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Aqueous polyurethane—vinyl polymer hybrid dispersions

  • US 10,239,987 B2
  • Filed: 07/24/2015
  • Issued: 03/26/2019
  • Est. Priority Date: 07/31/2014
  • Status: Active Grant
First Claim
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1. A process for the preparation of an aqueous polyurethane-vinyl polymer hybrid dispersion, comprisingin step a), producing a polyester A′

  • having residual hydroxyl and acid groups by a polyesterification process wherein a mixture of aliphatic diols A1 and aliphatic and/or aromatic diacids A2, optionally in the presence of hydroxyacids A3, and further optionally, in the presence of one or more of hydroxy compounds A11 having more than two hydroxyl groups, acid compounds A21 having more than two acid groups, or hydroxyacids A31 having more than one hydroxyl group or more than one acid group, or at least two hydroxyl groups and at least two acid groups, is esterified at an elevated temperature of up to 250°

    C., under removal of a water formed in the polycondensation reaction,in step b), producing hydrophobically modified polyesters A by reacting the acid groups of the polyester A′

    with a mono-functional compound A4 having an epoxide or aziridine functionality, and a linear or branched alkyl residue of at least four carbon atoms, in which reaction at least 90% of the remaining acid groups are converted to ester or amide groups,in step c), mixing the hydrophobically modified polyesters A withacids B that have further groups which react with isocyanates under formation of urethanes, ureas, or thiourethanes,optionally, hydroxy-functional oligomeric or polymeric compounds C selected from the group consisting of polyesters, polycarbonates, polyethers, polyamides, polydienes and polyenes, and which have at least two hydroxyl groups per molecule, andoptionally, monomeric hydroxy compounds D having at least two hydroxyl groups per molecule,wherein none, either, or both of C and D are added to the mixture, andheating the resulting mixture under stirring to at least 60°

    C. to form a homogeneous solution,in step d), adding a substoichiometric quantity of a multifunctional isocyanate I to the homogeneous solution and keeping the reaction temperature in a range of from 60°

    C. to 150°

    C., to form a prepolymer, and wherein the amount of substance of isocyanate groups in the quantity of multifunctional isocyanate I added is less than the sum of the amounts of substance of isocyanate-reactive hydroxyl groups, of the compounds A, B, C, and D present in this reaction, so that no more unreacted isocyanate groups are present in the reaction mixture,in step e), adding to this the prepolymer,a solution which comprises at least one olefinically unsaturated monomer H1 having no further functional group other than one or more vinyl or polymerisable olefinically unsaturated groups, and at least one olefinically unsaturated monomer H2 having at least one hydroxyl group and a vinyl or polymerisable olefinically unsaturated group,optionally, an antioxydant or radical scavenger, andoptionally, a solvent S which is inert in the reaction, andhomogenising the solution and the prepolymer to form a homogenous mixture,in step f), adding to the homogeneous mixture, a further multifunctional isocyanate I in stoichiometric excess so that the ratio of the amount of substance of isocyanate groups n(NCO) to the sum n(OH, Σ

    ) of the amounts of substance of isocyanate-reactive groups hydroxyl groups present in the reaction mixture satisfies the following formula;


    n(NCO)/n(OH,Σ

    )≥

    1.02 mol/mol,in step g), adding thereto a mixture which comprises compounds G, water, optionally, compounds E, optionally, compounds F,and homogenising well the resulting mixture,in step h), adding an aqueous solution of a radical initiator to the mixture of resulting from step g),andin step i), polymerising the reaction mixture to obtain a dispersion which is finally cooled to room temperature and filtered.

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