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. 20, 2016

Filed:

Sep. 17, 2015
Applicant:

Total Research & Technology Feluy, Seneffe (Feluy), BE;

Inventors:

Cindy Adam, Wierde, BE;

Delphine Minoux, Nivelles, BE;

Nikolai Nesterenko, Nivelles, BE;

Sander Van Donk, Sainte-Adresse, FR;

Jean-Pierre Dath, Beloeil, BE;

Assignee:

TOTAL RESEARCH & TECHNOLOGY FELUY, Seneffe (Feluy), BE;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 1/22 (2006.01); C07C 1/24 (2006.01); C07C 4/06 (2006.01); C07C 6/04 (2006.01); C10G 3/00 (2006.01); C12P 5/02 (2006.01); C12P 7/16 (2006.01); C08F 10/02 (2006.01); B01J 29/40 (2006.01);
U.S. Cl.
CPC ...
C07C 1/24 (2013.01); C07C 1/22 (2013.01); C07C 4/06 (2013.01); C07C 6/04 (2013.01); C08F 10/02 (2013.01); C10G 3/42 (2013.01); C10G 3/44 (2013.01); C10G 3/49 (2013.01); C12P 5/026 (2013.01); C12P 7/16 (2013.01); B01J 29/40 (2013.01); B01J 2229/42 (2013.01); C07C 2529/40 (2013.01); C10G 2300/1014 (2013.01); C10G 2300/1022 (2013.01); C10G 2300/201 (2013.01); C10G 2300/4081 (2013.01); C10G 2400/20 (2013.01); C10G 2400/22 (2013.01); Y02E 50/10 (2013.01); Y02P 20/52 (2015.11);
Abstract

A process for the conversion of an alcohol mixture to make propylene may include introducing into a reactor a stream that includes the alcohol mixture. The alcohol mixture may include 20 to 100 weight percent isobutanol. The process may include contacting the stream with a single catalyst at a temperature above 450° C. in the reactor at conditions effective to dehydrate the isobutanol, forming Colefins, and to catalytically crack the Colefins. The single catalyst may be an acid catalyst adapted to cause both the dehydration and the catalytic cracking. The process may include recovering from the reactor an effluent that includes ethylene, propylene, water, and various hydrocarbons. The process may include fractionating the effluent to produce an ethylene stream, a propylene stream, a fraction of hydrocarbons having 4 carbon atoms or more, and water.


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