Separation of ammonium chloride from the gas phase of an isocyanate production process

1. A process for producing an isocyanate comprising:

(a) feeding an amine and phosgene to a reactor wherein the amine is phosgenated in the gas phase to produce a gas phase isocyanate-containing reaction mixture,

(b) feeding the gas phase isocyanate-containing reaction mixture and a quenching agent to a scrubber to separate the isocyanate from the gas stream;

(c) feeding the gas stream from the scrubber to a condenser to produce a gas stream free of liquid constituents or constituents condensable to liquid form;

(d) feeding the gas stream produced by the condenser to a scrubber that separates the gas stream into a waste gas stream and a phosgene stream; and

(e) feeding the phosgene produced by the scrubber to the phosgene that is fed to the reactor,

wherein the process further comprises separating a by-product from a gas stream subsequent to (a) by desublimating the by-product as a solid at a point in the process subsequent to the condenser, and

wherein the desublimation is carried out in one or more plate-type heat exchangers operated with a heat transfer medium that has a temperature of from 100° C to −40° C.

2. The process of claim 1 in which the amine is triaminocyclohexane; tris(aminomethyl)cyclohexane, triaminomethylcyciohexane;

1,8-diamino-4-(aminomethyhoctane; 1,6,11-undecanetriamine; 1,7-diamino-4-(3-aminopropyl)heptane;1,6-diamino-3-(aminomethyl)hexane; 1,3,5-tris(aminomethyl)cyclohexane; an isomer of toluenediamine (TDA)or a mixture of TDA isomers; diaminobenzene; 2,8-xylidine; naphthylenediamine (NDA); or 2,4′-, 4,4′-methylene(diphenylarnine) (MDA); 1,4-diaminobutane; 1,6-diaminohexane; 1,8-diaminooctane; 1,10-diaminodecane; 1,8-diamino-3,3,5-trimethylhexane; 1-amino-3,3,5-trimethyl-5-aminornethylcyclohexane (IPDA); 2,4- or 2,8-diamino-1-methylcyclohexane; and 4,4′-diaminodicyclohexylmethane 1,6-Diaminohexane; -amino-3,3,5-trimethyl-5-(aminomethy)clcyolohexane; and/or 4,4′-di(aminocyclohexyl)methane.

3. The process of claim 1 in which the amine and phosgene are fed to the reaction zone as a mixture with an inert gas.

4. The process of claim 1 in which the temperature in the reaction zone is greater than 260° C. and below 570° C.

5. The process of claim 1 in which the heat exchanger is designed and the process is operated under conditions such that gas being treated has a velocity of 2 m/s or less on passage through the heat exchanger used for the desublimation.

6. The process of claim 1 in which the by-product separated off is an ammonium halide.