Method for the purification of isocyanates
Isocyanates are prepared by a process in which a product stream from the isocyanate synthesis is purified.
1. A method of purifying a product stream from isocyanate synthesis, comprising:
separating a crude isocyanate stream into a gaseous vapor stream and a liquid part-stream by distillation;
recovering isocyanate present in the liquid part-stream as an isocyanate-containing residual stream in vapor form;
wherein:
recovering isocyanate is carried out in a falling-film evaporator, a rising-film evaporator, a thin-film evaporator, a long-tube vertical-film evaporator, a helical-tube evaporator, a forced-circulation flush evaporator, a paddle dryer without cooling zone and with discharge screw for the nonvaporizable residue, or a combination thereof.
2. The method according to claim 1 , wherein recovering isocyanate is carried out in the thin-film evaporator, the falling-film evaporator, the forced-circulation flush evaporator or the paddle dryer without cooling zone and with discharge screw for the nonvaporizable residue, or a combination thereof.
3. The method according to claim 1 , wherein recovering isocyanate is carried out in the paddle dryer without cooling zone and with discharge screw for the nonvaporizable residue.
4. The method according to claim 1 , wherein the crude isocyanate stream is obtained by phosgenation of an amine, by phosgenation of an amine hydrochloride, by phosgenation of a carbamate salt, by urea process or by reaction of a parent amine with dialkyl carbonates.
5. The method according to claim 1 , wherein the crude isocyanate stream is obtained by phosgenation of an amine, by phosgenation of an amine-hydrochloride or by phosgenation of a carbamate salt.
6. The method according to claim 1 , wherein the crude isocyanate stream is obtained by phosgenation of an amine.
7. The method according to claim 1 , wherein the isocyanate is selected from the group consisting of monomeric methylenediphenyl isocyanate (MDI), tolylene diisocyanate (TDI), R,S-1-phenylethyl isocyanate, 1-methyl-3-phenylpropyl isocyanate, naphthyl diisocyanate (NDI), n-pentyl isocyanate, 6-methyl-2-heptane isocyanate, cyclopentyl isocyanate, hexamethylene diisocyanate (HDI), isophorone diisocyanate (IPDI), 2,4- and 2,6-diisocyanatomethylcyclohexane (H6TDI) and isomer mixtures thereof, o-, m- or p-xylene diisocyanate (XDI), diisocyanatocyclohexane (t-CHDI), di(isocyanatocyclohexyl)methane (H12MDI), tetramethyl-m-xylylene diisocyanate (m-TMXDI), 1,3-bis(isocyanatomethyl)cyclohexane (H6XDI), 1,6-diisocyanato-2,2,4,4-tetramethylhexane, 1,6-diisocyanato-2,2,4-trimethylhexane (TMDI) and mixtures thereof.
8. The method according to claim 1 , wherein the isocyanate is selected from the group consisting of monomeric methylenediphenyl isocyanate (MDI), tolylene diisocyanate (DI), naphthyl diisocyanate (NDI), hexamethylene diisocyanate (HDI), isophorone diisocyanate (IPDI), 2,4- and 2,6-diisocyanatomethylcyclohexane (H6TDI) and isomer mixtures thereof, o-, m- or p-xylene diisocyanate (XDI), di(isocyanatocyclohexyl)methane (H12MDI) and diisocyanatocyclohexane (t-CHDI).
9. The method according to claim 1 , wherein recovering isocyanate is carried out at a temperature of from 80 to 320° C.
10. The method according to claim 1 , wherein recovering isocyanate is carried out at a pressure of from 0.1 to 40 mbar.
11. A method of purifying a product stream from isocyanate synthesis, comprising:
separating a crude isocyanate stream into a gaseous vapor stream and a liquid part-stream by distillation;
recovering isocyanate present in the liquid part-stream as an isocyanate-containing residual stream in vapor form;
wherein:
recovering isocyanate is carried out in a paddle dryer without a cooling zone and optionally including a discharge screw for non-vaporizable residue.