Process for preparing polyisocyanates by the adiabatic phosgenation of primary amines
View Patent ↗A two-stage process for the preparation of organic isocyanates by reacting primary amines with phosgene in which: a) in a first stage, amine and phosgene are reacted in an adiabatically managed reaction, in which the temperature of reaction is restricted to values between 100 and 220° C. by actively adjusting the absolute pressure in the reactor to values between 8 and 50 bar by decompression, and the temperature is held at values between 100 and 220° C. until the stoichiometric conversion of phosgene has reached at least 80%; and then b) in a second stage, the reaction mixture from a) is decompressed to an absolute pressure of 1 to 15 bar and the reaction mixture is reacted further at temperatures between 90 and 240° C., optionally with the introduction of heat.
1. A two-stage process for the production of an organic isocyanate by reacting a primary amine with phosgene comprising:
a) in a first stage, adiabatically reacting the amine and phosgene in a temperature controlled reactor in which reaction temperature is maintained between 100 and 220° C. by actively adjusting absolute pressure in the reactor to values between 8 and 50 bar by decompression until at least 80% of the phosgene has been consumed, and
b) in a second stage, decompressing reaction mixture from a) to an absolute pressure of 1 to 15 bar and further reacting the decompressed reaction mixture at temperatures between 90 and 200° C., optionally with the introduction of heat.
2. The process of claim 1 in which the reaction temperature in step a) is restricted to between 115 and 180° C.
3. The process of claim 1 in which the absolute pressure in the reactor in step a) is actively restricted to between 12 and 25 bar.
4. The process of claim 1 in which the temperature in step a) is held between 100 and 220° C. until conversion of phosgene has reached at least 95%.
5. The process of claim 1 in which the reaction mixture is decompressed to an absolute pressure of from 1 to 7 bar in step b).