Method of producing toner particles by in-situ polymerization and imaging process

Claim 2

A process for producing colored toner particles comprising admixing a colorant with a first organic monomer to form an organic phase; maintaining said organic phase under continuous agitation; admixing a polymerization initiator with said organic phase; admixing said organic phase with an aqueous phase containing a suspending agent therein under polymerization conditions to form a suspension; polymerizing said suspension to provide polymer particles containing said colorant and having a particle size in the range of 1 to about 100 microns; admixing a second monomer of a tough polymer with the polymer particles under continuous agitation for a period of time sufficient to enable the monomer to diffuse into the polymer particles; admixing a water soluble polymerization initiator with the polymer particles under polymerization conditions in said aqueous phase; polymerizing said second monomer; and thereafter recovering the polymer particles.

Claim 3

A process as defined in claim 1 wherein said second monomer is a vinyl monomer.

Claim 4

A process as defined in claim 1 wherein the colorant is an insoluble pigment.

Claim 5

A process as defined in claim 1 wherein the colorant is a soluble dye.

Claim 6

A process as defined in claim 1 wherein the colorant is photosensitive.

Claim 7

A process as defined in claim 1 wherein the amount of colorant employed ranges from about 2 to about 15 weight percent based on the weight of said first monomer.

Claim 8

A process as defined in claim 1 wherein from about 0.5 to about 1 weight percent of a surfactant based on the weight of said first monomer is admixed with the organic phase.

Claim 9

A process as defined in claim 1 wherein the dispersion of colorant in the organic phase is stabilized by the addition of from about 1 to about 20 weight percent based on the weight of the monomer of a polymer soluble in said first monomer.

Claim 10

A process as defined in claim 1 wherein from about 0.5 to about 5 weight percent polymerization initiator based on the weight of said first monomer is admixed with the organic phase.

Claim 11

A process as defined in claim 1 wherein the suspending agent is a water soluble polymer.

Claim 12

A process as defined in claim 10 wherein from about 1 to about 10 weight suspending agent based on the weight of water is employed.

Claim 13

A process as defined in claim 1 wherein the organic phase is admixed with the aqueous phase at speeds of from about 1000 to about 3000 rpm.

Claim 14

A process as defined in claim 1 wherein the volumetric ratio of organic phase to aqueous phase ranges from about 0.05:1 to about 0.4:1.

Claim 15

A process as defined in claim 1 wherein the first polymerization is effected at temperatures ranging from 60° to about 90° C with continuous agitation at speeds ranging from about 300 to 1000 rpm.

Claim 16

A process as defined in claim 1 wherein the colorant is carbon black and the first polymerization initiator is azobisisobutyronitrile.

Claim 17

A process as defined in claim 1 wherein the polymer particles after the polymerization of said second monomer are rendered moisture insensitive by treatment with an insolublizing agent.

Claim 18

A process as defined in claim 1 wherein after completion of the first polymerization, the reaction system is heated at a temperature ranging from about 60° to about 90° C for a sufficient period of time to remove any residual polymerization initiator; admixing from about 5 to about 10 weight percent, based on the weight of polymer particles, of styrene with said polymer particles with continuous stirring for a sufficient period of time to enable the styrene to diffuse into the polymer particles.

Claim 19

A process as defined in claim 17 wherein the diffusion period ranges from about 0.5 to about 2 hours.

Claim 20

A process as defined in claim 17 wherein, upon completion of the diffusion period, from about 0.1 to about 10 weight percent based on the weight of the monomer of a water soluble initiator is admixed with the polymer particles and polymerization is effected by heating said polymer particles at tempertures ranging from about 60° to about 80° C with continuous agitation.

Claim 21

A process as defined in claim 19 wherein the water soluble initiator is potassium persulfate.

Claim 22

A process as defined in claim 19 wherein the water soluble initiator is ammonium persulfate.

Claim 23

The process of claim 1 wherein the polymer particles are rendered moisture insensitive after the polymerization of said second monomer by treatment with a material selected from the group of melamine formaldehyde resins, toluene diisocyanate and dimethylolurea.

Claim 24

An electrostatographic developer composition comprising a mixture of finely-divider toner particles and a solid or liquid vehicle therefor, said toner particles being prepared by admixing a colorant with at least one organic monomer to form an organic phase; maintaining said organic phase under continuous agitation; admixing a polymerization initiator with said organic phase; admixing said organic phase with an aqueous phase containing a suspending agent therein under polymerization conditions to form a suspension; polymerizing said suspension to provide polymer particles containing said colorant and having a particle size in the range of 1 to about 100 microns; admixing a second monomer of a tough polymer with the polymer particles under continuous agitation for a period of time sufficient to enable the monomer to diffuse into the polymer particles; admixing a water soluble polymerization initiator with the polymer particles under polymerization conditions in said aqueous phase; polymerizing said second monomer; and thereafter, recovering said polymer particles.

Claim 25

An electrostatographic developer composition comprising a mixture of finely-divider toner particles and a solid or liquid vehicle therefor, said toner particles being prepared by admixing a colorant with at least one organic monomer to form an organic phase; maintaining said organic phase under continuous agitation; admixing a polymerization initiator with said organic phase; admixing said organic phase with an aqueous phase containing a suspending agent therein under polymerization conditions to form a suspension; polymerizing said suspension to provide polymer particles containing said colorant and having a particle size in the range of 1 to about 100 microns; admixing a second monomer of a tough polymer with the polymer particles under continuous agitation for a period of time sufficient to enable the monomer to diffuse into the polymer particles; admixing a water soluble polymerization initiator with the polymer particles under polymerization conditions in said aqueous phase; polymerizing said second monomer; and thereafter, recovering said polymer particles.

Claim 26

Electrostatographic developer composition as defined in claim 23 comprising from about 10 to 200 parts by weight of solid or liquid vehicle per part by weight of toner particles.

Claim 27

An electrostatic imaging process comprising the steps of forming an electrostatic latent image on an imaging surface and developing said electrostatic latent image with the developer composition of claim 23 whereby at least a portion of said finelydivided toner particles is attracted to and held on said surface in conformance with said electrostatic latent image to form a developed latent electrostatic image.

Claim 28

An electrostatic latent image process as defined in claim 25 wherein the developed electrostatic latent image is electrostatically transferred to a second surface and said transferred image is fused onto said second surface.