Chemically-initiated inverse emulsion polymerization with Na, Li/Cl, Br salt

Claim 2

In a chemically initiated water-in-oil emulsion polymerization process for making water-soluble anionic copolymers from at least two water-soluble, ethylenically unsaturated, addition polymerizable monomers, at least one of which is anionic, the improvement comprising: adding a salt selected from the group consisting of NaCl, NaBr, LiCl and LiBr to the aqueous phase of the water-in-oil emulsion prior to polymerization, and dispersing the aqueous phase and oil phase whereby the droplet size of the aqueous phase in the resulting emulsion is about 5 microns or less.

Claim 3

The process of claim 1 wherein the improvement further comprises maintaining the temperature of the water-in-oil emulsion below about 40° C. during polymerization.

Claim 4

The process of claim 1 or 2 wherein the water-soluble, ethylenically unsaturated, addition polymerizable monomers are sodium acrylate and acrylamide.

Claim 5

The process of claim 1 or 2 wherein the salt is NaCl.

Claim 6

The process of claim 2 wherein the water-soluble, ethylenically unsaturated, addition polymerizable monomers are sodium acrylate and acrylamide and the salt is NaCl.

Claim 7

In a chemically initiated water-in-oil emulsion polymerization process for making water-soluble anionic copolymers from at least two water-soluble, ethylenically unsaturated, addition polymerizable monomers, at least one of which is an anionic monomer selected from the group consisting of (a) monomers conforming to the formula ##STR7## wherein R represents hydrogen or methyl, Y represents --NH 2 , --OM, or ##STR8## and wherein M is hydrogen, H 4 N + , alkali metal, or a cation yielding a water-soluble polymerizable compound, (b) vinyl sulfonic acid, (c) alkali metal salts of vinyl sulfonic acid, (d) diacetone acrylamide, and (e) mixtures thereof, the improvement comprising adding to the emulsion prior to polymerization a water-soluble salt selected from the group consisting of NaCl, NaBr, LiCl, and LiBr, said salt comprising from about 2% by weight, based on the weight of the total emulsion, up to the saturation level of the salt in the aqueous phase of the emulsion at the temperature of polymerization, and the droplet size of the aqueous phase in the emulsion being about 5 microns or less.

Claim 8

In a chemically initiated water-in-oil emulsion polymerization process for making water-soluble anionic copolymers from at least two water-soluble, ethylenically unsaturated, addition polymerizable monomers, at least one of which is an anionic monomer selected from the group consisting of (a) monomers conforming to the formula ##STR7## wherein R represents hydrogen or methyl, Y represents --NH 2 , --OM, or ##STR8## and wherein M is hydrogen, H 4 N + , alkali metal, or a cation yielding a water-soluble polymerizable compound, (b) vinyl sulfonic acid, (c) alkali metal salts of vinyl sulfonic acid, (d) diacetone acrylamide, and (e) mixtures thereof, the improvement comprising adding to the emulsion prior to polymerization a water-soluble salt selected from the group consisting of NaCl, NaBr, LiCl, and LiBr, said salt comprising from about 2% by weight, based on the weight of the total emulsion, up to the saturation level of the salt in the aqueous phase of the emulsion at the temperature of polymerization, and the droplet size of the aqueous phase in the emulsion being about 5 microns or less.

Claim 9

The process of claim 6 wherein the improvement further comprises maintaining the temperature of the water-in-oil emulsion below about 40° C. during polymerization.

Claim 10

The process of claims 6 or 7 in which aqueous phase comprises from about 70% to about 75% by weight and the oil phase comprises from about 30% to about 25% by weight, based on the weight of the water-in-oil emulsion and the salt is sodium chloride.

Claim 11

The process of claim 6 in which the droplet size of the aqueous phase in the emulsion is about one micron or less.

Claim 12

The process of claim 9 wherein the improvement further comprises maintaining the temperature of the water-in-oil emulsion below about 40° C. during polymerization.