Toner compositions and processes

• US 5,763,133 A
• Filed: 03/28/1997
• Issued: 06/09/1998
• Est. Priority Date: 03/28/1997
• Status: Expired due to Term

• Current Assignee: Xerox Corporation (Xerox Holdings Corp.)
• Original Assignee: Xerox Corporation (Xerox Holdings Corp.)
• Inventors: Ong, Beng S., Drappel, Stephan V., Sanders, David J., Mychajlowskij, Walter, Patel, Raj D., Kmiecik-Lawrynowicz, Grazyna E.
• Primary Examiner(s): Goodrow, John
• Application Number:
  US08/825,451
• Time in Patent Office: 438 Days
• Field of Search: 430/137, 430/107, 430/110
• US Class Current: 430/137.14
• CPC Class Codes: G03G 9/0804 whereby the components are brought together in a liquid dispersing medium
• CPC Class Codes: G03G 9/08708 Copolymers of styrene
• CPC Class Codes: G03G 9/08711 with esters of acrylic or methacrylic acid
• CPC Class Codes: G03G 9/08728 Polymers of esters
• CPC Class Codes: G03G 9/08731 Polymers of nitriles
• CPC Class Codes: G03G 9/08733 Polymers of unsaturated polycarboxylic acids
• CPC Class Codes: G03G 9/08793 Crosslinked polymers

Abstract

A process for the preparation of toner comprising

(i) blending (a) an aqueous pigment dispersion containing a first ionic surfactant and an optional charge control agent with (b) a latex blend comprised of linear polymer and crosslinked polymer particles, optional nonionic surfactant and a second ionic surfactant with a charge polarity opposite to that of said first ionic surfactant in said pigment dispersion;

(ii) heating the resulting mixture at about below the glass transition temperature (Tg) of the linear latex polymer to form toner sized aggregates; and

(iii) subsequently heating said aggregate suspension about above the Tg of the linear latex polymer to effect fusion or coalescence of said aggregates.

Claims

1. A process for the preparation of toner comprising

(i) blending (a) an aqueous colorant dispersion containing a first ionic surfactant and an optional charge control agent with (b) a latex blend comprised of linear polymer and crosslinked polymer particles, optional nonionic surfactant and a second ionic surfactant with a charge polarity opposite to that of said first ionic surfactant in said pigment dispersion;

(ii) heating the resulting mixture at about below the glass transition temperature (Tg) of the linear latex polymer to form toner sized aggregates; and

(iii) subsequently heating said aggregate suspension about above the Tg of the linear latex polymer to effect fusion or coalescence of said aggregates.

2. A process in accordance with claim 1 wherein the temperature at which the aggregates are formed in (ii) controls the size of said aggregates to be in the range of from about 2 to about 10 microns in volume average diameter, and wherein said coalescence of (iii) provides mechanically stable integral toner particles.

3. A process in accordance with claim 1 wherein the crosslinked polymer is a crosslinked linear polymer.

4. A process in accordance with claim 1 wherein the crosslinked polymer is selected from the group consisting of a crosslinked poly(styrene-alkyl acrylate), poly(styrene-butadiene), poly(styrene-isoprene), poly(styrene-alkyl methacrylate), poly(styrene-alkyl acrylate-acrylic acid), poly(styrene-butadiene-acrylic acid), poly(styrene-isoprene-acrylic acid), poly(styrene-alkyl methacrylate-acrylic acid), poly(alkyl methacrylate-alkyl acrylate), poly(alkyl methacrylate-aryl acrylate), poly(aryl methacrylate-alkyl acrylate), poly(alkyl methacrylate-acrylic acid), poly(styrene-alkyl acrylate-acrylonitrile-acrylic acid), and a crosslinked poly(alkyl acrylate-acrylonitrile-acrylic acid).

5. A process in accordance with claim 1 wherein the crosslinked polymer particles are present in an amount of from about 0.1 to about 70 weight percent, or preferably from about 1 to about 50 weight percent of the toner.

6. A process in accordance with claim 1 wherein the crosslinked polymer particles are present in an amount of from about 20 to about 50 weight percent of the toner.

7. A process in accordance with claim 1 wherein the linear polymer is present in an amount of from about 25 to about 95 weight percent of the toner.

8. A process in accordance with claim 1 wherein the linear polymer is present in an amount of from about 50 to about 90 weight percent of the toner.

