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:
Oct. 11, 2016

Filed:

Feb. 02, 2016
Applicant:

Air Products and Chemicals, Inc., Allentown, PA (US);

Inventors:

Rajiv Krishan Agarwal, Malvern, PA (US);

Sai-Hong Andrew Lo, Allentown, PA (US);

Howard Paul Withers, Jr., Breinigsville, PA (US);

Joseph T. Sluzevich, Frackville, PA (US);

James Joseph Hart, Fogelsville, PA (US);

Assignee:

Air Products and Chemicals, Inc., Allentown, PA (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07F 7/10 (2006.01); C01B 21/087 (2006.01); B01J 8/24 (2006.01); B01J 8/00 (2006.01); B01J 8/10 (2006.01); B01J 8/02 (2006.01);
U.S. Cl.
CPC ...
C01B 21/087 (2013.01); B01J 8/0015 (2013.01); B01J 8/02 (2013.01); B01J 8/10 (2013.01); B01J 8/24 (2013.01); B01J 2208/00761 (2013.01); B01J 2208/00823 (2013.01);
Abstract

The method described herein provides a method for preparing trisilylamine. In one aspect, the method comprises: providing a reaction mixture of trisilylamine and monochlorosilane into a reactor wherein the reaction mixture is at a temperature and pressure sufficient to provide trisilylamine in a liquid phase wherein the reaction mixture is substantially free of an added solvent; contacting the reaction mixture with ammonia to provide a crude mixture comprising trisilylamine and an ammonium chloride solid wherein monochlorosilane is in stoichiometric excess in relation to ammonia; purifiying the crude mixture to provide trisilylamine wherein the trisilyamine is produced at purity level of 90% or greater; and optionally removing the ammonium chloride solid from the reactor.


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