Claims
- 1. A process for producing a phthalocyanine crystal comprising a phthalocyanine compound and a substituted or unsubstituted condensed polycyclic hydrocarbon compound, said process comprising subjecting a phthalocyanine compound to an acid pasting step including dissolving or dispersing the phthalocyanine compound in an acid which has been mixed with a substituted or unsubstituted condensed polycyclic hydrocarbon compound, the phthalocyanine compound being gallium phthalocyanine, the gallium phthalocyanine being hydroxgallium phthalocyanine, and having a crystal form characterized by strong peaks at Bragg angles 2θ of 7.4 deg.+0.2 deg. and 28.2 deg.+0.2 deg.
- 2. A process for producing a phthalocyanine crystal comprising a phthalocyanine compound and a substituted or unsubstituted condensed polycyclic hydrocarbon compound, said process comprising subjecting a phthalocyanine compound to an acid pasting step including dissolving or dispersing a phthalocyanine compound in an acid to form a mixture, and adding the mixture into a solution containing a substituted or unsubstituted condensed polycyclic hydrocarbon compound, the phthalocyanine compound being gallium phthalocyanine, the gallium phthalocyanine being hydroxgallium phthalocyanine, and having a crystal form characterized by strong peaks at Bragg angles 2θ of 7.4 deg.+0.2 deg. and 28.2 deg.+0.2 deg.
- 3. A process for producing a phthalocyanine crystal comprising a phthalocyanine compound and a substituted or unsubstituted condensed polycyclic hydrocarbon compound, said process comprising subjecting a crystal transformation step including milling a phthalocyanine compound within a solvent containing a substituted or unsubstituted condensed polycyclic hydrocarbon compound, the phthalocyanine compound being gallium phthalocyanine, the gallium phthalocyanine being hydroxgallium phthalocyanine, and having a crystal form characterized by strong peaks at Bragg angles 2θ of 7.4 deg.+0.2 deg. and 28.2 deg.+0.2 deg.
- 4. The process according to claim 1, wherein the substituted or unsubstituted condensed polycyclic hydrocarbon compound is a halo-substituted condensed polycyclic hydrocarbon compound.
- 5. The process according to claim 4, wherein the halo-substituted condensed polycyclic hydrocarbon compound is α-chloronaphthalene.
- 6. The process according to claim 1, wherein the substituted or unsubstituted condensed polycyclic hydrocarbon compound is naphthalene.
- 7. The process according to claim 2, wherein said substituted or unsubstituted condensed polycyclic hydrocarbon compound is a halo-substituted condensed polycyclic hydrocarbon compound.
- 8. The process according to claim 7, wherein the halo-substituted condensed polycyclic hydrocarbon compound is α-chloronaphthalene.
- 9. The process according to claim 2, wherein the substituted or unsubstituted condensed polycyclic hydrocarbon compound is napthalene.
- 10. The process according to claim 3, wherein the substituted or unsubstituted condensed polycyclic hydrocarbon compound is a halo-substituted condensed polycyclic hydrocarbon compound.
- 11. The process according to claim 10, wherein the halo-substituted condensed polycyclic hydrocarbon compound is α-chloronaphthalene.
- 12. The process according to claim 3, wherein the substituted or unsubstituted condensed polycyclic hydrocarbon compound is naphthalene.
- 13. The process according to claim 1, wherein the acid is concentrated sulfuric acid.
- 14. The process according to claim 1, wherein the acid is used in an amount of 10-40 times the weight of the phthalocyanine compound.
- 15. The process according to claim 1, wherein the phthalocyanine compound is dissolved in the acid at a temperature of at most 50° C.
- 16. The process according to claim 1, wherein said substituted or unsubstituted condensed polycyclic hydrocarbon compound is used in an amount of 0.01-2 times the weight of the phthalocyanine compound.
- 17. The process according to claim 2, wherein said acid is concentrated sulfuric acid.
- 18. The process according to claim 2, wherein the acid is used in a mount of 10-40 times the weight of the phthalocyanine compound.
- 19. The process according to claim 2, wherein the phthalocyanine compound is dissolved in the acid at a temperature of at most 50° C.
- 20. The process according to claim 2, wherein the substituted or unsubstituted condensed polycyclic hydrocarbon compound is used in a amount of 0.01-10 times the weight of the phthalocyanine compound.
- 21. The process according to claim 3, wherein the solvent is N,N-dimethyl formamide.
- 22. The process according to claim 3, wherein the solvent is used in an amount of 10-30 times the weight of the phthalocyanine compound.
- 23. The process according to claim 3, wherein the substituted or unsubstituted condensed polycyclic hydrocarbon compound is used in an amount of 0.01-3 times the weight of the phthalocyanine compound.
Priority Claims (1)
Number |
Date |
Country |
Kind |
2000/022611 |
Jan 2000 |
JP |
|
Parent Case Info
This application is a divisional application of U.S. patent application Ser. No. 09/771,714, filed Jan, 30, 2001, now U.S. Pat. No. 6,447,967.
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