9. A process in accordance with claim 1 wherein the resulting toner has an image gloss value of from about 5 to about 60 GGU at the toner'"'"'s minimum fix temperature (MFT), which temperature is from about 120°

to about 185°

C.

10. A process in accordance with claim 1 wherein the toner possesses an image gloss value of from about 10 to about 70 GGU at the toner MFT of from about 120°

to about 185°

C., and which gloss value is enabled by the presence of from about 0.1 to about 70 weight percent of crosslinked polymer particles in the toner.

11. A process in accordance with claim 1 wherein the surfactant in the aqueous colorant dispersion is a cationic surfactant, and the surfactant in the latex blend is nonionic and anionic surfactants.

12. A process in accordance with claim 1 wherein the surfactant in the colorant dispersion is an anionic surfactant and the surfactant in the latex blend is nonionic and cationic surfactants.

13. A process in accordance with claim 1 wherein the aqueous colorant dispersion is prepared by homogenizing a colorant in water in the presence of a suitable surfactant, which homogenizing is at from about 1,000 revolutions per minute to about 10,000 revolutions per minute, at a temperature of from about 25°

C. to about 55°

C., and for a duration of from about 1 minute to about 120 minutes.

14. A process in accordance with claim 1 wherein the colorant dispersion is prepared by mixing a colorant in a suitable surfactant in water using an ultrasonic probe at from about 300 watts to about 900 watts of energy, at from about 5 to about 50 megahertz of amplitude, at a temperature of from about 25°

C. to about 55°

C., and for a duration of from about 1 minute to about 120 minutes.

15. A process in accordance with claim 1 wherein the aggregation step (ii) is accomplished at temperatures of from about 25°

C. to about 1°

C. below the Tg of the linear polymer for a duration of from about 0.5 hour to about 6 hours.

16. A process in accordance with claim 1 wherein the linear polymer is selected from the group consisting of poly(styrene-butadiene), poly(methyl methacrylate-butadiene), poly(ethyl methacrylate-butadiene), poly(propyl methacrylate-butadiene), poly(butyl methacrylate-butadiene), poly(methyl acrylate-butadiene), poly(ethyl acrylate-butadiene), poly(propyl acrylate-butadiene), poly(butyl acrylate-butadiene), poly(styrene-isoprene), poly(methylstyrene-isoprene), poly(methyl methacrylate-isoprene), poly(ethyl methacrylate-isoprene), poly(propyl methacrylate-isoprene), poly(butyl methacrylate-isoprene), poly(methyl acrylate-isoprene), poly(ethyl acrylate-isoprene), poly(propyl acrylate-isoprene), poly(butyl acrylate-isoprene), poly(styrene-butylacrylate), poly(styrene-butadiene), poly(styrene-isoprene), poly(styrene-butyl methacrylate), poly(styrene-butyl acrylate-acrylic acid), poly(styrene-butadiene-acrylic acid), poly(styrene-isoprene-acrylic acid), poly(styrene-butyl methacrylate-acrylic acid), poly(butyl methacrylate-butyl acrylate), poly(butyl methacrylate-acrylic acid), poly(styrene-butyl acrylate-acrylonitrile-acrylic acid), poly(acrylonitrile-butyl acrylate-acrylic acid), and the crosslinked polymer is comprised of said linear polymer with crosslinking.

17. A process in accordance with claim 1 wherein the linear polymer is poly(styrene-butylacrylate), poly(styrene-butyl acrylate-acrylic acid), poly(styrene-butadiene), poly(styrene-butadiene-acrylic acid), poly(styrene-butyl acrylate-acrylonitrile), or poly(styrene-butyl acrylate-acrylonitrile-acrylic acid), and the crosslinked resin is the crosslinked derivative of poly(styrene-butyl acrylate), poly(styrene-butyl acrylate-acrylic acid), poly(styrene-butadiene), poly(styrene-butadiene-acrylic acid), poly(styrene-butyl acrylate-acrylonitrile), or poly(styrene-butyl acrylate-acrylonitrile-acrylic acid).

