Process for preparing organopolysiloxanes

Patent metadata

Field	Value
Publication number	US-10125225-B2
Application number	US-201615537163-A
Country	US
Kind code	B2
Filing date	Jul 21, 2016
Priority date	Jul 30, 2015
Publication date	Nov 13, 2018
Grant date	Nov 13, 2018

Abstract

Multistep continuous and semicontinuous hydrolysis and condensation of chlorosilanes with alcohol containing minimal water in a column in a first step to form a silicone resin intermediate, followed by further condensation provides silicone resins in reproducible fashion substantially free of hydrogen chloride, without reactor gelatin.

First claim

The invention claimed is:

1. A fully continuous process for the production of branched organopolysiloxanes, comprising:
a) in a first step, in a column as a first reaction unit, continuously reacting at least one chlorosilane with alcohol to produce a silicone resin intermediate, wherein the reaction takes place
a)i) with alcohol and water, or
a)ii) with alcohol, water, and at least one further chlorosilane which differs from the first chlorosilane by being less volatile and having a higher boiling point than the first chlorosilane, and optionally having a lower reactivity,

wherein 0.1 to 2.0 moles alcohol are used per mole of hydrolyzable chlorine, and the alcohol contains at most 5 wt. % water, and
b) in a second step, introducing the silicone resin intermediate from the first step into a continuous loop reactor, a stirred batch reactor with continuous input and output, or a continuously connected stirring device cascade as a second reaction unit, and reacting the silicone resin intermediate,
b)i) with alcohol and water and in the presence of catalytic traces of hydrogen chloride, or
b)ii) with alcohol and water and in the presence of catalytic traces of hydrogen chloride and with addition of one or more further alkoxy- and/or hydroxy-functionalized organopolysiloxanes or alkoxy- and/or hydroxy-functionalized silanes,

to produce a branched organopolysiloxane with a targeted degree of condensation,
with the proviso that during the whole process, apart from the alcohol, no other solvent is used,
wherein the alcohol can comprise only one type of alcohol or a mixture of at least two different alcohols.

2. A partially continuous process for the production of branched organopolysiloxanes, comprising:
a) in a first step, in a column as a first reaction unit, continuously reacting at least one chlorosilane to produce a silicone resin intermediate, wherein the reaction takes place
a)i) with alcohol and water, or
a)ii) with alcohol, water, and at least one further chlorosilane which differs from the first chlorosilane by being less volatile and having a higher boiling point, and optionally having a lower reactivity,

wherein 0.1 to 2.0 moles alcohol are used per mole of hydrolyzable chlorine, and the alcohol contains at most 5 wt. % water, and
b) in a second step the silicone resin intermediate from the first step is transferred into a stirred discontinuously operated batch reactor as a second reaction unit, and therein reacting the silicone resin intermediate
b)i) with alcohol and water and in the presence of catalytic traces of hydrogen chloride, or
b)ii) with alcohol and water and in the presence of catalytic traces of hydrogen chloride and with addition of one or more further alkoxy- and/or hydroxy-functionalized organopolysiloxanes or alkoxy- and/or hydroxy-functionalized silanes,

to provide as an end product, a branched organopolysiloxane with a targeted degree of condensation,
with the proviso that during the entire process apart from the alcohol, no other solvent is employed,
wherein the alcohol can consist of only one type of alcohol or of a mixture of at least two different alcohols.

3. The process of claim 1 , wherein the alcohol in the first step contains at most 4 wt. % water.

4. The process of claim 2 , wherein the alcohol in the first step contains at most 4 wt. % water.

5. The process of claim 1 , wherein a hydrochloric acid-containing head distillate of the column of the first step is condensed and fed back onto the column a short distance below the feed point of the reaction mixture from a pre-reactor, so that it does not reach the bottom of the column and thus the hydrochloric acid liberated in the column is wholly removed from the reaction system and as a result the silicone resin intermediate in the bottom of the reaction column without further workup accumulates with less than 100 ppm residual hydrochloric acid content.

6. The process of claim 2 , wherein a hydrochloric acid-containing head distillate of the column of the first step is condensed and fed back onto the column a short distance below the feed point of the reaction mixture from a pre-reactor, so that it does not reach the bottom of the column and thus the hydrochloric acid liberated in the column is wholly removed from the reaction system and as a result the silicone resin intermediate in the bottom of the reaction column without further workup accumulates with less than 100 ppm residual hydrochloric acid content.

7. The process of claim 3 , wherein a hydrochloric acid-containing head distillate of the column of the first step is condensed and fed back onto the column a short distance below the feed point of the reaction mixture from a pre-reactor, so that it does not reach the bottom of the column and thus the hydrochloric acid liberated in the column is wholly removed from the reaction system and as a result the silicone resin intermediate in the bottom of the reaction column without further workup accumulates with less than 100 ppm residual hydrochloric acid content.

8. The process of claim 4 , wherein a hydrochloric acid-containing head distillate of the column of the first step is condensed and fed back onto the column a short distance below the feed point of the reaction mixture from a pre-reactor, so that it does not reach the bottom of the column and thus the hydrochloric acid liberated in the column is wholly removed from the reaction system and as a result the silicone resin intermediate in the bottom of the reaction column without further workup accumulates with less than 100 ppm residual hydrochloric acid content.

Assignees

• Wacker Chemie Ag

Inventors

• Sandmeyer Frank
• Loessel Georg
• Prasse Marko

Classifications

• C08G77/06 Primary

  Preparatory processes · CPC title

• C08G77/18 Primary

  to alkoxy or aryloxy groups · CPC title

• C08G77/16

  to hydroxy groups · CPC title