Semisuspension polymerization processes

Claim 2

A process for the preparation of polymeric particles which comprises mixing at least one monomer with a polymerization initiator, a crosslinking component and a chain transfer component; effecting bulk polymerization until from about 10 to about 50 weight percent of the monomer has been polymerized; dispersing with a high shear mixer the aforementioned partially polymerized product in water containing a stabilizing component selected from a group consisting of non-ionic and ionic water soluble polymeric stabilizers to obtain a suspension of particles with an average diameter of from about 0.1 to about 5 microns in water; and polymerizing the resulting suspension.

Claim 3

A process in accordance with claim 1 wherein a mixture of monomers is selected.

Claim 4

A process in accordance with claim 2 wherein the mixture contains from 2 monomers to about 20 monomers.

Claim 5

A process in accordance with claim 1 wherein the polymerized product obtained is subjected to washing and drying.

Claim 6

A process in accordance with claim 1 wherein the polymeric particles obtained have an average particle diameter of from about 0.1 micron to about 5 microns.

Claim 7

A process in accordance with claim 1 wherein heating is accomplished at a temperature of from about 45° C. to about 120° C.

Claim 8

A process in accordance with claim 1 wherein the number and weight average molecular weight of the bulk polymerization product is between about 5,000 to about 500,000 and about 10,000 to about 1,000,000, respectively.

Claim 9

A process in accordance with claim 1 wherein the number and weight average molecular weight of the final polymer product is between about 5,000 to about 500,000 and about 10,000 to about 2,000,000, respectively.

Claim 10

A process in accordance with claim 1 wherein the dispersion of the partially polymerized monomer in water containing the stabilizing component is accomplished with a high shear mixer.

Claim 11

A process in accordance with claim 1 wherein the monomer is selected from the group consisting of styrene and its derivatives.

Claim 12

A process in accordance with claim 1 wherein the monomer is selected from the group consisting of α-methyl-styrene, p-chlorostyrene, monocarboxylic acids and the derivatives thereof; dicarboxylic acids with a double bond and their derivatives; vinyl ketones; vinyl naphthalene; unsaturated mono-olefins; vinylidene halides; N-vinyl compounds; and mixtures thereof.

Claim 13

A process in accordance with claim 1 wherein the monomer is selected from the group consisting of acrylic acid, methyl acrylate, ethyl acrylate, butyl acrylate, dodecyl acrylate, octyl acrylate, phenyl acrylate, methacrylic acids, methyl methacrylate, ethyl methacrylate, butyl methacrylate, octyl methacrylate, acrylonitrile and acrylamide; maleic acid, monobutyl maleate, dibutyl maleate; vinyl chloride, vinyl acetate and vinyl benzoate; vinylidene chloride and N-vinyl pyrrole.

Claim 14

A process in accordance with claim 1 wherein the polymerization initiator is selected from the group consisting of azo compounds and peroxides.

Claim 15

A process in accordance with claim 13 wherein the polymerization initiator is benzoyl peroxide, lauryl peroxide, 1-1-(t-butylperoxy)-3,3,5-trimethylcyclohexane, n-butyl-4,4-di-(t-butylperoxy)valerate, dicumyl peroxide, 2,2'azodimethylvaleronitrile, 2,2'azoisobutyronitrile, azobiscyclohexanenitrile, or 2-methylbutronitrile.

Claim 16

A process in accordance with claim 1 wherein the stabilizing component is selected from the group consisting of methyl cellulose, ethyl cellulose, hydroxypropyl cellulose, the sodium salt of carboxyl methyl cellulose, polyacrylate acids and their salts, polyvinyl alcohol, gelatins, starches, gums, alginates, zein and casein.

Claim 17

A process in accordance with claim 1 wherein the stabilizing component is tricalcium phosphate, talc or barium sulfate.

Claim 18

A process in accordance with claim 1 wherein the crosslinking component is selected from a group consisting of compounds having two or more polymerizable double bonds.

Claim 19

A process in accordance with claim 1 wherein the crosslinking component is divinylbenzene, divinylnaphthalene, ethylene glycol diacrylate, or divinylether.

