Production of Toner for Use in Printing Applications

• US 20110159421A1
• Filed: 01/15/2009
• Published: 06/30/2011
• Est. Priority Date: 01/16/2008
• Status: Active Grant

• Current Assignee: Penn Color, Inc.
• Original Assignee: Penn Color, Inc.
• Inventors: Lai, Choung, Rybny, Charles B., Schuck, Ronald W.
• Granted Patent: US 8,247,155 B2
• Time in Patent Office: Days
• US Class Current: 430/105
• CPC Class Codes: G03G 9/0806 whereby chemical synthesis of at least one of the toner components takes place
• CPC Class Codes: G03G 9/09783 Organo-metallic compounds

Abstract

The present invention provides a process for producing a colored toner comprising the steps of: providing a polymer composition comprising at least one polymer wherein the at least one polymer has a softening temperature from about 30° C. to about 160° C.; and a colorant; forming an aqueous mineral suspension of at least one multivalent metal phosphate by contacting a water-soluble salt of the multivalent metal with an aqueous solution comprising: a water-soluble phosphate salt; and at least one crystal growth inhibitor which controls the growth of the at least one multivalent metal phosphate, wherein the pH of the aqueous mineral suspension is from 5.5 to 14; and forming a dispersion of the polymer composition by adding the polymer composition to the aqueous mineral suspension under agitation to form a solid portion comprising dispersed particles of the polymer composition, wherein the temperature of the aqueous mineral suspension during the dispersing step is at least about 70° C.

Claims

1. A process for producing a colored toner comprising the steps of:

providing a polymer composition comprising at least one polymer wherein the at least one polymer has a softening temperature from about 60°

C. to about 160°

C.; and

a colorant;

forming an aqueous mineral suspension of at least one multivalent metal phosphate by contacting a water-soluble salt of the multivalent metal with an aqueous solution comprising;

a water-soluble phosphate salt; and

at least one crystal growth inhibitor selected from the group consisting of;

an organic polycarboxylic acid or a salt there of, a pyrophosphate salt, phosphonic acid or a salt thereof, citric acid, L-Serine, 1,2-dihydroxy-1,2-bis(dihydroxyphosphonyl)ethane, and a Zn²⁺ salt,

to precipitate the at least one multivalent metal phosphate, wherein the pH of the aqueous mineral suspension is from 5.5 to 14;

forming a dispersion of the polymer composition by adding the polymer composition to the aqueous mineral suspension under agitation to form a solid portion comprising dispersed particles of the polymer composition, wherein the temperature of the aqueous mineral suspension during the dispersing step is at least about 70°

C.;

cooling the aqueous mineral suspension comprising the dispersed particles of the polymer composition to a temperature of from about 1°

C. to about 89°

C.;

washing the particles; and

recovering the particles.

2. The process of claim 1 wherein the volume average particle size of the recovered particles is less than 12 μ

m, and particle size distribution is less than 1.4.

3. The process of claim 1 wherein the polymer composition further comprises a wax and a charge control agent.

4. The process of claim 1 wherein the metal is at least one of calcium and magnesium.

5. The process of claim 1 wherein the crystal growth inhibitor includes at least the organic polycarboxylic acid and the organic polycarboxylic acid is selected from the group consisting of:

phthalic acid, isophthalic acid, terephthalic acid, trimelitic acid, citric acid, anhydrides, polyacrylic acid and salts thereof.

6. The process of claim 1 wherein the at least one polymer includes a polyester.

7. The process of claim 1 wherein the at least one polymer includes a styrene-acrylic copolymer.

8. The process of claim 1 wherein the crystal growth inhibitor is the phosphonic acid or a salt thereof and is selected from the group consisting of:

1-hydroxyethylidene phosphonic acid, 1-hydroxyethylidene diphosphonic acid, and a mixture thereof.

