Claims
- 1. A process for producing a toner, comprising the steps of;
- preparing a polymerizable monomer composition containing at least styrene monomer-containing polymerizable monomers, a colorant, a polyester resin, a release agent and a polymerization initiator; said polyester resin containing a tetrahydrofuran-soluble matter having a weight average molecular weight Mw.sub.2 of from 7,000 to 50,000 and an ethyl alcohol-soluble matter having a weight average molecular weight Mw.sub.3 of from 1,000 to 7,000; Mw.sub.2 /Mw.sub.3 being from 1.2 to 10;
- dispersing said polymerizable monomer composition in an aqueous medium to form granules of the polymerizable monomer composition;
- causing the localization of polyester resin on the surfaces of the particles of the polymerizable monomer composition;
- polymerizing the polymerizable monomers present in the granules to produce a binder resin to form toner particles; said binder resin being a styrene polymer, a styrene copolymer, or a mixture of these, and having a weight average molecular weight Mw.sub.1 of from 10,000 to 1,000,000; and
- adding a water-soluble polymerization initiator in the aqueous medium to treat the surfaces of the toner particles.
- 2. The process according to claim 1, wherein said water-soluble polymerization initiator is a persulfate.
- 3. The process according to claim 2, wherein said persulfate is potassium persulfate or ammonium persulfate.
- 4. The process according to claim 1, wherein said water-soluble polymerization initiator is added in the aqueous medium in an amount of from 0.01 part by weight to 5 parts by weight based on 100 parts by weight of the toner particles.
- 5. The process according to claim 4, wherein said toner particles are dispersed in said aqueous medium in an amount of from 300 parts by weight to 3,000 parts by weight based on 100 parts by weight.
- 6. The process according to claim 4, wherein said aqueous medium is heated to 50.degree. C. to 90.degree. C.
- 7. The process according to claim 4, wherein said toner particles are surface-treated with said water-soluble polymerization initiator in said aqueous medium for 60 minutes to 600 minutes.
- 8. The process according to claim 1, wherein said aqueous medium has a pH of from 6.8 to 11.
- 9. The process according to claim 1, wherein said polyester resin is contained in an amount of from 2 parts by weight to 30 parts by weight based on 100 parts by weight of the binder resin, and contains the ethyl alcohol-soluble matter in an amount of from 0.1% by weight to 20% by weight.
- 10. The process according to claim 1 or 9, wherein said polyester resin has an acid value of 3 mgKOH/g to 35 mgKOH/g.
- 11. The process according to claim 9, wherein said polyester resin is a resin formed from a material composition containing at least an aromatic dicarboxylic acid and a bisphenol type diol.
- 12. The process according to claim 1, wherein said binder resin has a weight average molecular weight Mw.sub.1 of from 50,000 to 900,000, said polyester resin has Mw.sub.2 of from 8,000 to 40,000 and Mw.sub.3 of from 1000 to 5,000.
- 13. The process according to claim 1, wherein said polymerizable monomers contain a styrene monomer and an acrylate monomer.
- 14. The process according to claim 1, wherein said polymerizable monomers contain a styrene monomer, an acrylate monomer and divinyl benzene.
- 15. The process according to claim 1, wherein said binder resin contains a toluene-insoluble matter.
- 16. The process according to claim 1, wherein said polymerizable monomers contain a styrene monomer and a methacrylate monomer.
- 17. The process according to claim 1, wherein said polymerizable monomers contain a styrene monomer, a methacrylate monomer and divinyl benzene.
- 18. The process according to claim 1, wherein said release agent is contained in an amount of from 5 parts by weight to 40 parts by weight based on 100 parts by weight of the binder resin.
- 19. The process according to claim 1, wherein said release agent is contained in an amount of from 12 parts by weight to 35 parts by weight based on 100 parts by weight of the binder resin.
- 20. The process according to claim 1, wherein said release agent is contained in said toner particles in an amount of from 10% by weight to 30% by weight.
- 21. The process according to claim 1, wherein said toner particles have a shape factor SF-1 of from 100 to 150.
- 22. The process according to claim 1, wherein said toner particles have a shape factor SF-1 of from 100 to 125.
- 23. The process according to claim 1, wherein said toner particles have a weight average particle diameter of from 3 .mu.m to 8 .mu.m, and a coefficient of number variation of 35% or less.
- 24. The process according to claim 1, wherein said release agent is a solid wax.
- 25. The process according to claim 24, wherein said release agent has a weight average molecular weight of from 300 to 1,500, has a ratio of weight average molecular weight Mw to number average molecular weight Mn, Mw/Mn, of 1.5 or less, has a main endothermic peak in the DSC endothermic curve at a temperature of from 55.degree. C. to 120.degree. C., with a tangent takeoff temperature at 40.degree. C. or above.
- 26. The process according to claim 25, wherein said release agent has the main endothermic peak in the DSC endothermic curve at a temperature of from 60.degree. C. to 90.degree. C., and the peak has a half width of 10.degree. C. or less.
- 27. The process according to claim 26, wherein said release agent has the main endothermic peak having the half width of 5.degree. C. or less.
- 28. The process according to claim 25, wherein said release agent is a solid ester wax.
- 29. The process according to claim 1, wherein said colorant in said polymerizable monomer composition is a cyan colorant.
- 30. The process according to claim 29, wherein said polymerizable monomer composition contains a negative charge control agent.
- 31. The process according to claim 1, wherein said colorant in said polymerizable monomer composition is a magenta colorant.
- 32. The process according to claim 31, wherein said polymerizable monomer composition contains a negative charge control agent.
- 33. The process according to claim 1, wherein said colorant in said polymerizable monomer composition is a yellow colorant.
- 34. The process according to claim 33, wherein said polymerizable monomer composition contains a negative charge control agent.
- 35. The process according to claim 1, wherein said polyester resin has a ratio of weight average molecular weight Mw.sub.2 to number average molecular weight Mn.sub.2 of said tetrahydrofuran-soluble matter, Mw.sub.2 /Mn.sub.2, of from 1.2 to 3.0.
- 36. The process according to claim 35, wherein said polyester resin has the ratio Mw.sub.2 /Mn.sub.1 of from 1.5 to 3.0.
Priority Claims (1)
Number |
Date |
Country |
Kind |
7-156772 |
May 1995 |
JPX |
|
Parent Case Info
This application is a division of application Ser. No. 08/655,605 filed May 30, 1996, now U.S. Pat. No. 5,679,490.
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Divisions (1)
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Number |
Date |
Country |
Parent |
655605 |
May 1996 |
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