Processes for in-mold coating using a multi-cavity mold and substrates coated thereby

1. A process for in-mold coating comprising:

(a) molding a plastic substrate in a first mold cavity of a mold comprising at least two cavities to form a molded plastic substrate;

(b) introducing the molded plastic substrate into a second mold cavity of the mold;

(c) introducing a coating composition into the second mold cavity containing the molded plastic substrate in order to coat the substrate, the coating composition comprising:

(i) a polymer comprising isocyanate-reactive groups; and

(ii) a polyisocyanate;

(d) curing the composition in the second mold cavity at cure conditions of a mold temperature of 62-105° C. and an external mold pressure of at least 100 kg/mm 2 for a period of at least 60 seconds; and

(e) opening the mold cavity, wherein the coated molded substrate release from the second mold cavity by gravity alone or with suction alone.

2. The process of claim 1 , wherein the substrate comprises a polycarbonate/acrylonitrile butadiene styrene (PC/ABS) blend.

3. The process of claim 1 , wherein the molding of the substrate in the first mold cavity is conducted in the presence of a silicone comprising isocyanate-reactive functional groups.

4. The process of claim 1 , wherein the coating composition is a 100% solids composition.

5. The process of claim 1 , wherein the polymer comprising isocyanate-reactive groups comprises: (i) an aromatic branched polyester polyol; and (ii) an aliphatic polycarbonate polyol.

6. The process of claim 5 , wherein the aromatic branched polyester polyol has a M n of 400 to 1000 gram/mole, a hydroxyl functionality of 1.9 to 2.5, a viscosity at 23° C. of 3000 to 5000 mPa·s, when measured according to DIN EN ISO 3219/A3 determined using a rotational viscometer—Visco Tester® 550, Thermo Haake GmbH, a hydroxyl content of 15.4-16.6% measured according to DIN 53 240/2, and a hydroxyl number of 100 to 200 mg KOH/gram.

7. The process of claim 5 , wherein the weight ratio of (i) and (ii) in the coating composition is in the range of 1:4 to 4:1.

8. The process of claim 1 , wherein the polyisocyanate comprises an isocyanurate of hexamethylene diisocyanate.

9. The process of claim 8 , wherein the polyisocyanate has a viscosity at 23° C. and at 100% solids of 800 to 1400 mPa·s, when measured according to DIN EN ISO 3219/A3 determined using a rotational viscometer—Visco Tester® 550, Thermo Haake GmbH; an isocyanate group content of 22.5-23.5% according to DIN EN ISO 11909; an NCO calculated functionality of 2.8 to 3.2; and a content of monomeric diisocyanate of less than 1 wt. %.

10. The process of claim 1 , wherein the polymer comprising isocyanate-reactive groups and the polyisocyanate are combined in relative amounts such that the coating composition has a ratio of isocyanate groups to isocyanate-reactive groups of 1:1 to 1.8:1.

11. The process of claim 10 , wherein the ratio is at least 1.3:1.

12. The process of claim 1 , wherein the composition further comprises a polyether-modified silicone present in the composition in an amount of 0.1 to 1.0 percent by weight, based on the total weight of the coating composition.

13. The process of claim 1 , wherein the composition further comprises a silicone that is present in the composition in an amount sufficient to provide a cured coating with a surface tension of no more than 30 dynes/cm.

14. The process of claim 1 , wherein an external release agent is present on a surface of the second mold cavity, wherein the external release agent comprises a coating comprising electroless nickel and polytetrafluoroethylene.

15. The process of claim 1 , wherein the coating is cured:

(a) at a mold temperature of 75 to 105° C.,

(b) an external mold pressure of at least 110 (10787 bar); and

(c) for a period of at least at least 70 seconds.