发明名称 Aqueous polyurethane-polyurea dispersions
摘要 The invention relates to a method for producing aqueous polyurethane-polyurea dispersions, aqueous polyurethane-polyurea dispersions produced by this method and their use to produce coating agents and adhesives.
申请公布号 US9206331(B2) 申请公布日期 2015.12.08
申请号 US201113640986 申请日期 2011.04.13
申请人 Covestro Deutschland AG 发明人 Zastrow Alfred;Witkowski Reiner;Werner Ralf;Kurek Gerald;Rische Thorsten;Avtomonov Evgeny;Kraus Harald;Peerlings Henricus
分类号 C08G18/08;C08G18/28;C08J3/00;C08K3/20;C08L75/00;C09D175/06;C09J175/04;C09D175/04;C08G18/12;C08G18/10;C08G18/42;C08G18/72;C08G18/73;C09J175/06 主分类号 C08G18/08
代理机构 Drinker Biddle & Reath LLP 代理人 Drinker Biddle & Reath LLP
主权项 1. Method for producing aqueous polyurethane-polyurea dispersions, wherein in a first step (I) an isocyanate-functional prepolymer free from urea groups is produced by complete or partial reaction of compounds A) polyisocyanates, B) polyols having number-average molecular weights of 400 to 8000 g/mol, C′) low-molecular-weight compounds having a molecular weight of 60 to 400, which in total have two or more hydroxyl groups, D′) optionally compounds having one hydroxyl group, E) isocyanate-reactive, ionically or potentially ionically hydrophilising compounds, F) isocyanate-reactive, non-ionically hydrophilising compounds, optionally already in at least one organic solvent, or in a second step (II), if not in step (I), this isocyanate-functional prepolymer is dissolved in at least one organic solvent in such a way that a solution of the isocyanate-functional prepolymer is produced in a concentration of 20 wt. % to 70 wt. %, relative to all components of the solution, in a third step (III) the optional addition of C″) low-molecular weight compounds having a molecular weight of 32 to 400, which in total have two or more amino groups and/or hydroxyl groups, or D″) optionally compounds having one amino group takes place and then dispersion takes place by mixing water with the polymer solution with simultaneous distillation of the organic solvent in a dispersion and distillation unit, with the proviso that the volumetric content of the dispersion and distillation unit is 50 vol. % to 95 vol. %, and then a largely solvent-free polyurethane-polyurea dispersion having a residual content of organic solvent of 0.0 wt. % to 5 wt. % and a concentration of polyurethane-polyurea polymer particles of 20 wt. % to 70 wt %, relative in each case to all components of the polyurethane-polyurea dispersion, is obtained.
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