Process for the preparation of isocyanates in the gas phase
View Patent ↗Aromatic isocyanates are produced by reacting one or more aromatic primary amines with phosgene in the gas phase. The phosgene and primary aromatic amine(s) are reacted at a temperature above the boiling temperature of the amine(s) in a reactor having a reaction space which is essentially rotationally symmetric to the direction of flow. The flow fate, averaged over the cross-section, of the reaction mixture along the axis of the essentially rotationally symmetric reaction space in the section of the reaction space in which the conversion of the amine groups into isocyanate groups is between 4 and 80% is not more than 8 m/sec. The flow rate averaged over the cross-section of the reaction mixture along the axis of the essentially rotationally symmetric reaction space in the section of the reaction space in which the conversion of the amine groups into isocyanate groups is 4 to 80% is always below the flow rate averaged over the cross-section at the start of this section.
1. A process for the production of an aromatic isocyanate comprising
a) combining at least one aromatic primary amine with phosgene in the gas phase at a temperature above the boiling temperature of the amine to form a reaction mixture,
b) reacting the reaction mixture in a reactor comprising a reaction space which is essentially rotationally symmetric to direction of flow of the reaction mixture in which
(i) flow rate, averaged over cross-section of the reactor, of the reaction mixture along the axis of the essentially rotationally symmetric reaction space in a section of the reaction space in which conversion of amine groups in the amine into isocyanate groups is from 4 to 80% complete is not more than 8 m/s and
(ii) the flow rate, averaged over the cross-section, of the reaction mixture along the axis of the essentially rotationally symmetric reaction space in the section of the reaction space in which the conversion of the amine groups into isocyanate groups is between 4 and 80% is always lower than a flow rate averaged over the cross-section at the start of this section,
wherein the reaction space in the section of the reaction space in which the conversion of the arsine groups into isocyanate groups is between 4 and 80% has a widened flowed-through cross-sectional area of the reaction space.
2. The process of claim 1 wherein the conical widening has an expanding haft-angle of ≦6°.
3. The process of claim 1 wherein the conical widening has an expanding half-angle of ≦3.5°.
4. The process of claim 1 wherein the conical widening has an expanding half-angle of ≦2°.
5. The process of claim 1 in which after the section of the reaction space in which the conversion of the amine groups into isocyanate groups is between 4 and 80% the reactor has an essentially rotationally symmetric reaction space with a constant and/or widening flowed-through cross-sectional area.
6. The process of claim 1 in which the mixing and the reacting are carried out isothermally or at least partly adiabatically.
7. The process of claim in which the essentially rotationally symmetric reaction space has at least one zone in which at least one liquid is injected for discontinuation of the reaction.
8. The process of claim 7 in which the cross-sectional area of the at least one zone in which at least one liquid is injected for discontinuation of the reaction is equally as large or larger than the cross-sectional area of the reaction space in which the reaction takes place.
9. The process of claim 1 in which the phosgene and the amine are fed to the reaction space in gaseous form using a jet mixer.
10. The process of claim 1 in which an amine-containing or phosgene-containing stream fed into the reaction space is fed to the reaction space at an average flow rate ratio of from 2 to 12.
11. The process of claim 9 in which the stream containing the amine enters into the reaction space at a higher average flow rate than the stream containing the phosgene.
12. The process of claim 1 in which the amine is a diamine.
13. The process of claim 1 in which the amine is 2,4-toluenediamine, 2,6-toluenediamine or a mixture thereof.
14. The process of claim 1 in which the reactor has a throughput capacity of >1 t of amines/h.