Claims
- 1. A process for the preparation of hydroxygallium phthalocyanines consisting essentially of hydrolyzing a gallium phthalocyanine precursor pigment by dissolving said precursor hydroxygallium phthalocyanine in a concentrated acid and then reprecipitating the resulting dissolved pigment in basic aqueous media; optionally removing any ionic species formed by washing with water; concentrating the resulting aqueous slurry comprised of water and hydroxygallium phthalocyanine to a wet cake; removing water from said slurry by azeotropic distillation with an organic solvent, and subjecting said resulting pigment slurry to mixing with the addition of a second solvent to cause the formation of said hydroxygallium phthalocyanine; and wherein the sulfur content in said pigment slurry is reduced from about 3,000 to about 5,000 parts per million to from about 50 to about 100 parts per million by solvent washing of the pigment slurry by dispersing in an organic solvent of N,N-dimethylformamide, acetone, N,N-dimethylpyrrolidone, tetrahydrofuran, methanol, or isopropanol; adding to the resulting dispersion concentrated ammonium hydroxide solution and stirring for from about 2 to about 16 hours; followed by further washing with deionized water until the conductivity of the filtrate decreases to below about 20 mS/cm.sup.2.
- 2. A process in accordance with claim 1 wherein said gallium phthalocyanine precursor pigment is a halogallium phthalocyanine.
- 3. A process in accordance with claim 2 wherein said halogallium phthalocyanine is chlorogallium phthalocyanine, and said concentrated acid is sulfuric acid.
- 4. A process in accordance with claim 1 wherein the gallium phthalocyanine precursor pigment is an alkoxy-bridged gallium phthalocyanine.
- 5. A process in accordance with claim 1 wherein the gallium phthalocyanine precursor pigment is prepared by the reaction of o-phthalodinitrile or 1,3-diiminoisoindolene with a nonhalogenated gallium compound in a suitable solvent.
- 6. A process in accordance with claim 5 wherein the nonhalogenated gallium compound is gallium alkoxide, gallium acetylacetonate, or gallium acetate.
- 7. A process in accordance with claim 1 wherein Type V hydroxygallium phthalocyanine is formed.
- 8. A process in accordance with claim 1 wherein the aqueous pigment slurry is concentrated by filtration.
- 9. A process in accordance with claim 1 wherein the azeotropic water removal is accomplished with a hydrophobic organic solvent.
- 10. A process in accordance with claim 9 wherein the hydrophobic organic solvent is the hydrocarbon hexane, heptane, cyclohexane, or cyclopentane, or the esters of propylacetate, butylacetate or a ketone.
- 11. A process in accordance with claim 1 wherein a nonmilling mixing with the addition of a second solvent is performed to induce the formation of hydroxygallium phthalocyanine Type V.
- 12. A process in accordance with claim 11 wherein said second solvent is an aprotic polar solvent of N,N-dimethylformamide (DMF), N',N'-dimethylsulfoxide, pyridine or N',N'-dimethylpyrrolidinone.
- 13. A process in accordance with claim 12 wherein hydroxygallium phthalocyanine Type V results.
- 14. A process in accordance with claim 1 wherein the azeotropic water removal is accomplished by dispersing the wet cake comprised of Type I hydroxygallium phthalocyanine formed in a hydrophobic organic solvent followed by heating to reflux; removing any water formed; refluxing until the boiling point of the reaction mixture reaches that of the hydrophobic organic solvent; cooling and filtering the dispersion formed; dispersing the resulting precipitate in N,N-dimethylformamide and stirring for from about 16 to about 48 hours whereby conversion to Type V hydroxygallium phthalocyanine results.
- 15. A process in accordance with claim 14 wherein the water content is less than about 0.2 percent by weight.
- 16. A process in accordance with claim 1 wherein the washing results in the removal of from about 500 to about 3,000 parts per million of the impurity sulfur, which sulfur orginates from the acid selected, and there is formed Type V hydroxygallium phthalocyanine.
- 17. A process in accordance with claim 1 wherein the washing enables the amount of sulfur in the hydroxygallium phthalocyanine polymorph to be reduced to from about 3,000 to about 100 parts per million.
- 18. A process in accordance with claim 1 wherein the washing mixture is comprised of from about 1 part to about 10 parts of N,N-dimethylformamide, acetone, N,N-dimethlypyrrolidone, tetrahydrofuran or methanol, or isopropanol and 1 part of concentrated ammonium hydroxide solution.
- 19. A process for the preparation of Type V hydroxygallium phthalocyanine which comprises formation of a precursor gallium phthalocyanine prepared by heating 1 part gallium acetylacetonate with from about 1 part to about 10 parts in a solvent, present in an amount of from about 10 parts to about 100 parts per part of gallium acetylacetonate that is present; hydrolyzing said precursor by dissolving in a concentrated acid; and then reprecipitating the dissolved pigment in aqueous ammonia, thereby forming Type I hydroxygallium phthalocyanine; and admixing said Type I hydroxygallium phthalocyanine with an organic solvent.
