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:
Nov. 06, 2018

Filed:

Nov. 13, 2015
Applicant:

Abengoa Bioenergia Nuevas Tecnologias, S.a., Seville, ES;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 29/34 (2006.01); C07C 29/80 (2006.01); B01J 21/00 (2006.01); B01J 21/10 (2006.01); B01J 37/03 (2006.01); B01J 37/06 (2006.01); B01J 37/02 (2006.01); B01J 23/44 (2006.01); B01J 37/08 (2006.01); B01J 37/18 (2006.01); B01J 23/648 (2006.01); B01J 23/08 (2006.01); B01J 23/62 (2006.01); B01J 23/72 (2006.01); B01J 23/89 (2006.01); B01J 8/02 (2006.01); B01D 3/14 (2006.01); B01D 3/00 (2006.01);
U.S. Cl.
CPC ...
C07C 29/34 (2013.01); B01D 3/009 (2013.01); B01D 3/143 (2013.01); B01J 8/0278 (2013.01); B01J 21/10 (2013.01); B01J 23/08 (2013.01); B01J 23/44 (2013.01); B01J 23/62 (2013.01); B01J 23/6482 (2013.01); B01J 23/72 (2013.01); B01J 23/898 (2013.01); B01J 37/0213 (2013.01); B01J 37/0236 (2013.01); B01J 37/036 (2013.01); B01J 37/06 (2013.01); B01J 37/08 (2013.01); B01J 37/18 (2013.01); C07C 29/80 (2013.01); B01J 2208/021 (2013.01);
Abstract

The present disclosure generally relates to processes for preparation of n-butanol, n-octanol and n-decanol from a reaction mixture comprising ethanoi and n-hexanol by Guerbet condensation. In some aspects, the present disclosure relates to improvements in n-octanol and n-decanol yield and selectivity by the selection of process reaction conditions such as, but not limited to, mole ratio of n-hexanol to ethanol. The present disclosure further generally relates to integrated processes for preparation of n-butanol in a n-butanol reactor from a reaction mixture comprising ethanol and hydrogen to produce a n-butanol product stream by Geurbet condensation comprising n-butanol and n-hexanol and for preparation of n-octanol in a n-octanol reactor from a reaction mixture comprising ethanol, n-hexanol and hydrogen to produce a n-octanol product stream by Geurbet condensation comprising n-butanol, n-hexanol and n-octanol. A predominant proportion of the n-hexanol contained in the n-butanol and n-octanol product streams is isolated and recycled to the n-octanol reaction mixture. In some aspects, the present disclosure relates to improvements in n-octanol and n-butanol yield and selectivity by the selection of process reaction conditions such as, but not limited to, mole ratio of n-hexanol to ethanol and recovery and recycle of n-hexanol.


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