IP Library Granted Patent US 7,847,073
Granted Patent B2
US 7,847,073 · App. 11/569,263 · Granted Dec 7, 2010

Method for producing a liquid formulation of salts of sulphonic-acid azo dyes

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 7,847,073
App. No.
11/569,263
Granted
Dec 7, 2010
Kind
B2
Abstract

A process for producing a liquid formulation of salts of sulfonated azo dyes by coupling an at least equimolar amount of diazotized aminoarylsulfonic acids I H 2 N—Ar—SO 3 H  (I), where Ar is phenylene (which may be monosubstituted by sulfo) or naphthylene (which may be mono- or disubstituted by sulfo and/or monosubstituted by hydroxyl) onto the coupling product of an unsubstituted or methyl-substituted phenylenediamine with itself comprises dissolving the azo dye in a basic medium and then subjecting the solution to a nanofiltration.

Claims (31)

1. A process for producing a liquid formulation of salts of sulfonated azo dyes, which process comprises:

(a) forming an azo dye by coupling at least an equimolar amount of diazotized aminoarylsulfonic acids of the formula I

H 2 N—Ar—SO 3 H  (I),

wherein Ar is phenylene, which may be monosubstituted by sulfo, or naphthylene, which may be mono- or disubstituted by sulfo and/or monosubstituted by hydroxyl, onto the coupling product of an unsubstituted or methyl-substituted phenylenediamine coupled with itself;

(b) dissolving the azo dye in a basic medium; and then

(c) subjecting the solution to a nanofiltration;

wherein the process for producing the liquid formulation avoids isolation of the dye as a solid and the liquid formulation produced has an inorganic salt content of less than 2% by weight based on 100% pure dye.

2. The process for producing a liquid formulation according to claim 1 wherein the dye is dissolved with aqueous sodium hydroxide solution and a nitrogenous base.

3. The process for producing a liquid formulation according to claim 1 wherein the dye is dissolved with aqueous sodium hydroxide solution and ammoniacal water.

4. The process for producing a liquid formulation according to claim 2 wherein the molar ratio of aqueous sodium hydroxide solution/nitrogenous base is in the range from 1/19 to 19/1.

5. The process for producing a liquid formulation according to claim 1 wherein the dye is dissolved by adjusting the pH of the reaction mixture to a value in the range from 8.5 to 11.

6. The process for producing a liquid formulation according to claim 1 wherein the solution is subjected to nanofiltration employing a nanofiltration membrane having ceramic separating layers.

7. The process for producing a liquid formulation according to claim 1 wherein the dye is dissolved with aqueous sodium hydroxide solution and a nitrogenous base and the pH is kept constant with the nitrogenous base during nanofiltration.

8. The process for producing a liquid formulation according to claim 1 wherein the azo dyes are prepared starting from o-, m- and/or p-aminobenzenesulfonic acid diazo component.

9. The process for producing a liquid formulation according to claim 1 wherein the unsubstituted or methyl-substituted coupling product of a phenylenediamine with itself and diazo component I are used in a stoichiometric ratio in the range from 1:1 to 1:4.

10. A process for producing a liquid formulation of salts of sulfonated azo dyes comprising:

a) preparing a coupling product of an unsubstituted or methyl-substituted phenylenediamine coupled with itself;

b) without intervening isolation of this coupling product, coupling at least an equimolar amount of diazotized aminoarylsulfonic acids of the formula I

H 2 N—Ar—SO 3 H  (I),

wherein Ar is phenylene, which may be monosubstituted by sulfo, or naphthylene, which may be mono- or disubstituted by sulfo and/or monosubstituted by hydroxyl, onto the coupling product obtained according to a), to form a dye;

c) dissolving the dye in a basic medium; and

d) subjecting the solution obtained according to c) to nanofiltration;

wherein the process for producing the liquid formulation avoids isolation of the dye as a solid and the liquid formulation produced has an inorganic salt content of less than 2% by weight based on 100% pure dye.

11. The process for producing a liquid formulation according to claim 1 , wherein the dye is dissolved in the basic medium to produce a solution with a dye content in the range from 3% to 10% by weight.

12. The process for producing a liquid formulation according to claim 10 , wherein the dye is dissolved in the basic medium to produce a solution with a dye content in the range from 3% to 10% by weight.

13. The process for producing a liquid formulation according to claim 1 , wherein the dye is dissolved in the basic medium to produce a solution with a dye content in the range from 3% to 6% by weight.

14. The process for producing a liquid formulation according to claim 10 , wherein the dye is dissolved in the basic medium to produce a solution with a dye content in the range from 3% to 6% by weight.

15. The process for producing a liquid formulation according to claim 1 , wherein the liquid formulation produced has a NaCl content of less than 2% by weight based on 100% pure dye.

16. The process for producing a liquid formulation according to claim 10 , wherein the liquid formulation produced has a NaCl content of less than 2% by weight based on 100% pure dye.

17. The process for producing a liquid formulation according to claim 1 , wherein the solution is subjected to nanofiltration employing a nanofiltration membrane having molecular weight cutoffs of 200 to 2000 daltons, a transmembrane pressure ranging from 1 to 50 bar, and a temperature up to 100° C.

18. The process for producing a liquid formulation according to claim 10 , wherein the solution is subjected to nanofiltration employing a nanofiltration membrane having molecular weight cutoffs of 200 to 2000 daltons, a transmembrane pressure ranging from 1 to 50 bar, and a temperature up to 100° C.

Assignments (7)
RELEASE OF SECURITY INTEREST Recorded Nov 14, 2025
From: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A., AS NOTES COLLATERAL AGENT
To: BIRKO CORPORATION; DIVERSEY, INC.; DIVERSEY TASKI, INC.; INNOVATIVE WATER CARE, LLC; SOLENIS TECHNOLOGIES, L.P.
Reel/Frame 073564/0864 →
SECURITY AGREEMENT (NOTES) Recorded Sep 14, 2022
From: SOLENIS TECHNOLOGIES, L.P.; INNOVATIVE WATER CARE, LLC
To: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A. AS COLLATERAL AGENT
Reel/Frame 061432/0821 →
SECURITY AGREEMENT (ABL) Recorded Sep 14, 2022
From: SOLENIS TECHNOLOGIES, L.P.; INNOVATIVE WATER CARE, LLC
To: BANK OF AMERICA, N.A, AS COLLATERAL AGENT
Reel/Frame 061432/0958 →
SECURITY AGREEMENT (TERM) Recorded Sep 13, 2022
From: SOLENIS TECHNOLOGIES, L.P.; INNOVATIVE WATER CARE, LLC
To: GOLDMAN SACHS BANK USA, AS COLLATERAL AGENT
Reel/Frame 061431/0851 →
SECURITY AGREEMENT (NOTES) Recorded Sep 13, 2022
From: SOLENIS TECHNOLOGIES, L.P.; INNOVATIVE WATER CARE, LLC
To: THE BANK OF NEW YORK MELLON TRUST COMPANY, N.A. AS COLLATERAL AGENT
Reel/Frame 061431/0865 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 9, 2022
From: BASF SE
To: SOLENIS TECHNOLOGIES, L.P.
Reel/Frame 059206/0621 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 10, 2008
From: SCHROEDER, GUNTER-RUDOLF; DECKER, JUERGEN; REICHELT, HELMUT; KLOPP, INGO; DIEFENBACHER, ARMIN; VOSS, HARTWIG
To: BASF AKTIENGESELLSCHAFT
Reel/Frame 021075/0024 →