The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Aug. 20, 2019

Filed:

Feb. 23, 2016
Applicant:

Schmid Silicon Technology Gmbh, Freudenstadt, DE;

Inventors:

Christian Schmid, Freudenstadt, DE;

Jochem Hahn, Rottenburg, DE;

Christian Andreas Fuhrmann, Haigerloch-Weildorf, DE;

Assignee:

Schmid Silicon Technology GmbH, Freudenstadt, DE;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 19/24 (2006.01); C01B 3/22 (2006.01); C07C 253/00 (2006.01); B01J 8/04 (2006.01); B01D 3/00 (2006.01); B01D 3/20 (2006.01); C01B 33/04 (2006.01); C01B 33/107 (2006.01); B01J 8/06 (2006.01);
U.S. Cl.
CPC ...
B01J 8/0449 (2013.01); B01D 3/009 (2013.01); B01D 3/20 (2013.01); B01J 8/065 (2013.01); C01B 33/043 (2013.01); C01B 33/046 (2013.01); C01B 33/1071 (2013.01); C01B 33/10773 (2013.01); C01B 33/10778 (2013.01); B01J 2208/06 (2013.01); Y02P 20/127 (2015.11);
Abstract

A column includes a column head, a column sump and a tube-shaped column shell disposed therebetween, two or more reaction zones lying above each other which each accommodate a catalyst bed, in which catalyst beds chlorosilanes disproportionate into low-boiling silanes, which form an ascending stream of gas, and also into high-boiling silanes which form a downwardly directed stream of liquid, within the column shell and along the column axis, two or more rectificative separation zones, the reaction zones and the separation zones alternate along the column axis, the separation zones are configured such that the stream of gas and the stream of liquid meet in the separation zones, and the reaction zones are configured such that the downwardly directed stream of liquid is led through the catalyst beds, whereas the upwardly directed stream of gas passes the catalyst beds in spatial separation from the stream of liquid.


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