Solvent borne polyurethane process
Abstract
A process for obtaining a solvent borne polyurethane composition comprising preparing an isocyanate-terminated prepolymer A; reacting the isocyanate groups of isocyanate-terminated prepolymer A with 0.1 to 1.8 stoichiometric equivalents of at least one active-hydrogen containing chain-terminating compound and or chain-extending compound; optionally introducing an isocyanate-terminated compound B; and reacting the isocyanate groups of the isocyanate-terminated prepolymer obtained in the previous steps and isocyanate-terminated compound B with 0 to 1.2 stoichiometric equivalents of at least one active-hydrogen containing chain-terminating compound and or chain-extending compound.
Claims
exact text as granted — not AI-modified1 . A process for obtaining a solvent borne polyurethane composition comprising 80 to 25 wt % of a liquid medium, where the liquid medium comprises <20 wt % of water and where the PDi of the solvent borne polyurethane is in the range of from 2.8 to 6, the process comprising the following steps:
1) preparing an isocyanate-terminated prepolymer A; 2a) reacting the isocyanate groups of isocyanate-terminated prepolymer A with 0 to 0.95 stoichiometric equivalents of at least one active-hydrogen containing chain-terminating compound selected from the group consisting of mono-alcohols, amino-alcohols, primary or secondary amines and mono-functional hydrazines; 2b) reacting the isocyanate groups of isocyanate-terminated prepolymer A with 0 to 0.95 stoichiometric equivalents of at least one active-hydrogen containing chain-extending compound; where steps 2a) and 2b) together are in the range of from 0.1 to 1.8 stoichiometric equivalents; 3) optionally introducing an isocyanate-terminated compound B; 4a) reacting the isocyanate groups of the isocyanate-terminated prepolymer obtained in steps 2a) and 2b) and isocyanate groups of the isocyanate-terminated compound B introduced in step 3) with 0 to 1.0 stoichiometric equivalents of at least one active-hydrogen containing chain-terminating compound selected from the group consisting of mono-alcohols, amino-alcohols, primary or secondary amines and mono-functional hydrazines; 4b) reacting the isocyanate groups of the isocyanate-terminated prepolymer obtained in steps 2a) and 2b) and the isocyanate groups of the isocyanate-terminated compound B introduced in step 3) with 0 to 1.2 stoichiometric equivalents of at least one active-hydrogen containing chain-extending compound; where steps 4a) and 4b) together are in the range of from 0 to 1.2 stoichiometric equivalents; where the process comprises at least one step with an active-hydrogen containing chain-extending compound and at least one step with an active-hydrogen containing chain-terminating compound; where if 0 wt % of the isocyanate-terminated compound B is introduced then step 2a) comprises 0.1 to 0.95 stoichiometric equivalents of at least one active-hydrogen containing chain-terminating compound and at least a step 2a) is performed before a step 2b).
2 . A process for obtaining a solvent borne polyurethane composition comprising the following steps:
1) preparing an isocyanate-terminated prepolymer A; 2a) reacting the isocyanate groups of isocyanate-terminated prepolymer A with 0 to 0.95 stoichiometric equivalents of at least one active-hydrogen containing chain-terminating compound; 2b) reacting the isocyanate groups of isocyanate-terminated prepolymer A with 0 to 0.95 stoichiometric equivalents of at least one active-hydrogen containing chain-extending compound; where steps 2a) and 2b) together are in the range of from 0.1 to 1.8 stoichiometric equivalents; 3) optionally introducing an isocyanate-terminated compound B; 4a) reacting the isocyanate groups of the isocyanate-terminated prepolymer obtained in steps 2a) and 2b) and isocyanate groups of the isocyanate-terminated compound B introduced in step 3) with 0 to 1.0 stoichiometric equivalents of at least one active-hydrogen containing chain-terminating compound; 4b) reacting the isocyanate groups of the isocyanate-terminated prepolymer obtained in steps 2a) and 2b) and the isocyanate groups of the isocyanate-terminated compound B introduced in step 3) with 0 to 1.2 stoichiometric equivalents of at least one active-hydrogen containing chain-extending compound; where steps 4a) and 4b) together are in the range of from 0 to 1.2 stoichiometric equivalents; where the process comprises at least one step with an active-hydrogen containing chain-extending compound and at least one step with an active-hydrogen containing chain-terminating compound.
3 . A process according to claim 1 where steps 2a) and 2b) together are in the range of from 0.2 to 0.95 stoichiometric equivalents.
4 . A process according to claim 1 where step 3 comprises introducing 0 to 1600 by weight of isocyanate-terminated prepolymer A of an isocyanate-terminated compound B.
5 . A process according to claim 1 where the Mp of the solvent borne polyurethane is in the range of from 6,000 to 60,000 g/mol.
6 . A process according to claim 2 where the PDi of the solvent borne polyurethane is in the range of from 1.3 to 10.
7 . A process according to claim 1 where the Mp of the solvent borne polyurethane is in the range of from 6,000 to 60,000 g/mol and the PDi is in the range of from 2.8 to 6.
8 . A process according to claim 1 where isocyanate-terminated prepolymer A is obtained by reacting components comprising:
(i) 8 to 45 wt % of at least one polyisocyanate;
(ii) 0 to 5 wt % of at least one isocyanate-reactive polyol with a weight-average molecular weight in the range of from 50 to 200 g/mol;
(iii) 40 to 92 wt % of at least one isocyanate-reactive polyol with a weight-average molecular weight in the range of from 201 to 20,000 g/mol; and
(iv) 0 to 3 wt % of an isocyanate-reactive polyol not comprised by (ii) or (iii); where (i), (ii), (iii) and (iv) add up to 100%; optionally in the presence of a liquid medium.
