US4522654A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Continuous method of producing phthalocyanine pigment dispersions in organic solvent
Assignee: BASF Corp
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Filing: 1983-12-23
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Granted: 1985-06-11
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Expires: 2003-12-23
Abstract
Abstract A continuous method for producing a dispersion of phthalocyanine blue pigment in an organic solvent is disclosed. The method involves the following two steps: (A) mixing a phthalocyanine crude pigment at about 10 to 50% by weight with from about 5 to 20% by weight of surfactant in a binder containing an organic solvent, and (B) continuously pumping the blend of (A) through at least two shot mills in series in which the shot grinding media range in size from 0.1 to 2.5 mm. diameter and grinding the blend until the particle size of the crude is reduced to where the solvent dispersion has suitable pigment tinctorial strength for use in inks and coatings. The dispersion of blue pigment produced by this method is especially useful in paste inks and organic solvent-based coatings.
Inventors
- 👤 Dominick Chisvette
- 👤 James Lattimore
- 👤 Stanley G. Sova
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 04:02
CPC Classifications
C; C09; C09B; C09B67/00; C09B67/0001; C09B67/0022; C09B67/0023; C09B67/0032
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
153 words
The method of converting a phthalocyanine crude wherein at least 80% of the crude particles have a size greater than 1 micrometer to a dispersed form which is useful in inks and coatings, said method comprising (A) premixing phthalo crude at about 10 to 50% by weight with from about 5 to 20% by weight of surfactant based on pigment in a binder containing an organic solvent, said premixing being accomplished by agitation to break down loose crude agglomerates and obtain a uniform blend of the crude without appreciably reducing the particle size of the crude, and (B) continuously pumping the blend of (A) through at least one but preferably two shot mills containing between 50 and 90% by volume of a grinding media that has a size of from about 0.1 to 2.5 mm. diameter and then grinding at such rate that the particle size has been reduced to pigment particle size.
Claim 2
Independent Claim
153 words
The method of converting a phthalocyanine crude wherein at least 80% of the crude particles have a size greater than 1 micrometer to a dispersed form which is useful in inks and coatings, said method comprising (A) premixing phthalo crude at about 10 to 50% by weight with from about 5 to 20% by weight of surfactant based on pigment in a binder containing an organic solvent, said premixing being accomplished by agitation to break down loose crude agglomerates and obtain a uniform blend of the crude without appreciably reducing the particle size of the crude, and (B) continuously pumping the blend of (A) through at least one but preferably two shot mills containing between 50 and 90% by volume of a grinding media that has a size of from about 0.1 to 2.5 mm. diameter and then grinding at such rate that the particle size has been reduced to pigment particle size.
Claim 3
Dependent Claim
24 words
The method of claim 1 in which the grinding in the shot mill is carried out at a temperature of 5 to 80° C.
Claim 4
Dependent Claim
14 words
The method of claim 1 in which the surfactant is a solvent-soluble non-ionic surfactant.
Claim 5
Dependent Claim
16 words
The method of claim 3 in which the solvent-soluble non-ionic surfactant is an ethylene oxide adduct.
Claim 6
Dependent Claim
14 words
The method of claim 1 in which the surfactant is a solvent-soluble cationic surfactant.
Claim 7
Dependent Claim
12 words
The method of claim 1 in which the surfactant is solid surfactant.
Claim 8
Dependent Claim
21 words
The method of claim 1 wherein the crude phthalocyanine pigment is selected from copper, cobalt, zinc, nickel, cadmium and metal-free phthalocyanine.
Claim 9
Independent Claim
138 words
The method of converting a crude copper phthalocyanine pigment wherein at least 80% of the crude has a size greater than 1 micrometer to a dispersed form which is useful in inks and coatings, said method comprising (A) premixing crude pigment, with 5 to 20% by weight of surfactant in a binder containing an organic solvent, said premixing being accomplished by agitation to break down loose pigment agglomerates and obtain a uniform blend of the ingredients without appreciably reducing the particle size of the pigment, and (B) continuously pumping the blend of (A) through at least two shot mills containing between 50 and 90% by volume of a grinding media that has a size in the range of 0.1 to 2.5 mm. diameter, and then grinding until the dispersion has suitabletinctorial strength for use in inks and coatings.
Claim 10
Independent Claim
138 words
The method of converting a crude copper phthalocyanine pigment wherein at least 80% of the crude has a size greater than 1 micrometer to a dispersed form which is useful in inks and coatings, said method comprising (A) premixing crude pigment, with 5 to 20% by weight of surfactant in a binder containing an organic solvent, said premixing being accomplished by agitation to break down loose pigment agglomerates and obtain a uniform blend of the ingredients without appreciably reducing the particle size of the pigment, and (B) continuously pumping the blend of (A) through at least two shot mills containing between 50 and 90% by volume of a grinding media that has a size in the range of 0.1 to 2.5 mm. diameter, and then grinding until the dispersion has suitabletinctorial strength for use in inks and coatings.
Claim 11
Dependent Claim
32 words
A dispersion for solvent based ink comprising copper phthalocyanine blue pigment dispersed in a solution of binder resin. and organic solvent wherein the pigment is dispersed by the method of claim 8.
Claim 12
Dependent Claim
31 words
A dispersion for paste ink comprising copper phthalocyanine blue pigment dispersed in a solution of binder resin and organic solvent wherein the pigment is dispersed by the method of claim 8.
References Cited (Backward Citations)
US3775149A
Cited
US4227810A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1988-06-10 | 1988-12-10 | 1989-06-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-06-10 | 1992-12-10 | 1993-06-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-06-10 | 1996-12-10 | 1997-06-11 | $7700.00 | Window Closed / Lapsed |