Preparation of isocyanatosilanes
There is provided herein a method and an apparatus for producing an isocyanatoorganosilane which method includes feeding a carbamatoorganosilane to a cracking device where it is thermally dissociated into a reaction product mixture comprising isocyanatoorganosilane, alcohol, and heavies, followed by separating the mixture in a distillation column of two parts and collecting the isocyanatoorganosilane from the distillation column via a side stream having a predetermined location between the top and bottom parts of the column; and wherein the distillation column is configured to have a ratio of the length of the bottom part of the distillation column to the length of the top part of the distillation column which is effective to provide a side stream having a high purity and high weight percent of isocyanatoorganosilane.
1. A method for producing a high purity isocyanatoorganosilane of the general formula (I)
R 2 R 3 R 4 Si—R 1 —N═C═O (I),
comprising:
(A) feeding a carbamatoorganosilane of the general formula (II)
R 2 R 3 R 4 Si—R 1 —NH—CO—OR (II),
where
R is a monovalent alkyl radical containing from 1 to 10 carbon atoms or an aromatic group of from 6 to 12 carbon atoms,
R 1 is a divalent hydrocarbon radical containing from 1 to about 6 carbon atoms, and R 2 , R 3 and
R 4 are independently selected from the group consisting of methyl, ethyl, n-propyl, isopropyl, methoxy, ethoxy, n-propoxy and isopropoxy radicals, to a cracking device;
(B) heating the fed carbamatoorganosilane to a temperature and pressure effective to thermally dissociate the carbamatoorganosilane to a reaction product mixture comprising isocyanatoorganosilane, alcohol, unreacted carbamatoorganosilane, and heavies,
(C) separating isocyanatoorganosilane having a purity greater than about 90% from the rest of the reaction product mixture in a distillation column having a bottom part and a top part by conveying the isocyanatoorganosilane and alcohol in the reaction mixture of step (B) as a vapor mixture to the top part of the distillation column and removing the alcohol from the vapor mixture and condensing the isocyanatoorganosilane into the liquid phase by a partial condenser positioned above the top part of the distillation column, and reintroducing the liquid phase into the top part of the distillation column to provide the separated isocyanatoorganosilane having a purity greater than about 90%, and
(D) collecting the isocyanatoorganosilane having greater than about 90% purity through a side stream which is located between the bottom part of the distillation column and the top part of the distillation column and
wherein the ratio of the length of the bottom part of the distillation column to the length of the top part of the distillation column is from 2:1 to about 10:1.
2. The method of claim 1 , wherein the ratio of the bottom part of the distillation column to the length of the top part of the distillation column is from about 3:1 to about 5:1.
3. The method of claim 1 , where the method is a continuous method.
4. The method of claim 1 , where the carbamatoorganosilane is such that R is a monovalent alkyl radical containing from 1 to about 3 carbon atoms, R 1 is a divalent hydrocarbon radical containing from 1 to about 3 carbon atoms, and R 2 , R 3 and R 4 are independently selected from the group consisting of methyl, ethyl, methoxy, and ethoxy radicals.
5. The method of claim 1 , where the carbamatoorganosilane is selected from the group consisting of methyl N-(3-trimethoxysilypropyl) carbamate, ethyl N-(3-triethoxysilypropyl) carbamate and combinations thereof.
6. The method of claim 1 wherein the temperature and pressure effective to thermally dissociate the carbamatoorganosilane are from about 150° C. to about 300° C. and from about 2 to about 500 mbar.
7. The method of claim 1 , where the isocyanatoorganosilane is selected from the group consisting of 3-isocyanatopropyltrimethoxysilane, 3-isocyanatopropyltriethoxysilane and combinations thereof.
8. The method of claim 1 , wherein step (B) further comprises employing a catalyst.
9. The method of claim 1 wherein step (B) further comprises adding a solvent to the cracking device.
10. The method of claim 1 , further comprising removing the heavies from the cracking device.
11. The method of claim 1 , wherein the purity of the isocyanatoorganosilane which is separated in step (C) and collected in step (D) is greater than about 92%.
12. The method of claim 1 , wherein the yield of isocyanatoorganosilane collected in step (D) is greater than or equal to about 60% based on the weight of collected isocyanatoorganosilane relative to the weight of fed carbamatoorganosilane.
13. The method of claim 1 , wherein the yield of isocyanatoorganosilane collected in step (D) is greater than or equal to about 65% based on the weight of collected isocyanatoorganosilane relative to the weight of fed carbamatoorganosilane.
14. The method of claim 1 , wherein the side stream of step (D) is located at an exit point from the bottom part of the distillation column.
15. The method of claim 1 , wherein the isocyanatoorganosilane having greater than about 90% purity which is collected through a side stream in step (D) is removed from the distillation column at a rate that provides for a hydrodynamically stable system.
16. The method of claim 1 , wherein the distillation column is a single distillation column.