9 . A process according to claim 1 where isocyanate-terminated compound B is at least one polyisocyanate.
10 . A process according to claim 1 where isocyanate-terminated compound B is at least one isocyanate-terminated prepolymer B.
11 . A process according to claim 10 where isocyanate-terminated prepolymer B is obtained by reacting components comprising:
(i) 8 to 45 wt % of at least one polyisocyanate;
(ii) 0 to 5 wt % of at least one isocyanate-reactive polyol with a weight-average molecular weight in the range of from 50 to 200 g/mol; (iii) 40 to 92 wt % of at least one isocyanate-reactive polyol with a weight-average molecular weight in the range of from 201 to 20,000 g/mol; and
(iv) 0 to 3 wt % of an isocyanate-reactive polyol not comprised by (ii) or (iii); where (i), (ii), (iii) and (iv) add up to 100%; optionally in the presence of a liquid medium.
12 . A process according to any claim 8 where the liquid medium comprises <20 wt % of water.
13 . A process according to claim 1 where the solvent borne polyurethane composition has a viscosity <5,000 mPa-s at any solids content in the range of from 45 to 75 wt % in a solvent comprising >70 wt % of at least one solvent having an evaporation rate of >1.0.
14 . An ink comprising a solvent borne polyurethane composition obtained by a process according to claim 1 , a colorant and optionally an additional organic solvent.
15 . An ink comprising a solvent borne polyurethane composition, a colorant and optionally an additional organic solvent, wherein the solvent borne polyurethane composition is obtained by a process comprising the following steps:
1) preparing an isocyanate-terminated prepolymer A; 2a) reacting the isocyanate groups of isocyanate-terminated prepolymer A with 0 to 0.95 stoichiometric equivalents of at least one active-hydrogen containing chain-terminating compound; 2b) reacting the isocyanate groups of isocyanate-terminated prepolymer A with 0 to 0.95 stoichiometric equivalents of at least one active-hydrogen containing chain-extending compound; where steps 2a) and 2b) together are in the range of from 0.1 to 1.8 stoichiometric equivalents; 3) optionally introducing an isocyanate-terminated compound B; 4a) reacting the isocyanate groups of the isocyanate-terminated prepolymer obtained in steps 2a) and 2b) and isocyanate groups of the isocyanate-terminated compound B introduced in step 3) with 0 to 1.0 stoichiometric equivalents of at least one active-hydrogen containing chain-terminating compound; 4b) reacting the isocyanate groups of the isocyanate-terminated prepolymer obtained in steps 2a) and 2b) and the isocyanate groups of the isocyanate-terminated compound B introduced in step 3) with 0 to 1.2 stoichiometric equivalents of at least one active-hydrogen containing chain-extending compound; where steps 4a) and 4b) together are in the range of from 0 to 1.2 stoichiometric equivalents; where the process comprises at least one step with an active-hydrogen containing chain-extending compound and at least one step with an active-hydrogen containing chain-terminating compound.
16 . An ink according to claim 14 having a viscosity in the range of from 10 to 100 seconds when measured using a Ford Cup 4 at 20° C.
17 . A method for printing an image on a substrate comprising applying an ink according to claim 14 .
18 . A flexographic printing process for printing an image on a substrate comprising applying to the substrate an ink according to claim 14 .
19 . A gravure printing process for printing an image on a substrate comprising applying to the substrate an ink according to claim 14 .
20 . A laminate comprising a substrate printed with an ink according to claim 14 .
21 . A process for making an ink comprising combining a colourant, a solvent borne polyurethane, and optionally an additional organic solvent, wherein the solvent borne polyurethane is obtained by the steps of:
1) preparing an isocyanate-terminated prepolymer A; 2a) reacting the isocyanate groups of isocyanate-terminated prepolymer A with 0 to 0.95 stoichiometric equivalents of at least one active-hydrogen containing chain-terminating compound; 2b) reacting the isocyanate groups of isocyanate-terminated prepolymer A with 0 to 0.95 stoichiometric equivalents of at least one active-hydrogen containing chain-extending compound; where steps 2a) and 2b) together are in the range of from 0.1 to 1.8 stoichiometric equivalents; 3) optionally introducing an isocyanate-terminated compound B; 4a) reacting the isocyanate groups of the isocyanate-terminated prepolymer obtained in steps 2a) and 2b) and isocyanate groups of the isocyanate-terminated compound B introduced in step 3) with 0 to 1.0 stoichiometric equivalents of at least one active-hydrogen containing chain-terminating compound; 4b) reacting the isocyanate groups of the isocyanate-terminated prepolymer obtained in steps 2a) and 2b) and the isocyanate groups of the isocyanate-terminated compound B introduced in step 3) with 0 to 1.2 stoichiometric equivalents of at least one active-hydrogen containing chain-extending compound; where steps 4a) and 4b) together are in the range of from 0 to 1.2 stoichiometric equivalents; where the process comprises at least one step with an active-hydrogen containing chain-extending compound and at least one step with an active-hydrogen containing chain-terminating compound.
22 . A process for making an ink according to claim 21 , wherein the ink has a viscosity in the range of from 10 to 100 seconds when measured using a Ford Cup 4 at 20° C.
23 . A method for printing an image on a substrate comprising applying an ink according to claim 21 .
24 . A flexographic printing process for printing an image on a substrate comprising applying to the substrate an ink according to claim 21 .
25 . A gravure printing process for printing an image on a substrate comprising applying to the substrate an ink according to claim 21 .Join the waitlist — get patent alerts
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