Method and apparatus for the separation by distillation of a three- or multi-component mixture

Patent metadata

Field	Value
Publication number	US-10076713-B2
Application number	US-201414786269-A
Country	US
Kind code	B2
Filing date	Mar 26, 2014
Priority date	Apr 22, 2013
Publication date	Sep 18, 2018
Grant date	Sep 18, 2018

Abstract

A method and apparatus for distillative separation of a mixture comprising three or more components including at least one low boiler, at least one medium boiler, and at least one high boiler, the method comprising feeding the mixture of three or more components to a first distillation column, removing the at least one high boiler as a bottom fraction from the first distillation column, feeding a top fraction of the first distillation column to a second distillation column, removing the at least one medium boiler via a sidestream takeoff from the second distillation column, removing the at least one low boiler as a top fraction from the second distillation column, and feeding a bottom takeoff stream from the second distillation column to the first distillation column as a reflux, wherein the first and the second distillation columns have vertical dividing walls.

First claim

The invention claimed is:

1. An apparatus for distillative separation of a mixture comprising three or more components, the apparatus comprising:
a first distillation column coupled to a second distillation column to allow material transfer;
at least one vapor tube of the first distillation column connected to a bottom of the second distillation column such that vapor(s) from the first distillation column are communicatively connected to the bottom of the second distillation column; and
at least one bottom takeoff stream of the second distillation column connected to a reflux section of the first distillation column,
wherein the first and the second distillation columns both have vertical dividing walls which in the first distillation column extend to a top end of the interior of the column, and which in the second distillation column extend to a bottom end of the interior of the column, the first distillation column having a combined lower stripping section and the second distillation column having a combined upper recitifying section, wherein the second distillation column has one or more sidestream takeoffs below a top takeoff stream and above the at least one bottom takeoff stream, and wherein at least the first distillation column comprises one or more evaporators for evaporating a liquid bottom stream.

2. The apparatus of claim 1 , wherein the first and the second distillation columns have 1-200 theoretical plates.

3. The apparatus of claim 2 , wherein both the first distillation column and the second distillation column comprise one or more evaporators for evaporating liquid bottom stream.

4. The apparatus of claim 1 , wherein at least the second distillation column comprises one or more condensers for condensing vapor stream(s).

5. The apparatus of claim 2 , wherein at least the second distillation column comprises one or more condensers for condensing vapor stream(s).

6. A method for distillative separation of a mixture comprising three or more components including at least one low boiler, at least one medium boiler, and at least one high boiler in an apparatus of claim 1 , the method comprising:
feeding the mixture of three or more components to the first distillation column,
removing the at least one high boiler as a bottom fraction from the first distillation column;
feeding a top fraction of the first distillation column to the bottom of the second distillation column;
removing the at least one medium boiler via a sidestream takeoff from the second distillation column;
removing the at least one low boiler as a top fraction from the second distillation column; and
feeding a bottom takeoff stream from the second distillation column to the first distillation column as a reflux.

7. The method of claim 6 , further comprising operating the first and the second distillation columns at an offgas pressure of from about −1 to 10 bar and a boiling temperature range of from about −20 to 200° C.

8. The method of claim 6 , wherein the first and the second distillation columns comprise one or more evaporators that utilize water vapor or thermal oil(s) of various pressure and temperature ratings as heat transfer agents.

9. The method of claim 6 , wherein the first and the second distillation columns comprise one or more condensers that utilize cooling water or cooling brine of various pressure and temperature ratings as heat transfer agents.

10. The method of claim 7 , wherein the first and the second distillation columns comprise one or more condensers that utilize cooling water or cooling brine of various pressure and temperature ratings as heat transfer agents.

11. The method of claim 6 , further comprising feeding uncondensable top stream component(s) from a first condensation stage to a second condensation stage and/or to a scrubber system.

12. The method of claim 7 , further comprising feeding uncondensable top stream component(s) from a first condensation stage to a second condensation stage and/or to a scrubber system.

13. The method of claim 6 , wherein the mixture comprising three or more components comprises chlorosilanes as the medium boiler.

14. The method of claim 7 , wherein the mixture comprising three or more components comprises chlorosilanes as the medium boiler.

Assignees

• Wacker Chemie Ag

Inventors

• Schreieder Franz
• Aigner Maximilian
• Prochaska Jan

Classifications

• C07F7/121

  Preparation or treatment not provided for in C07F7/14, C07F7/16 or C07F7/20 · CPC title

• B01D3/141 Primary

  where at least one distillation column contains at least one dividing wall · CPC title

• C07F7/12

  Organo silicon halides · CPC title