Polyamine crosslinking agent formulation and its preparation
AssigneeBayer Aktiengesellschaft
InventorsKlaus Konig, Otto Neuner, Werner Rasshofer
Life of this patent
Estimating the term…
Loading patent…
AssigneeBayer Aktiengesellschaft
InventorsKlaus Konig, Otto Neuner, Werner Rasshofer
Estimating the term…
Liquid polyamine crosslinking agent formulations based on trimerized toluylene 2,4- and/or 2,6-diisocyanate, with formation of an isocyanurate structure and hydrolysis of the isocyanate groups to amine groups, are described. The novel crosslinking agent formulations have a content of 40 to 80% of the total weight of the solids content of the crosslinking agent formulation of 1,3,5-tris-(3-amino-4-methyl-phenyl,2-methyl-3-aminophenyl) isocyanurate (I) which is not further condensed, and a content of not more than 1.0% of the total weight of the crosslinking agent formulations of toluylene-2,4- and/or -2,6-diamine (III). For the preparation, toluylene diisocyanate is trimerized, to form the isocyanurate structure, until 10 to 25% of the NCO groups have been reacted. The toluylene diisocyanate which has not undergone condensation is then distilled off, the bottom product formed by this operation is taken up directly in a solvent A and the 30 to 70% strength by weight solution formed by this procedure is metered into a hydrolysis in water/N,N-dialkyl-carboxylic acid amide in the presence of a catalytic amount of a basic catalyst. After the hydrolysis, the crosslinking agent formulations are brought to a solids content of 35 to 60% of the total weight of the formulation by distilling off a portion of the solvents and adding a solvent B.
A liquid polyamine crosslinking agent formulation with a solids content based on a triamine of the formula (I) ##STR8## in which R.sup.1,R.sup.2 and R.sup.3 independently of one another denote 2-methyl-3-amino-phenyl or 3-amino-4-methyl-phenyl,
The process of 10, wherein the distillation in step b) is carried out at a heating medium temperature of 160.degree. to 180.degree. C.
The process of 10, wherein the distillation in step b) is carried out under 0.1 to 20 mbar.
The process of 10, wherein the distilling off of a portion of the solvents in step e) results in a 70 to 85% strength by weight solution of the hydrolysis product.
Dependencies are inferred from the claim text.