# US 11,299,592 B2 · Method for producing organopolysiloxane resins

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- Number: US 11,299,592 B2
- Document ID: US11299592B2
- Status: Granted
- Kind: B2
- Application number: 16/613,955
- Filed: 2017-05-16
- Published: 2021-10-28
- Granted: 2022-04-12
- Earliest claimed: 2017-05-16
- Assignees: Wacker Chemie AG
- Applicants: Wacker Chemie AG
- Inventors: Klaus Kaeppler; Elfriede Thumser
- Web page: https://patentgrep.com/patent/US11299592B2

## CPC

- C08G 77/04: Polysiloxanes
- C08G 77/06: Preparatory processes
- C08G: MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS

## Abstract

Silicone resins are reproducibly prepared in a four step process in which alcohol recovered in a second step is recycled to the first step, and an aqueous phase recovered in the fourth step contains very little HCl, alcohol, or organopolysiloxane, and can be directed to waste treatment without any prior processing.

## Claims

### Claim 1

A process for preparing organopolysiloxane resins, comprising:
in a first continuous step, reacting organochlorosilanes in an upright circulation tube reactor which, via a heating assembly on an ascending part of the tube reactor regulates the temperature in the circulation tube reactor, with an aqueous alcohol comprising 0.10 to 0.75 mol of water per mole of hydrolyzable chlorine and 0.3 to 1.0 mol of alcohol per mole of hydrolyzable chlorine, where the molar ratio of water to alcohol is 0.10 to 2.5, and withdrawing a product mixture from the reactor, wherein the ratios of water and alcohol of the aqueous alcohol to organochlorosilanes is regulated within the previous limits such that the fraction of the aqueous alcohol phase in the product mixture is from 0.1-50 wt %, and wherein the temperature of the reaction medium is provided to the heating assembly as a regulated variable, compared with a fixed temperature in the range of 20-60° C. as a control variable, and is regulated with an accuracy of ±5° C. with respect to the fixed temperature of the control variable, and wherein the aqueous alcohol used optionally comprises up to 31 wt % of dissolved HCl and up to 5 wt % of water-insoluble organic solvents;
in a second step, adding to the reaction mixture obtained in the first step, water-insoluble organic solvent having a density of below 0.95 kg/l and metering in water in amounts of 1.5 to 5 mol of water and 0.1 to 0.5 mol of alcohol per mole of organochlorosilane, and, after the end of the metered additions in the second step, separating an alcoholic HCl phase from a siloxane phase;
in a third step, metering in water in amounts of 5 to 200 mol of water per mole of organochlorosilane to the siloxane phase of the second step, and optionally adding water-insoluble organic solvent having a density of below 0.95 kg/l; and
in a fourth step, after the end of the metering of water in the third step, separating an aqueous phase from the siloxane phase.

### Claim 2 (depends on 1)

The process of claim 1, wherein in the second step, water-insoluble organic solvent is metered in amounts of 0.5 to 50 mol, based on 1 mole of Si component.

### Claim 3 (depends on 1)

The process of claim 1, wherein in the second step, water-insoluble organic solvent is metered in amounts of 1 to 30 mol, based on 1 mole of organochlorosilane.