Method for continuously producing low-alkoxy branched siloxanes

Patent metadata

Field	Value
Publication number	US-11203606-B2
Application number	US-201716330563-A
Country	US
Kind code	B2
Filing date	Feb 1, 2017
Priority date	Feb 1, 2017
Publication date	Dec 21, 2021
Grant date	Dec 21, 2021

Abstract

Branched organopolysiloxanes and organopolysiloxanes with low alkoxy content are produced in a first reaction unit by continuous feed of organohalosilanes and alcohol to a reaction vessel surmounted by a distillation column, the vessel containing an excess of water relative to the halogen content of the organohalosilanes. A second reaction unit for removing volatiles from the product from the first reaction unit is also preferably employed.

First claim

The invention claimed is:

1. A continuous method for producing organosiloxanes (O) by reacting at least one silicon compound 1 of formula 1
R n SiHal 4-n   (1),

and at least one silicon compound 2, which comprise silicon compounds of formula 2a, silicon compounds of formula 2b, or mixtures of silicon compounds of formulae 2a and 2b
R 1 3 SiHal  (2a),

R 1 3 Si—O—SiR 1 3   (2b),

wherein
R is hydrogen or a C 1 -C 12 hydrocarbon radical,
R 1 is hydrogen or a C 1 -C 7 hydrocarbon radical,
Hal is fluorine, chlorine, bromine or iodine, and
n has a value of 0 or 1,
with alcohol and water in the presence of organosiloxane (O) in a first reaction unit comprising a distillation column and a vessel (V) containing organosiloxane (O) arranged thereunder, wherein the content of the vessel is heated to boiling under reflux, the at least one silicon compound 1 is introduced into the column above the lower end of the column, the at least one silicon compound 2 is introduced into the vessel (V), hydrogen halide formed by the reaction is removed by means of the distillation column, and organosiloxane (O) is constantly drawn off from the vessel (V) to an extent to which is it formed, wherein the at least one silicon compound 1, the at least one silicon compound 2, alcohol and water are constantly supplied to the reaction unit in such amounts that there is always more water contained in the first reaction unit than can be consumed by the at least one silicon compound 1 and at least one silicon compound 2 supplied to the first reaction unit.

2. The method of claim 1 , wherein silicon compounds 1 and 2, alcohol and water are introduced into the first reaction unit in such amounts that there is at least 3 wt % of water present in the vessel (V), based on the total weight of the liquid phase in the vessel (V).

3. The method of claim 1 , wherein silicon compounds 1 and 2, alcohol and water are introduced into the first reaction unit in such amounts that there is at least 20 wt % of alcohol present in the vessel (V), based on the total weight of the liquid phase in the vessel (V).

4. The method of claim 2 , wherein silicon compounds 1 and 2, alcohol and water are introduced into the first reaction unit in such amounts that there is at least 20 wt % of alcohol present in the vessel (V), based on the total weight of the liquid phase in the vessel (V).

5. The method of claim 1 , wherein the C 1 -C 7 or C 1 -C 12 hydrocarbon radicals R and R 1 are selected from the group consisting of methyl, ethyl, vinyl, n-propyl, i-propyl, n-butyl, i-butyl, n-pentyl, i-pentyl, n-hexyl, i-hexyl, cyclohexyl, n-heptyl, n-octyl, i-octyl, phenyl, tolyl radicals, and mixtures thereof.

6. The method of claim 1 , wherein the halogen atom Hal is chlorine.

7. The method of claim 1 , wherein additionally silicon compound 3
R 1 2 SiHal 2   (3),

is introduced into the vessel (V) or into the column above a lower end of the column.

8. The method of claim 1 , wherein the alcohol corresponds to the formula R″OH, in which R″ is a monovalent aliphatic hydrocarbon radical having 1 to 8 carbon atoms.

9. The method of claim 1 , wherein the mixture comprising the organosiloxane (O) obtained from the first reaction unit is passed into a second reaction unit and heated there to a temperature at which volatile constituents are completely or partially removed from the mixture, wherein the volatile constituents are recycled from the second reaction unit back into the first reaction unit, and organosiloxane (O) is constantly drawn off from the bottom of the second reaction unit to the extent to which is it formed.

10. The method of claim 1 , wherein the amount of hydrogen halide dissolved in a liquid phase of vessel (V) is 40,000 to 100,000 ppm, based on the total weight of the liquid phase in the vessel (V) of the first reaction unit.

11. The method of claim 1 , wherein the concentration of hydrogen halide is controlled by introducing an inert gas into the vessel (V) of the first reaction unit.

12. The method of claim 9 , wherein the concentration of hydrogen halide is controlled by introducing an inert gas into the column bottom of the second reaction unit.

13. The method of claim 9 , wherein a phase separation unit is positioned between the first and second reaction unit.

Assignees

• Wacker Chemie Ag

Inventors

• Dörrich Steffen
• Weidner Richard

Classifications

• C08G77/06 Primary

  Preparatory processes · CPC title

• C08G77/70

  Siloxanes defined by use of the MDTQ nomenclature · CPC title

• C07F7/0872 Primary

  Preparation and treatment thereof · CPC title

• B01J2219/00033

  Continuous processes · CPC title

• B01J2219/00306

  Reactor vessels in a multiple arrangement · CPC title