Claim 20

A process in accordance with claim 1 wherein the chain transfer component is selected from a group consisting of mercaptans and halogenated hydrocarbons.

Claim 21

A process in accordance with claim 19 wherein the chain transfer component is carbon tetrachloride, butylmercaptan, or laurylmercaptan.

Claim 22

A process for the preparation of polymeric particles useful for powder coating which comprises mixing at least one monomer with a polymerization initiator, a crosslinking component and a chain transfer component; effecting bulk polymerization until from about 10 to about 50 weight percent of the monomer has been polymerized; dispersing with a high shear mixer the aforementioned partially polymerized product in water containing a stabilizing component selected from a group consisting of non-ionic and ionic water soluble polymeric stabilizers to obtain a suspension of particles with an average diameter of from about 0.1 to about 0.8 micron; and polymerizing the resulting suspension wherein bulk and suspension polymerization is accomplished by heating at a temperature of from about 30° C. to about 200° C.

Claim 23

A process for the preparation of polymeric particles useful for powder coating which comprises mixing at least one monomer with a polymerization initiator, a crosslinking component and a chain transfer component; effecting bulk polymerization until from about 10 to about 50 weight percent of the monomer has been polymerized; dispersing with a high shear mixer the aforementioned partially polymerized product in water containing a stabilizing component selected from a group consisting of non-ionic and ionic water soluble polymeric stabilizers to obtain a suspension of particles with an average diameter of from about 0.1 to about 0.8 micron; and polymerizing the resulting suspension wherein bulk and suspension polymerization is accomplished by heating at a temperature of from about 30° C. to about 200° C.

Claim 24

A process in accordance with claim 21 wherein a mixture of monomers is selected.

Claim 25

A process in accordance with claim 21 wherein the mixture contains from 2 monomers to about 20 monomers.

Claim 26

A process in accordance with claim 21 wherein the polymerized product obtained is subjected to washing and drying.

Claim 27

A process in accordance with claim 21 wherein bulk and suspension polymerization is accomplished by heating to a temperature between about 30° C. to about 200° C.

Claim 28

A process in accordance with claim 21 wherein the number and weight average molecular weight of the polymer produced in the bulk polymerization step is between about 5,000 to about 50,000 and about 10,000 to about 100,000, respectively.

Claim 29

A process in accordance with claim 21 wherein the number and weight average molecular weight of the final polymeric product particles are between about 10,000 to about 40,000 and about 200,000 to about 500,000, respectively.

Claim 30

A process in accordance with claim 21 wherein the dispersion of partially polymerized monomer or comonomers in water containing the stabilizing component is accomplished with a high shear mixer.

Claim 31

A process in accordance with claim 21 wherein the monomer is selected from vinyl monomers consisting of styrene and its derivatives, monocarboxylic acids and the derivatives thereof; dicarboxylic acids with a double bond and the derivatives thereof; vinyl ketones; vinyl ethers; vinyl naphthalene; unsaturated mono-olefins; vinylidene halides; N-vinyl compounds; or mixtures thereof.

Claim 32

A process in accordance with claim 21 wherein the polymerization initiator is selected from the group consisting of 2,2'azodimethylvaleronitrile, 2,2'azoisobutyronitrile, azobiscyclohexanenitrile, 2-methylbutronitrile, benzoyl peroxide, lauryl peroxide, 1-1-(t-butylperoxy)-3,3,5-trimethylcyclohexane, n-butyl-4,4-di-(t-butylperoxy)valerate, or dicumyl peroxide.

Claim 33

A process in accordance with claim 21 wherein a crosslinking component is selected from a group consisting of divinylbenzene, divinylnaphthalene, ethylene glycol diacrylate, divinylether and the like.

Claim 34

A process in accordance with claim 21 wherein the chain transfer component is selected from a group consisting of mercaptans such as butylmercaptan, laurylmercaptan, and halogenated carbons.

Claim 35

A process in accordance with claim 21 wherein the polymer particles can be selected for the coating of carrier cores.

Claim 36

A process in accordance with claim 1 wherein the resulting particles are selected as a resin component for toner compositions.

Claim 37

A process in accordance with claim 21 wherein the resulting particles are selected as a resin component for toner compositions.