9. The process of claim 1 wherein the washing step includes the step of adding an acid to the aqueous mineral suspension comprising the dispersed particles to bring the pH of the aqueous mineral suspension to less than about 2.

10. The process of claim 9 wherein the washing step further includes separating the solid portion from the aqueous solution and rinsing the solid portion with water.

11. The process of claim 9 wherein the acid is selected from the group consisting of HCl, HNO₃, H₂PO₄, and mixtures thereof.

12. The process of claim 11 wherein the acid is HCl.

13. The process of claim 1 wherein the recovering step includes capturing the particles in a filter and drying the particles.

14. The process of claim 1 wherein the volume average particle size is between about 4.0 μ

m and about 9.0 μ

m.

15. The process of claim 1 wherein the aqueous solution during the step of forming an aqueous mineral suspension is at a temperature of from about 30°

C. to about 60°

C.

16. The process of claim 1 wherein the aqueous solution further comprises at least one pH control agent selected from the group consisting of:

acetic acid, propionic acid, butyric acid, phthalic acid, hydrochloric acid, sulfuric acid, phosphoric acid, ethyl amine, triethyl amine, sodium hydroxide, potassium hydroxide, and ammonium hydroxide.

17. The process of claim 1 wherein the polymer composition further comprises at least one polymer selected from the group consisting of:

an epoxy-containing polymer and a polystyrene-acrylate polymer.

18. The process of claim 17 wherein the at least one polymer is the epoxy-containing polymer.

19. The process of claim 17 wherein the at least one polymer is the polystyrene-acrylate polymer.

20. The process of claim 1 wherein the polyester has a weight average molecular weight of from 5,000 g/mol to about 500,000 g/mol.

21. The process of claim 1 wherein the polyester polymer has a gel content greater than 0.1%.

22. The process of claim 1 further comprising the step of heating the at least one multivalent metal phosphate to a temperature of from about 60°

C. to about 100°

C. for from about 5 to about 60 minutes prior to the step of forming a dispersion of the polymer composition.

23. The process of claim 22 wherein the at least one multivalent metal phosphate is heated at a temperature of from about 90°

C. to about 100°

C. for from about 10 to about 20 minutes.

24. The process of claim 23 wherein the at least one multivalent metal phosphate is heated at a temperature of from about 95°

C. to about 100°

C. for about 15 minutes.

25. The toner produced by the process of claim 1.

27. The process of claim 1 wherein the at least one polymer includes a polyurethane.

26. A process for producing a colored toner comprising the steps of:

providing a polymer composition comprising at least one polyester polymer having a softening temperature from about 30°

C. to about 160°

C.; and

a colorant;

forming an aqueous mineral suspension of at least one of a calcium phosphate and a magnesium phosphate by contacting a water soluble salt of at least one of calcium or magnesium with an aqueous solution comprising;

a water soluble phosphate salt; and

at least one crystal growth inhibitor selected from the group consisting of;

an organic polycarboxylic acid or a salt there of, a pyrophosphate salt, phosphonic acid or a salt thereof, citric acid, L-Serine, 1,2-dihydroxy-1,2-bis(dihydroxyphosphonyl)ethane, and a Zn²⁺ salt,

to precipitate the at least one of a calcium phosphate and a magnesium phosphate, wherein the pH of the aqueous mineral suspension is from 7 to 14;

heating the at least one multivalent metal phosphate at a temperature of from about 90°

C. to about 100°

C. for from about 10 to about 20 minutes;

dispersing the polymer composition by adding the polymer composition to the aqueous mineral suspension under agitation to form a solid portion comprising dispersed particles of the polymer composition, wherein the temperature of the aqueous mineral suspension during the dispersing step is at least about 70°

C.;

cooling the aqueous mineral suspension comprising the dispersed particles of the polymer composition to a temperature of from about 1°

C. to about 89°

C.;

washing the particles; and

recovering the particles, wherein the volume average particle size of the particles is less than 12 μ

m, and particle size distribution is less than 1.4.