Process for the preparation of aqueous polyurethane dispersions and solutions

• US 4,269,748 A
• Filed: 03/02/1979
• Issued: 05/26/1981
• Est. Priority Date: 03/15/1978
• Status: Expired due to Term

• Current Assignee: Bayer AG
• Original Assignee: Bayer AG
• Inventors: Nachtkamp, Klaus, Pedain, Josef, Grammel, Jurgen
• Primary Examiner(s): Pertilla, Theodore E.
• Application Number:
  US06/017,017
• Time in Patent Office: 816 Days
• Field of Search: 260/29.2 TN, 260/566 B, 528/46, 528/61
• US Class Current: 524/839
• CPC Class Codes: C08G 18/0804 Manufacture of polymers containing ionic or ionogenic groups
• CPC Class Codes: C08G 18/10 Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
• CPC Class Codes: C08G 18/283 Compounds containing ether groups, e.g. oxyalkylated monohydroxy compounds
• CPC Class Codes: C08G 18/3256 Reaction products of polyamines with aldehydes or ketones
• CPC Class Codes: Y10T 428/31551 Of polyamidoester [polyurethane, polyisocyanate, polycarbamate, etc.]

Abstract

The present invention relates to a process for the preparation of aqueous solutions or dispersions of polyurethanes, in which process prepolymers which have at least two free isocyanate groups and contain chemically-fixed hydrophilic groups and/or external emulsifiers which are not chemically fixed are reacted with chain lengthening agents in the aqueous phase, characterized in that the isocyanate prepolymer which is hydrophilically modified and/or contains an external emulsifier is mixed with chain lengthening agents selected from the group consisting of azines and hydrazones in the absence of water and the mixture obtained is then mixed with water. The present invention also relates to the dispersions or solutions which can be obtained by this process. Lastly, this invention relates to the use of the dispersions or solutions which can be obtained by this process for coating flexible substrates.

Claims

1. A process for the preparation of aqueous solutions or dispersions of polyurethanes prepared by the reaction of prepolymers which have at least two free isocyanate groups and contain either chemically fixed hydrophilic groups and/or external emulsifiers which are not chemically fixed, with chain lengthening agents in the aqueous phase, characterized in that the isocyanate prepolymer which is hydrophilically modified and/or contains an external emulsifier is mixed with azine chain lengthening agents in the absence of water, and the resulting mixture is then mixed with water before significant increases in viscosity occur.

2. The process according to claim 1, characterized in that the nature and proportions of the reactants are chosen to provide from about 0.25 to 1.5 isocyanate-reactive, at least partially blocked hydrazinic-NH₂ groups of the chain lengthening agent for each isocyanate group of the isocyanate group-containing prepolymer.

3. Dispersions or solutions obtainable according to claim 1.

4. Coatings prepared by a process which comprises applying the solutions or dispersions of claim 1 to a substrate.

5. Films prepared from the solutions or dispersions of claim 1.

6. Lacquers prepared from the solutions or dispersions of claim 1.

7. A process for the preparation of aqueous solutions or dispersions comprising

(A) mixing in the absence of water

(i) a hydrophilic isocyanate prepolymer having

(a) an average isocyanate functionality of from about 1.8 to 2.2;

(b) its hydrophilic properties contributed by dispersing centers selected from the group consisting of chemically incorporated cationic or anionic groups present in from about 0 to 100 milliequivalents per 100 g of isocyanate prepolymer, chemically incorporated ethylene oxide units present in the isocyanate prepolymer in from about 0 to 30% by weight, based on the weight of the isocyanate prepolymer, and external emulsifiers present in about 0 to 30% by weight, based on the weight of the isocyanate prepolymer; and

(c) an average molecular weight of from about 500 to 10,000

(ii) with an azine chain lengthening agent which forms hydrazine under the hydrolytic influence of water to form a mixture and

(B) mixing the mixture of (A), before significant increases in viscosity occur, with water to release the hydrazine and chain lengthen the prepolymer.

