Method for producing isocyanate-organosilanes
Isocyanatosilanes are prepared by themolyzing carbamatosilanes in a fluidized bed reactor containing fluidized solid particles. The process substantially avoids the deposition of solid reaction by products in the reactor.
1. A process for preparing isocyanatoorganosilanes, comprising thermolyzing at least one carbamatoorganosilane in the presence of fluidized solid particles.
2. The process of claim 1 , wherein isocyanatoorganosilanes of the formula (1) are prepared
R 2 R 3 R 4 Si—R 1 —N═C═O (1),
where
R is a monovalent C 1 -C 10 -alkyl radical,
R 1 is a divalent C 1 -C 6 -hydrocarbon radical and
R 2 , R 3 and R 4 are in each case independently of one another, a methyl, ethyl, n-propyl, isopropyl, methoxy, ethoxy, n-propoxy or isopropoxy radical, by thermolyzing carbamatoorganosilane of the formula (2)
R 2 R 3 R 4 Si—R 1 —NH—CO—OR (2),
in the presence of fluidized solid particles.
3. The process of claim 1 , wherein thermolyzing takes place in the presence of a catalyst.
4. The process of claim 2 , wherein thermolyzing takes place in the presence of a catalyst.
5. The process of claim 1 , wherein the solid particles have a size between 1 10−6 m and 1 10−2 m.
6. The process of claim 2 , wherein the solid particles have a size between 1 10−6 m and 1 10−2 m.
7. The process of claim 1 , wherein 1% to 100% of the fluidized solid particles consist of a catalyst or a combination of a plurality of heterogeneous catalysts.
8. The process of claim 2 , wherein 1% to 100% of the fluidized solid particles consist of a catalyst or a combination of a plurality of heterogeneous catalysts.
9. The process of claim 1 , wherein the starting material is introduced into the reaction system via atomization.
10. The process of claim 2 , wherein the starting material is introduced into the reaction system via atomization.
11. The process of claim 1 , wherein at least one of the fluidized solid particles, the catalyst, precursor compounds of the catalyst, or fluidized solid particles are fed as solution, sol, gel, emulsion, suspension, melt, vapor or solid to the reaction system, batchwise or continuously, mixed with the starting material or separately, at one or more points of the reaction system.
12. The process of claim 1 , wherein energy is fed to at least one of the reaction system or the fluidized particles, by steam, thermal oil, liquid or vaporous synthetic heat carriers, liquid salt mixtures, liquid metal alloys, hot gases, electrical resistance heating or microwave heating.
13. The process of claim 1 , wherein, batchwise or continuously, fresh particles and/or catalyst are fed, a corresponding fraction of used particles is removed from the reaction system.
14. The process of claim 2 , wherein, batchwise or continuously, fresh particles and/or catalyst are fed, a corresponding fraction of used particles is removed from the reaction system.
15. The process of claim 9 , wherein, batchwise or continuously, fresh particles and/or catalyst are fed, a corresponding fraction of used particles is removed from the reaction system.
16. The process of claim 1 , wherein the effluent stream from the reactor comprising the crude products is passed into one or more post-reactors.
17. The process of claim 2 , wherein the effluent stream from the reactor comprising the crude products is passed into one or more post-reactors.
18. The process of claim 8 , wherein the effluent stream from the reactor comprising the crude products is passed into one or more post-reactors.
19. The process of claim 14 , wherein the effluent stream from the reactor comprising the crude products is passed into one or more post-reactors.
20. The process of claim 1 , wherein said fluidized particles are heated by irradiation with microwave energy.