Method for purifying contaminated gaseous hydrogen chloride

Patent metadata

Field	Value
Publication number	US-10179735-B2
Application number	US-201615527141-A
Country	US
Kind code	B2
Filing date	Jan 26, 2016
Priority date	Jan 28, 2015
Publication date	Jan 15, 2019
Grant date	Jan 15, 2019

Abstract

Impure gaseous hydrogen chloride from organochlorosilane hydrolysis is freed of impurities by first scrubbing with an organochlorosilane, which may be the same or different from the organochlorosilane(s) hydrolyzed, and then further scrubbing with chloromethane. The purified gaseous hydrogen chloride is preferably used in chlorosilane synthesis.

First claim

The invention claimed is:

1. A process for purifying contaminated gaseous hydrogen chloride containing water, organochlorosilane A and/or hydrolysis products thereof, comprising scrubbing the contaminated gaseous hydrogen chloride with a liquid organochlorosilane B to form a partially decontaminated gaseous hydrogen chloride, and after the scrubbing with organochlorosilane B, scrubbing the partially decontaminated gaseous hydrogen chloride with liquid chloromethane, wherein organochlorosilanes A and B comprise organochlorosilanes of the formula
R a SiCl 4-a (I)
where
the radicals R are identical or different radicals selected from among hydrogen and unsubstituted and substituted C 1 -C 18 hydrocarbon radicals and
a is 0, 1, 2 or 3,
with the proviso that at least 10 mol % of the radicals R are hydrocarbon radicals.

2. The process of claim 1 , wherein the gaseous hydrogen chloride originates from the hydrolysis of an organochlorosilane A.

3. The process of claim 1 , wherein organochlorosilane A is selected from the group consisting of dimethyldichlorosilane, trimethylchlorosilane, methyltrichlorosilane and mixtures thereof.

4. The process of claim 1 , wherein organochlorosilane A and organochlorosilane B are identical.

5. The process of claim 2 , wherein organochlorosilane A and organochlorosilane B are identical.

6. The process of claim 3 , wherein organochlorosilane A and organochlorosilane B are identical.

7. The process of claim 1 , wherein at least 10 times the stoichiometric amount of organochlorosilane B required for hydrolyzing water contained in the contaminated gaseous hydrogen chloride is employed for scrubbing.

8. The process of claim 1 , wherein scrubbing of the hydrogen chloride using organochlorosilane B is carried out at a temperature in the range of from 0° C. to 50° C.

9. The process of claim 1 , wherein the temperature during scrubbing with liquid chloromethane is from −15° C. to −55° C.

10. The process of claim 1 , wherein the purified hydrogen chloride is employed for preparing chloromethane.

11. The process of claim 1 , wherein a purified, scrubbed gaseous HCl fraction from the second scrubbing with chloromethane is diluted with further chlormethane and input into a reactor for producing chloromethane.

Assignees

• Wacker Chemie Ag

Inventors

• Mautner Konrad

Classifications

• C01B7/0731

  by extraction · CPC title

• C01B7/0706 Primary

  of hydrogen chloride · CPC title

• C01B2210/0003

  Chemical processing · CPC title

• C01B7/0725

  by active carbon · CPC title

• C08G77/32

  Post-polymerisation treatment · CPC title