EMULSION AGGREGATION POLYESTER TONERS

• US 20080107989A1
• Filed: 11/06/2006
• Published: 05/08/2008
• Est. Priority Date: 11/06/2006
• Status: Active Grant

• Current Assignee: Xerox Corporation (Xerox Holdings Corp.)
• Original Assignee: Xerox Corporation (Xerox Holdings Corp.)
• Inventors: SACRIPANTE, Guerino G., CHEN, Allan K.
• Granted Patent: US 7,858,285 B2
• Time in Patent Office: Days
• US Class Current: 430/109.4
• CPC Class Codes: G03G 9/0804 whereby the components are brought together in a liquid dispersing medium
• CPC Class Codes: G03G 9/08755 Polyesters
• CPC Class Codes: G03G 9/08795 characterised by their chemical properties, e.g. acidity, molecular weight, sensitivity to reactants
• CPC Class Codes: G03G 9/08797 characterised by their physical properties, e.g. viscosity, solubility, melting temperature, softening temperature, glass transition temperature

Abstract

An emulsion aggregation toner including an amorphous resin and a crystalline resin, wherein the toner has an acid value of from about 16 mg/eq. KOH to about 40 mg/eq. KOH and a relative humidity sensitivity ratio of from about 1 to about 2, and wherein the crystalline resin has a melting point of at least about 60° C. The process for forming particles including generating an emulsion of a polyester resin having an acid value of from about 16 mg/eq. KOH to about 40 mg/eq. KOH and generating aggregate particles from the emulsion. Increased charge maintainability and resistivity of the toner result, thereby generating high print quality and high gloss, and provide stable xerographic charging in all ambient environments.

Claims

1. An emulsion aggregation polyester toner comprised of an amorphous resin and a crystalline resin, wherein the toner has an acid value of from about 16 mg/eq. KOH to about 40 mg/eq. KOH, wherein the toner has a melting point of from about 50°

C. to about 130°

C.

2. The toner according to claim 1, wherein the toner is substantially free of surfactant and coagulant.

3. The toner according to claim 1, wherein the crystalline resin is a polyester resin or sulfonated polyester resin.

4. The toner according to claim 3, wherein the polyester resin is a linear polyester resin.

5. The toner according to claim 1, wherein the amorphous resin is a linear amorphous polyester resin.

6. The toner according to claim 1, further comprising at least one colorant.

7. The toner according to claim 1, further comprising at least one wax.

8. The toner according to claim 1, wherein the relative humidity sensitivity ratio of the toner is from about 1 to about 2.

9. A process for forming particles, comprising

generating an emulsion of a polyester resin having an acid value of from about 16 mg/eq. KOH to about 40 mg/eq. KOH;

and

generating aggregate particles from the emulsion.

10. The process according to claim 9, further comprising adding a colorant to the emulsion.

11. The process for forming a toner according to claim 9,

wherein the generating an emulsion comprises dissolving the polyester resin in an organic solvent, neutralizing the acid groups with an alkali base, and dispersing in water followed by heating to remove the organic solvent, thereby resulting in a latex;

wherein the process further comprises optionally adding to the emulsion a colorant dispersion and/or a wax dispersion;

wherein the generating the aggregate particles comprises shearing and adding an aqueous solution of acid until the pH of the mixture is from about 3 to about 5.5;

heating to a temperature of from about 30°

C. to about 60°

C., wherein the aggregate grows to a size of from about 3 to about 20 microns;

raising the pH of the mixture to a range of about 7 to about 9;

heating the mixture to about 60°

C. to about 95°

C.; and

optionally decreasing the pH to a range of about 6 to about 6.8.

12. The process according to claim 9, wherein the generating the emulsion comprises omitting any surfactant in the emulsion, and the generating the aggregate particles comprises omitting addition of coagulants.

13. The process according to claim 9, wherein the polyester resin is amorphous, crystalline, semi-crystalline, or a mixture thereof.

14. The process according to claim 9, wherein the polyester resin is a linear amorphous polyester resin.

15. The process according to claim 9, wherein the polyester resin has an acid value from about 25 to about 40 mg/eq KOH.

16. A process for forming particles, comprising

forming a latex by generating an emulsion of a polyester resin initially having an acid value of from about 16 mg/eq. KOH to 40 mg/eq. KOH;

optionally adding thereto a colorant dispersion, a wax dispersion, and/or a surfactant;

shearing and adding an aqueous solution of acid until the pH of the mixture is from about 3 to about 5.5, followed by optionally adding an aqueous solution of coagulant;

heating to temperature of from about 30°

C. to about 60°

C., wherein the aggregate grows to a size of from about 3 to about 20 microns;

raising the pH of the mixture to a range of 7 to about 9;

heating the mixture to about 60°

C. to about 95°

C.; and

optionally decreasing the pH to a range of about 6.0 to about 6.8.

17. The process according to claim 16, wherein the generating the emulsion comprises omitting any surfactant in the emulsion, and the generating the aggregate particles comprises omitting addition of coagulants.

18. The process according to claim 16, further comprising adding the wax dispersion in the amount of from about 5% to about 25% by weight of the toner before or when generating the aggregate composite.

19. The process according to claim 16, further comprising adding the colorant dispersion in the amount of from about 2% to about 35% by weight of the toner before or when generating the aggregate composite.

20. The process according to claim 16, further comprising adding the surfactant in the amount of from about 0.5% to 5% by weight of the toner when generating the aggregate composite.

21. The process according to claim 16, wherein the acid is nitric acid added in the amount of from about 0.01 to about 1 molar until the pH of the mixture is from about 3 to about 5.5.

22. The process according to claim 16, further comprising adding the coagulant, wherein the coagulant is an aluminum sulfate, a polyaluminum chloride, a cationic surfactant, an alkali halide, an alkali acetate, or a water soluble metal salt with valency of about 2 or more, or combinations thereof.