Reactive polyurethane coatings

Claim 2

A process for the production of microporous coatings comprising: (a) mixing an NCO-prepolymer prepared from polyisocyanates with compounds containing at least two isocyanate-reactive hydrogen atoms with about 3 to 40% by weight, based on the NCO-prepolymer, of a substantially inert, with respect to isocyanate groups, viscosity-reducing, non-migrating liquid organic compound miscible with said NCO-prepolymer as a plasticizer, wherein (i) said NCO-prepolymer is used free from solvents, has a viscosity of more than about 500 cP at 25° C. and a molecular weight of from about 300 to 20,000, (ii) said plasticizer has a volatility of less than 10% weight loss after storage for 72 hours at 90° C., and (iii) the resultant NCO-prepolymer-plasticizer mixture has a viscosity of less than about 15,000 cP at 20° C., (b) dispersing 3 to 300% by weight of water, based on the NCO-prepolymer, into the NCO-prepolymer-plasticizer mixture to form a water-in-oil emulsion, (c) adding a polyamine to the water-in-oil emulsion in a quantity substantially equivalent to the isocyanate groups. (d) applying a coating of the water-in-oil emulsion to a substrate and (e) hardening the coating by evaporating the chemically unbound water from said coating.

Claim 3

A process for the production of microporous coatings comprising: (a) mixing an NCO-prepolymer prepared from polyisocyanates with compounds containing at least two isocyanate-reactive hydrogen atoms with about 3 to 40% by weight, based on the NCO-prepolymer, of a substantially inert, with respect to isocyanate groups, viscosity-reducing, non-migrating liquid organic compound miscible with said NCO-prepolymer as a plasticizer, wherein (i) said NCO-prepolymer is used free from solvents, has a viscosity of more than about 500 cP at 25° C. and a molecular weight of from about 300 to 20,000, (ii) said plasticizer has a volatility of less than 10% weight loss after storage for 72 hours at 90° C., and (iii) the resultant NCO-prepolymer-plasticizer mixture has a viscosity of less than about 15,000 cP at 20° C., (b) dispersing 3 to 300% by weight of water, based on the NCO-prepolymer into the NCO-prepolymer-plasticizer mixture to form a water-in-oil emulsion, (c) adding a polyamine to the water-in-oil emulsion in a quantity substantially equivalent to the isocyanate groups, (d) directly coating the water-in-oil emulsion on a substrate, and (e) hardening the coating by evaporating the chemically unbound water from said coating.

Claim 4

A process for the production of microporous coatings comprising: (a) mixing an NCO-prepolymer prepared from polyisocyanates with compounds containing at least two isocyanate-reactive hydrogen atoms with about 3 to 40% by weight, based on the NCO-prepolymer, of a substantially inert, with respect to isocyanate groups, viscosity-reducing, non-migrating liquid organic compound miscible with said NCO-prepolymer as a plasticizer, wherein (i) said NCO-prepolymer is used free from solvents, has a viscosity of more than about 500 cP at 25° C. and a molecular weight of from about 300 to 20,000, (ii) said plasticizer has a volatility of less than 10% weight loss after storage for 72 hours at 90° C., and (iii) the resultant NCO-prepolymer-plasticizer mixture has a viscosity of less than about 15,000 cP at 20° C., (b) dispersing 3 to 300% by weight of water, based on the NCO-prepolymer into the NCO-prepolymer-plasticizer mixture to form a water-in-oil emulsion, (c) adding a polyamine to the water-in-oil emulsion in a quantity substantially equivalent to the isocyanate groups, (d) directly coating the water-in-oil emulsion on a substrate, and (e) hardening the coating by evaporating the chemically unbound water from said coating.

Claim 5

The process of claim 2 wherein the polyamine is dissolved in water.

Claim 6

The process of claim 3 wherein a catalyst capable of catalyzing the reaction of isocyanate groups with water is added to the water-in-oil emulsion.

Claim 7

A process for the production of microporous isocyanate polyaddition product coatings comprising: (a) mixing an NCO-prepolymer prepared from polyisocyanates with compounds containing at least two isocyanate-reactive hydrogen atoms with about 3 to 40% by weight, based on the NCO-prepolymer, of a plasticizer wherein (i) the NCO-prepolymer contains less than about 1 wt. % of volatile substances which can be removed over a period of 1 hour in a vacuum of 12 Torr, has a viscosity of more than about 500 cP at 25° C. and has a molecular weight of from about 300 to 20,000, (ii) the plasticizer is an organic compound which has a volatility of less than 5% weight loss after storage for 72 hours at 90° C., is chemically inert to isocyanate groups, is miscible with the NCO-prepolymer, and has an affinity for the ultimately formed isocyanate polyaddition product, and (iii) the mixture has a viscosity of less than about 15,000 cP at 20° C., (b) adding about 3 to 300 wt. % of water based on the NCO-prepolymer to said mixture to form a water in oil emulsion, said water having dispersed therein a diamine in a quantity substantially equivalent to the isocyanate groups to form an isocyanate polyaddition product with the NCO-prepolymer, (c) applying a coating of the water-in-oil coating emulsion to a substrate, and (d) hardening the coating by evaporating the chemically unbound water from it at temperatures below the boiling point of the lowest boiling point volatile contained in the coating.

Claim 8

A process for the production of microporous isocyanate polyaddition product coatings comprising: (a) mixing an NCO-prepolymer prepared from polyisocyanates with compounds containing at least two isocyanate-reactive hydrogen atoms with about 3 to 40% by weight, based on the NCO-prepolymer, of a plasticizer wherein (i) the NCO-prepolymer contains less than about 1 wt. % of volatile substances which can be removed over a period of 1 hour in a vacuum of 12 Torr, has a viscosity of more than about 500 cP at 25° C. and has a molecular weight of from about 300 to 20,000, (ii) the plasticizer is an organic compound which has a volatility of less than 5% weight loss after storage for 72 hours at 90° C., is chemically inert to isocyanate groups, is miscible with the NCO-prepolymer, and has an affinity for the ultimately formed isocyanate polyaddition product, and (iii) the mixture has a viscosity of less than about 15,000 cP at 20° C., (b) adding about 3 to 300 wt. % of water based on the NCO-prepolymer to said mixture to form a water in oil emulsion, said water having dispersed therein a diamine in a quantity substantially equivalent to the isocyanate groups to form an isocyanate polyaddition product with the NCO-prepolymer, (c) applying a coating of the water-in-oil coating emulsion to a substrate, and (d) hardening the coating by evaporating the chemically unbound water from it at temperatures below the boiling point of the lowest boiling point volatile contained in the coating.