High transparency pigments

• US 9,487,657 B2
• Filed: 08/16/2007
• Issued: 11/08/2016
• Est. Priority Date: 08/18/2006
• Status: Active Grant

• Current Assignee: Pigments Services Incorporated
• Original Assignee: Sun Chemical Corporation
• Inventors: Johnson, Mark W., Schulz, Gregory R.
• Primary Examiner(s): Fink, Brieann R
• Application Number:
  US12/374,515
• Publication Number:
  US 20090326105A1
• Time in Patent Office: 3,372 Days
• Field of Search: 524/88, 524/90
• US Class Current: 1/1
• CPC Class Codes: C09B 67/0002 Grinding; Milling with solid grinding or milling assistants
• CPC Class Codes: C09B 67/0022 Wet grinding of pigments
• CPC Class Codes: C09B 67/0063 of organic pigments with only macromolecular substances
• CPC Class Codes: C09B 67/009 polymeric dispersing agent
• CPC Class Codes: C09D 11/037 characterised by the pigment
• CPC Class Codes: C09D 11/101 Inks specially adapted for printing processes involving curing by wave energy or particle radiation, e.g. with UV-curing following the printing
• CPC Class Codes: C09D 11/322 Pigment inks
• CPC Class Codes: C09D 17/003 containing an organic pigment process features in the making of dye stuff preparations C09B67/00
• CPC Class Codes: C09K 23/16 Amines or polyamines

Abstract

The present invention provides a method for preparing conditioned pigments that have smaller diameter and increased color strength, masstone and travel by milling pigment with a dispersant comprising polyurethane. Further, the invention provides the conditioned pigments prepared by the method of the invention and their applications to paints, coatings, inks, plastics, optical devices, color filters and so forth.

Claims

1. A method for producing a conditioned pigment comprising:

(a) milling a pigment with a dispersant comprising polyurethane having a molecular weight of about 1,000 to about 100,000 to obtain a resulting slurry, wherein at the start of the milling, the milling mixture has a total solids content of about 10 to 50% by weight and the amount of the dispersant is about 1 wt% to 50 wt% based on weight of the pigment; and

(b) isolating a solid product containing the pigment and the dispersant from the resulting slurry, the solid product being the conditioned pigment;

wherein the pigment is a perylene.

2. The method of claim 1 wherein the pigment is present in an amount of about 5 wt. % to about 99 wt. % based on the total amount of the milling mixture.

3. The method of claim 1 wherein the polyurethane has a molecular weight of less than 50,000.

4. The method of claim 1 wherein the polyurethane is present in an amount of at least about 10 to 50 wt. % based on the weight of the pigment.

5. The method of claim 1 wherein the isolating step is by spray-drying, freeze drying, air drying or oven drying.

6. A polyurethane-conditioned pigment according to the method of claim 1.

7. The polyurethane-conditioned pigment according to claim 6, wherein the resulting slurry has a total solids above 20% of the pigment and the dispersant.

8. A method for improving color strength of a pigment comprising effecting the method of claim 1 for a sufficient period of time to realize the improved color strength.

9. A method for improving masstone of a pigment comprising effecting the method of claim 1 for a sufficient period of time to realize the improved masstone.

10. A paint comprising the conditioned pigment of claim 1.

11. A coating comprising the conditioned pigment of claim 1.

12. An ink comprising the conditioned pigment of claim 1.

13. A color filter comprising the conditioned pigment of claim 1.

14. An optical device comprising the conditioned pigment of claim 1.

15. A plastic composition comprising the conditioned pigment of claim 1.

16. The method of claim 3 wherein the pigment is present in an amount of about 10 wt. % to about 40 wt. % based on the total amount of the milling mixture, and the milling is effected such that the resulting slurry has a total solids above 20% of the pigment and the dispersant and the pigment has an average particle size of about 30 nm to 500 nm.

17. The method of claim 16 wherein the pigment is present in an amount of about 15 wt. % to about 30 wt. % based on the total amount of the milling mixture, and the milling is effected such that the resulting slurry has a total solids above 30% of the pigment and the dispersant and the pigment has an average particle size of about 60 nm to 300 nm.

18. The method of claim 17 wherein the milling is effected such that the pigment has an average particle size of about 75 nm to 200 nm.

19. The method of claim 16 wherein the milling is effected in the presence of a rheology additive in an amount of about 0.1 wt % to about 50 wt % based on the weight of the pigment.