8. The process of claim 7 wherein the hydrophilic isocyanate prepolymer has

(a) an average isocyanate functionality of about 2,

(b) its hydrophilic properties contributed by dispersing centers selected from the group consisting of chemically incorporated cationic or anionic groups present in from about 0.1 to 100 milliequivalents per 100 g of isocyanate prepolymer, chemically incorporated ethylene oxide units present in the isocyanate prepolymer in from about 0.5 to 30% by weight, based on the weight of the isocyanate prepolymer, and external emulsifiers present in from about 1 to 30% by weight, based on the weight of the isocyanate prepolymer, and

(c) an average molecular weight of from about 800 to 4000.

9. The process of claim 7 wherein the azines have the formula ##STR2## wherein R¹, R², R³ and R⁴, which may be the same or different, represent hydrogen, aliphatic hydrocarbon groups having from 1 to 17 carbon atoms, or R¹ and R² and/or R³ and R⁴, together with the >

C═

carbon atom, may form a cycloaliphatic ring having from 5 to 18 carbon atoms.

10. The process of claim 7 wherein the equivalent ratio of isocyanate groups of hydrophilic isocyanate prepolymer (i) to free and blocked hydrazinic-NH₂ -groups of chain lengthening agent (ii) is from about 4:

1 to 1;

1.5.

11. The process of claim 7 wherein hydrophilic isocyanate prepolymer (i) is mixed with chain lengthening agent (ii) at a temperature of from about -20°

to 100°

C.

12. The process of claim 11 wherein hydrophilic isocyanate prepolymer (i) is mixed with chain lengthening agent (ii) in the presence of up to about 30% by weight of an organic solvent, based on the weight of the hydrophilic isocyanate prepolymer.

13. The process of claim 7 wherein the mixture of hydrophilic isocyanate prepolymer (i) and chain lengthening agent (ii) is mixed with a sufficient quantity of water to produce a solution or dispersion having a solids content of from about 40 to 60% by weight.

14. The process of claim 13 wherein the water is at a temperature of from about 0°

to 90°

C.

15. The aqueous polyurethane solutions or dispersions produced by the process of claim 7.

16. A process for the preparation of aqueous solutions or dispersions of polyurethanes prepared by the reaction of prepolymers which have at least two free isocyanate groups and contain either chemically fixed hydrophilic groups and/or external emulsifiers which are not chemically fixed, with chain lengthening agents in the aqueous phase, characterized in that the isocyanate prepolymer which is hydrophilically modified and/or contains an external emulsifier is mixed with hydrazone chain lengthening agents in the absence of water, and the resulting mixture is then mixed with water, before significant increases in viscosity occur.

17. A process for the preparation of aqueous solutions or dispersions comprising:

(A) mixing in the absence of water

(i) a hydrophilic isocyanate prepolymer having

(a) an average isocyanate functionality of from about 1.8 to 2.2;

(b) its hydrophilic properties contributed by dispersing centers selected from the group consisting of chemically incorporated cationic or anionic groups present in from about 0 to 100 milliequivalents per 100 g of isocyanate prepolymer, chemically incorporated ethylene oxide units present in the isocyanate prepolymer in from about 0 to 30% by weight, based on the weight of the isocyanate prepolymer, and external emulsifiers present in about 0 to 30% by weight, based on the weight of the isocyanate prepolymers; and

(c) an average molecular weight of from about 500 to 10,000

(ii) with an at least partially blocked hydrazone chain lengthening agent which forms hydrazine under the hydrophilic influence of water to form a mixture, and

(B) mixing the mixture of (A), before significant increases in viscosity occur, with water to release the hydrazine and chain lengthen the prepolymer.

18. The process of claim 7 or 17 wherein the hydrophilic properties of the prepolymer are contributed by dispersing centers selected from the group consisting of chemically incorporated cationic or anionic groups present in from about 0.1 to 100 milliequivalents per 100 g of isocyanate prepolymer and chemically incorporated ethylene oxide units present in the isocyanate prepolymer in from about 0.5 to 30% by weight, based on the weight of the isocyanate prepolymer.