Method for producing organopolysiloxanes

Patent metadata

Field	Value
Publication number	US-9988496-B2
Application number	US-201615535453-A
Country	US
Kind code	B2
Filing date	Jul 21, 2016
Priority date	Jul 30, 2015
Publication date	Jun 5, 2018
Grant date	Jun 5, 2018

Abstract

Highly condensed silicon resins are obtained by a three step continuous procedure without the use of organic solvent, by preliminarily forming a partial alkoxylate by reacting a chlorosilane with alcohol containing no or a minimal amount of water, feeding the partial alkoxylate to a reaction column to form a silicone resin of low degree of condensation, and further condensing the silicone resin intermediate thus formed to produce a silicone resin product.

First claim

The invention claimed is:

1. A fully continuous process for preparing branched organopolysiloxanes, comprising:
a) in a first step, continuously reacting at least one chlorosilane with alcohol in a preliminary reactor to produce a partial alkoxylate, wherein
a)i) 0.1 to 2.0 mol of alcohol is reacted per mole of hydrolyzable chlorine, and
a)ii)) the alcohol contains not more than 5% by weight of water, and

b) in a second step, transferring the partial alkoxylate obtained in the first step into a first reaction unit comprising a reaction column, and continuously reacting the partial alkoxylate with
b)i) alcohol and water, or
b)ii) alcohol, water and at least one further chlorosilane which differs from the chlorosilane(s) of the first step by being less volatile, and/or having a lower reactivity, to produce an incompletely condensed silicone resin intermediate, and either

c) in a third step, transferring the silicone resin intermediate from the second step into a second reaction unit comprising at least one of a continuous loop reactor, a stirred batchwise reactor with continuous feed and drain, or a stirred tank cascade connected in a continuous system, and reacting the silicone resin intermediate with
c)i) alcohol and water in the presence of catalytic traces of hydrogen chloride, or
c)ii) alcohol and water in the presence of catalytic traces of hydrogen chloride, and with addition of further alkoxy- and/or hydroxy-functional organopolysiloxanes or alkoxy- and/or hydroxy-functional silanes, and further condensing to produce a branched organopolysiloxane end product, or having a targeted level of condensation, or

d) in a third step, transferring the silicone resin intermediate from the second step into a second reaction unit comprising a stirred batchwise reactor and further condensing the silicone resin intermediate with,
d)i) alcohol and water in the presence of catalytic traces of hydrogen chloride, or
d)ii) alcohol and water in the presence of catalytic traces of hydrogen chloride, and further alkoxy- and/or hydroxy-functional organopolysiloxanes or alkoxy- and/or hydroxy-functional silanes,

to produce a branched organopolysiloxane end product with a targeted level of condensation, with the proviso that no organic solvent other than the alcohol reacted is used over the entire process, the alcohol comprising a single alcohol or of a mixture of at least two different alcohols.

2. The process of claim 1 , wherein the process is a continuous process.

3. The process of claim 1 , wherein the alcohol in step a) contains not more than 4% by weight of water.

4. The process of claim 1 , further comprising:
condensing a hydrochloric acid-containing tops distillate of the reaction column of step b) and returning a condensate thusly obtained to the reaction column just below the feed point of the reaction mixture from the preliminary reactor to the reaction column, such that it does not reach the bottom of the reaction column, thereby removing the hydrochloric acid released in the reaction column completely from the reaction system, and obtaining the silicone resin intermediate from the bottom of the reaction column without further workup with a residual hydrochloric acid content of less than 100 ppm.

Assignees

• Wacker Chemie Ag

Inventors

• Sandmeyer Frank
• Loessel Georg
• Prasse Marko

Classifications

• C08G77/18

  to alkoxy or aryloxy groups · CPC title

• C08G77/16 Primary

  to hydroxy groups · CPC title

• C08G77/08

  characterised by the catalysts used · CPC title

• C08G77/06 Primary

  Preparatory processes · CPC title