Abstract A process for the production of a beta -form copper phthalocyanine having a particle size of 0.005 to 0.2 mu m and an aspect ratio of 1 to 3, which comprises the following steps: a. dry-milling a crude copper phthalocyanine in a milling apparatus until the resultant dry-milled product has an alpha -crystal content of more than 45% by weight, wet-milling the resultant dry-milled product in the presence of a water-soluble inorganic salt and at least one organic liquid selected from the group consisting of water-soluble alkylene glycols having 2 to 3 carbon atoms and polyoxyalkylene glycols, wherein the inorganic salt is used in an amount that is 2 to 10 times, by weight, as large as that of the dry-milled copper phthalocyanine, and wherein the organic liquid is used in an amount that is 0.1 to 2 times, by weight, as large as that of the dry-milled copper phthalocyanine, and c. removing the inorganic salt and the organic liquid from the resultant wet-milled product.
A process for the production of a β-form copper phthalocyanine having a particle size of 0.005 to 0.2 μm and an aspect ratio of 1 to 3, which comprises the following steps: a. dry-milling a crude copper phthalocyanine in a milling apparatus until the resultant dry-milled produce has an α-crystal content of more than 45% by weight, b. wet-milling the resultant dry-milled product with a kneader in the presence of a water-soluble inorganic salt and at least one organic liquid selected from the group consisting of water-soluble alkylene glycols having 2 to 3 carbon atoms and polyoxyalkylene glycols, wherein the inorganic salt is used in an amount that is 2 to 10 times, by weight, as large as that of the dry-milled copper phthalocyanine, and wherein the organic liquid is used in an amount that is 0.1 to 2 times, by weight, as large as that of the dry-milled copper phthalocyanine at a temperature of 70° to 150° C., and c. removing the inorganic salt and the organic liquid from the resultant wet-milled product.
Claim 2
Dependent Claim
174 words
A process for the production of a β-form copper phthalocyanine having a particle size of 0.005 to 0.2 μm and an aspect ratio of 1 to 3, which comprises the following steps: a. dry-milling a crude copper phthalocyanine in a milling apparatus until the resultant dry-milled produce has an α-crystal content of more than 45% by weight, b. wet-milling the resultant dry-milled product with a kneader in the presence of a water-soluble inorganic salt and at least one organic liquid selected from the group consisting of water-soluble alkylene glycols having 2 to 3 carbon atoms and polyoxyalkylene glycols, wherein the inorganic salt is used in an amount that is 2 to 10 times, by weight, as large as that of the dry-milled copper phthalocyanine, and wherein the organic liquid is used in an amount that is 0.1 to 2 times, by weight, as large as that of the dry-milled copper phthalocyanine at a temperature of 70° to 150° C., and c. removing the inorganic salt and the organic liquid from the resultant wet-milled product.
Claim 3
Dependent Claim
16 words
A process according to claim 1, wherein the crystal content is 50 to 90% by weight.
Claim 4
Dependent Claim
29 words
A process according to claim 1, wherein the crude copper phthalocyanine is dry-milled for 0.5 to 2 hours and the dry-milled product is wet-milled for 1 to 10 hours.
Claim 5
Dependent Claim
17 words
A process according to claim 1, wherein the dry-milled product is wet-milled for 2 to 4 hours.
Claim 6
Dependent Claim
20 words
A process according to claim 1, wherein the β-form copper phthaloycanine has a particle size of 0.01 to 0.1 μm.