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:
Dec. 04, 2018

Filed:

Nov. 19, 2015
Applicant:

Technip E&c Limited, Milton Keynes, GB;

Inventors:

Stephen Roy Partington, East Yorkshire, GB;

Stephen James Smith, East Yorkshire, GB;

Nakul Thakar, East Yorkshire, GB;

Assignee:

Technip E&C Limited, Milton Keynes, GB;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 1/24 (2006.01); B01J 23/30 (2006.01); B01J 37/08 (2006.01); B01J 23/00 (2006.01); B01J 27/188 (2006.01); B01J 35/02 (2006.01); B01J 35/10 (2006.01); B01J 37/02 (2006.01); B01J 21/08 (2006.01);
U.S. Cl.
CPC ...
C07C 1/24 (2013.01); B01J 23/002 (2013.01); B01J 23/30 (2013.01); B01J 27/188 (2013.01); B01J 35/023 (2013.01); B01J 35/1019 (2013.01); B01J 35/1042 (2013.01); B01J 35/1061 (2013.01); B01J 37/0201 (2013.01); B01J 37/08 (2013.01); B01J 21/08 (2013.01); B01J 35/1076 (2013.01); B01J 2523/00 (2013.01); C07C 2521/08 (2013.01); C07C 2523/30 (2013.01); Y02P 20/52 (2015.11);
Abstract

The present invention provides a process for the preparation of ethene by vapor phase chemical dehydration of a feed-stream comprising ethanol and optionally water and/or ethoxy ethane, said process comprising contacting a dried supported heteropolyacid catalyst in a reactor with the feed-stream having a feed temperature of at least 200° C.; wherein before the supported heteropolyacid catalyst is contacted with the feed-stream having a feed temperature of at least 200° C., the process is initiated by: (i) drying a supported heteropolyacid catalyst in a reactor under a stream of inert gas having a feed temperature of from above 100° C. to 200° C.; and (ii) contacting the dried supported heteropolyacid catalyst with an ethanol-containing vapor stream having a feed temperature of from above 100° C. to 160° C.


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