols having from 1 to 12 carbon atoms, (4) acrylic acid esters of branched alkanols having from 3 to 12 carbon atoms, and (5) mixtures thereof, and from 0 to 15% by weight of other monomer units copolymerizable with ethylene and vinyl chloride, having a non-uniform particle size, in which one particle size distribution maximum is at 0.03 to 2.0μ and a second maximum is at 0.15 to 1μ, where said second maximum particle size range differs from the first by at least 0.1μ and wherein the mass of particles in the particle size distribution curve of the second maximum is from 5% to 60% of the total mass of particles, said copolymer dispersion having a solids content of between 20% and 70% by weight and an emulsifier content of from 0.5% to 10% by weight, based on the total amount of monomers consisting essentially of heating substantially all of the water and at least some of the total amount of vinyl chloride, ethylene, said monomer units, and, optionally, said other monomer units to a temperature of between 0° and 90° C. and at an ethylene pressure of between 1 and 150 bar in the presence of a free-radical polymerization catalyst under agitation, and after a monomer conversion of from 1% to 60% by weight metering in from 0.5% to 10% by weight, based on the total amount of solid copolymer, of at least one polymerization emulsifier, together with the remainder of said water, said vinyl chloride, said ethylene, said monomer units, as well, optionally, of said other monomer units, while maintaining said agitation, temperature and ethylene pressure for a time sufficient to complete monomer polymerization, and recovering said copolymer dispersion.

Claim 8

A process for the production of an aqueous ethylene/vinyl chloride/vinyl alkanoate and/or alkyl acrylate copolymer dispersion wherein said copolymer consists of: from 20% to 92% by weight of vinyl chloride units, from 5% to 60% by weight of ethylene units, from 3% to 75% by weight of monomer units selected from the group consisting of: (1) vinyl esters of unbranched alkanoic acids having from 1 to 18 carbon atoms, (2) vinyl esters of branched alkanoic acids having from 4 to 18 carbon atoms, (3) acrylic acid esters of unbranched alkanols having from 1 to 12 carbon atoms, (4) acrylic acid esters of branched alkanols having from 3 to 12 carbon atoms, and (5) mixtures thereof, and from 0 to 15% by weight of other monomer units copolymerizable with ethylene and vinyl chloride, having a non-uniform particle size, in which one particle size distribution maximum is at 0.03 to 2.0μ and a second maximum is at 0.15 to 1μ, where said second maximum particle size range differs from the first by at least 0.1μ and wherein the mass of particles in the particle size distribution curve of the second maximum is from 5% to 60% of the total mass of particles, said copolymer dispersion having a solids content of between 20% and 70% by weight and an emulsifier content of from 0.5% to 10% by weight, based on the total amount of monomers consisting essentially of heating substantially all of the water and at least some of the total amount of vinyl chloride, ethylene, said monomer units, and, optionally, said other monomer units to a temperature of between 0° and 90° C. and at an ethylene pressure of between 1 and 150 bar in the presence of a free-radical polymerization catalyst under agitation, and after a monomer conversion of from 1% to 60% by weight metering in from 0.5% to 10% by weight, based on the total amount of solid copolymer, of at least one polymerization emulsifier, together with the remainder of said water, said vinyl chloride, said ethylene, said monomer units, as well, optionally, of said other monomer units, while maintaining said agitation, temperature and ethylene pressure for a time sufficient to complete monomer polymerization, and recovering said copolymer dispersion.

Claim 9

The process of claim 6 wherein said temperature is between 10° and 50° C.

Claim 10

The process of claim 6 wherein said ethylene pressure is between 10 and 100 bar.

Claim 11

The process of claim 6 wherein said monomer conversion is from 1% to 40% when said emulsifier metering in is begun.

Claim 12

The process of claim 6 wherein said copolymer consists of: from 45% to 85% by weight of said vinyl chloride units, from 5% to 30% by weight of said ethylene units, and from 5% to 35% by weight of said monomer units.

Claim 13

The process of claim 6 wherein said emulsifier content is from 2% to 6% by weight, based on the total amount of monomers.

Claim 14

The process of claim 6 wherein said copolymer has a further content of from 1.5% to 4% by weight, based on the weight of monomers, of water-soluble auxilliary monomer units copolymerizable with vinyl chloride and ethylene.

Claim 15

The process of claim 12 wherein said monomer units are vinyl acetate units.