- 20. A process in accordance with claim 5 wherein the o-phthalodinitrile, or 1,3-diiminoisoindolene and a nonhalogenated gallium compound of gallium alkoxide, gallium acetylacetonate, or gallium acetate is heated for a period of from about 1 minute to about 24 hours, and preferably about 4 hours.
- 21. A process in accordance with claim 5 wherein the solvent is comprised of quinoline, 1-chloronaphthalene, N-methylpyrrolidone or mixtures thereof.
- 22. A process in accordance with claim 2 wherein the washing of the precursor gallium phthalocyanine is accomplished with dimethylformamide at a temperature of from about 70.degree. C. to about 150.degree. C.
- 23. A process in accordance with claim 1 wherein the acid is sulfuric acid, methanesulfonic acid, or trifluoroacetic acid.
- 24. A process in accordance with claim 1 wherein the Type V hydroxygallium phthalocyanine obtained has major peaks, as measured with an X-ray diffractometer, at 7.4, 9.8, 12.4, 16.2, 17.6, 18.4, 21.9, 23.9, 25.0, 28.1, and the highest peak at 7.4 degrees 2.THETA..
- 25. A process in accordance with claim 1 wherein reaction with said acid is accomplished at a temperature ranging from about 0.degree. C. to about 50.degree. C., followed by stirring for about 5 minutes to about 10 hours, followed by pouring the hydrolyzed hyrdoxygallium phthalocyanine mixture onto ice or into ice cold water with continuous stirring, filtering, and subsequently washing with deionized water.
- 26. A process in accordance with claim 1 wherein the hydroxygallium phthalocyanine Type V obtained is free of residual chlorine.
- 27. A process in accordance with claim 1 wherein the hydroxygallium Type V obtained is of small particle size of from about 0.01 .mu.m to about 0.5 .mu.m in average volume diameter.
- 28. A process in accordance with claim 1 wherein said filtration provides Type V hydroxygallium phthalocyanine with a sulfur content of from about 50 to about 200 parts per million.
- 29. A process in accordance with claim 18 wherein about 4 parts of 1,3-diiminoisoindolene are selected, and about 19 parts of said solvent are selected.
- 30. A process in accordance with claim 19 wherein the Type V hydroxygallium phthalocyanine obtained subsequent to admixing said Type I hydroxygallium phthalocyanine with an organic solvent possesses a reduced sulfur content of from about 3,000 to about 5,000 parts per million to from about 50 to about 100 parts per million by effecting a solvent washing of the hydroxygallium Type V phthalocyanine, which washing is accomplished by dispersing said phthalocyanine in an organic solvent of N,N-dimethylformamide, acetone, N,N-dimethylpyrrolidone, tetrahydrofuran, methanol, or isopropanol; adding to the resulting dispersion concentrated ammonium hydroxide solution and stirring for from about 2 to about 16 hours; followed by further washing with deionized water until the conductivity of the filtrate decreases to below about 20 mS/cm.sup.2.
- 31. A process for the preparation of hydroxygallium phthalocyanines consisting of hydrolyzing a gallium phthalocyanine precursor pigment by dissolving said precursor hydroxygallium phthalocyanine in a concentrated acid and then reprecipitating the resulting dissolved pigment in basic aqueous media; concentrating the resulting aqueous slurry comprised of water and hydroxygallium phthalocyanine to a wet cake; removing water from said slurry by azeotropic distillation with an organic solvent; and subjecting said resulting pigment slurry to mixing with the addition of a second solvent to cause the formation of said hydroxygallium phthalocyanine; and wherein the sulfur content in said pigment slurry is reduced from about 3,000 to about 5,000 parts per million to from about 50 to about 100 parts per million by solvent washing of the pigment slurry containing Type V hydroxygallium phthalocyanine by dispersing in an organic solvent of N,N-dimethylformamide, acetone, N,N-dimethylpyrrolidone, tetrahydrofuran, methanol, or isopropanol; adding to the resulting dispersion concentrated ammonium hydroxide solution and stirring for from about 2 to about 16 hours; followed by further washing with deionized water until the conductivity of the filtrate decreases to below about 20 mS/cm.sup.2.
Parent Case Info
This is a division of application Ser. No. 332,304, filed Oct. 31, 1994, now U.S. Pat. No. 5,482,811.
US Referenced Citations (2)
Number |
Name |
Date |
Kind |
5350844 |
Martin et al. |
Sep 1994 |
|
5360475 |
Nukada et al. |
Nov 1994 |
|
Foreign Referenced Citations (1)
Number |
Date |
Country |
6-73299 |
Mar 1994 |
JPX |
Divisions (1)
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Number |
Date |
Country |
Parent |
332304 |
Oct 1994 |
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