Process for continuous isocyanate modification
View Patent ↗A process for continuous preparation of oligomeric or polymeric isocyanates by catalytic modification of monomeric di- and/or triisocyanates, characterized in that at least one isocyanate component A and at least one catalyst component B are combined continuously in a reaction apparatus and conducted through the reaction apparatus as a reaction mixture, the residence time distribution being characterized according to the dispersion model by Bo (Bodenstein number) above 40, preferably above 60 and most preferably above 80.
1. A process for the continuous preparation of oligomeric or polymeric isocyanates by catalytic modification of monomeric diisocyanates and/or triisocyanates, comprising continuously combining at least one isocyanate component A and at least one catalyst component B in a reaction apparatus and conveying as reaction mixture through the reaction apparatus, wherein a residence time distribution according to the dispersion model has a Bo (Bodenstein number) above 40 and wherein the residence section has a maximum pressure drop of from 0 to 30 bar and has a heat transfer rate above 10 kW/(K m3).
2. An oligomeric or polymeric isocyanate obtained by the process as claimed in claim 1 .
3. A method for producing optionally foamed plastics and surface coatings, coating compositions, adhesives and auxiliaries comprising utilizing the oligomeric or polymeric isocyanates as claimed in claim 2 .
4. The process according to claim 1 , wherein the catalyst is used in a proportion of from 5 mol-ppm to 0.1 mol %, based on the mass of diisocyanate and/or triisocyanate used.
5. The process according to claim 1 , wherein the isocyanate component and the catalyst component are combined using an intensive mixer.
6. The process according to claim 1 , wherein not only the components A and B but also further compounds are present in the reaction mixture or these are introduced along the reaction section, where these are, in the first case, bonding agents, stabilizers or fluidizers and in the second case, bonding agents, stabilizers, fluidizers, diisocyanates or triisocyanates different from A, catalysts different from B or catalyst-deactivating materials.
7. The process according to claim 1 , wherein intensive mixing of all components is effected by use of mixing elements along the residence section.
8. The process according to claim 1 , wherein it is carried out in the temperature range from 0° C. to +200° C., with a constant reaction temperature being realized over the entire reaction region.
9. The process according to claim 1 , wherein pentane 1,5-diisocyanate, hexamethylene diisocyanate (HDI), 2-methylpentane 1,5-diisocyanate, 2,4,4-trimethylhexane 1,6-diisocyanate, 2,2,4-trimethylhexane 1,6-diisocyanate, 4-isocyanatomethyloctane 1,8-diisocyanate, 3(4)-isocyanatomethyl-1-methylcyclohexyl isocyanate (IMCI), isophorone diisocyanate (IPDI), 1,3- and 1,4-bis(isocyanatomethyl)benzene (XDI), 1,3- and 1,4-bis(isocyanatomethyl)cyclohexane (H6XDI), tolylene 2,4- and 2,6-diisocyanate (TDI), bis(4-isocyanatophenyl)methane (4,4′-MDI), 4-isocyanatophenyl-2-isocyanatophenylmethane (2,4′-MDI) and/or multi-ring products which can be obtained by formaldehyde-aniline polycondensation and subsequent conversion of the resulting (poly)amines into the corresponding (poly)isocyanates (polymeric MDI) are used as diisocyanates and/or triisocyanates.
10. The process according to claim 1 , wherein aliphatic diisocyanates and/or triisocyanates are used.
11. The process according to claim 1 , wherein
tetraorganylammonium and/or tetraorganylphosphonium salts whose anions are derived by H+ abstraction from weak acids selected from the group consisting of carboxylic acids, carboxylic acids bearing fluorinated alkyl groups, phenols, alcohols, water and HF, in solid or dissolved form,
alcoholic solutions of alkali metal and alkaline earth metal oxides, hydroxides, alkoxides and phenoxides,
alcoholic solutions of metal salts of carboxylic acids, selected from the group consisting of potassium acetate, sodium benzoate, sodium acetate and potassium formate and/or
tertiary phosphines which contain the phosphorus atom as part of a ring, in solid or dissolved form,
are used as catalysts.
12. The process according to claim 1 , wherein the catalyst is used in a proportion of from 1 mol-ppm to 1 mol %, based on the mass of diisocyanate and/or triisocyanate used.
13. The process as claimed in claim 1 , wherein the process is stopped after from 5 to 80% of the monomeric diisocyanate and/or triisocyanate used has been reacted.
14. The process according to claim 1 , wherein the catalyst is used in a proportion of from 5 mol-ppm to 0.1 mol %, based on the mass of diisocyanate and/or triisocyanate used.