18. A process in accordance with claim 2 wherein the linear polymer is selected from the group consisting of poly(styrene-butadiene), poly(methyl methacrylate-butadiene), poly(ethyl methacrylate-butadiene), poly(propyl methacrylate-butadiene), poly(butyl methacrylate-butadiene), poly(methyl acrylate-butadiene), poly(ethyl acrylate-butadiene), poly(propyl acrylate-butadiene), poly(butyl acrylate-butadiene), poly(styrene-isoprene), poly(methylstyrene-isoprene), poly(methyl methacrylate-isoprene), poly(ethyl methacrylate-isoprene), poly(propyl methacrylate-isoprene), poly(butyl methacrylate-isoprene), poly(methyl acrylate-isoprene), poly(ethyl acrylate-isoprene), poly(propyl acrylate-isoprene), poly(butyl acrylate-isoprene), poly(styrene-butylacrylate), poly(styrene-butadiene), poly(styrene-isoprene), poly(styrene-butyl methacrylate), poly(styrene-butyl acrylate-acrylic acid), poly(styrene-butadiene-acrylic acid), poly(styrene-isoprene-acrylic acid), poly(styrene-butyl methacrylate-acrylic acid), poly(butyl methacrylate-butyl acrylate), poly(butyl methacrylate-acrylic acid), poly(styrene-butyl acrylate-acrylonitrile-acrylic acid), poly(acrylonitrile-butyl acrylate-acrylic acid), and wherein the crosslinked polymer is contained in said linear polymer.

19. A process in accordance with claim 1 wherein the nonionic surfactant is selected from the group consisting of polyvinyl alcohol, methalose, methyl cellulose, ethyl cellulose, propyl cellulose, hydroxy ethyl cellulose, carboxy methyl cellulose, polyoxyethylene cetyl ether, polyoxyethylene lauryl ether, polyoxyethylene octyl ether, polyoxyethylene octylphenyl ether, polyoxyethylene oleyl ether, polyoxyethylene sorbitan monolaurate, polyoxyethylene stearyl ether, polyoxyethylene nonylphenyl ether, and dialkylphenoxy poly(ethyleneoxy)ethanol.

20. A process in accordance with claim 1 wherein the anionic surfactant is selected from the group consisting of sodium dodecyl sulfate, sodium dodecylbenzene sulfate, sodium dodecylnaphthalene sulfate, and the cationic surfactant is a quaternary ammonium salt.

21. A process in accordance with claim 1 wherein the colorant is carbon black, magnetite, cyan, yellow, magenta colorant, and mixtures thereof.

22. A process in accordance with claim 1 wherein the surfactants are each present in an effective amount of from about 0.1 to about 5 weight percent of the reaction mixture.

23. A process in accordance with claim 1 wherein there is added to the surface of the formed toner metal salts, metal salts of fatty acids, silicas, metal oxides, or mixtures thereof, in an effective amount of from about 0.1 to about 10 weight percent of the obtained toner particles.

24. A process in accordance with claim 1 wherein the toner is washed with water or aqueous base at a temperature of from about 25°

to about 75°

C. primarily to remove the residual surfactants from the toner.

25. A process in accordance with claim 1 wherein the fusion or coalescence (iii) is accomplished at a temperature from about 10 to about 50°

C. above the Tg of the linear noncrosslinked resin, and wherein the heating in the coalescence (iii) is accomplished at a temperature of about 80°

to about 100°

C.

27. A toner obtained by the process of claim 1.

29. A process in accordance with claim 1, wherein subsequent to (iii) the aggregate suspension is cooled, the toner recovered, and thereafter washed and dried.

26. A process for the preparation of toner comprising heating (a) a mixture of an aqueous colorant dispersion containing a first ionic surfactant, and (b) a latex blend comprised of linear noncrosslinked polymer and crosslinked polymer particles, a non-ionic surfactant and a second ionic surfactant with a charge polarity opposite to that of said first ionic surfactant in said pigment dispersion;

heating the resulting mixture below the glass transition temperature (Tg) of the linear noncrosslinked polymer to form toner aggregates; and

subsequently heating said aggregates above the Tg of the linear latex polymer to effect coalescence of said aggregates.

28. A toner obtained by the process of claim 26.

30. A process in accordance with claim 26, wherein the toner is cooled, recovered, and thereafter washed and dried.

31. A process for the preparation of toner consisting essentially

(i) blending (a) an aqueous colorant dispersion containing a first ionic surfactant and an optional charge control agent with (b) a latex blend comprised of linear polymer and crosslinked polymer particles, optional nonionic surfactant and a second ionic surfactant with a charge polarity opposite to that of said first ionic surfactant in said pigment dispersion;

(ii) heating the resulting mixture at about below the glass transition temperature (Tg) of the linear latex polymer to form toner sized aggregates;

(iii) subsequently heating said aggregate suspension about above the Tg of the linear latex polymer to effect fusion or coalescence of said aggregates; and

(iv) cooling and isolating the toner product.