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:
Jul. 21, 2020

Filed:

Oct. 12, 2017
Applicant:

Johnson Matthey Davy Technologies Limited, London, GB;

Inventors:

Adrian Lord, London, GB;

Martin Smidt, London, GB;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 29/17 (2006.01); C07C 29/36 (2006.01); C07C 29/80 (2006.01); C07C 31/125 (2006.01); C07C 45/73 (2006.01); C07C 29/38 (2006.01); C07C 29/141 (2006.01); C07C 45/66 (2006.01);
U.S. Cl.
CPC ...
C07C 29/17 (2013.01); C07C 29/141 (2013.01); C07C 29/36 (2013.01); C07C 29/38 (2013.01); C07C 29/80 (2013.01); C07C 31/125 (2013.01); C07C 45/66 (2013.01); C07C 45/73 (2013.01);
Abstract

A process for the production of 2-alkylalkanol from an aldehyde is disclosed. The process comprises the steps of: feeding aldehyde to a reactor () operated under condensation and dehydration conditions such that reaction occurs and an unsaturated aldehyde is produced; recovering a stream from the reactor () comprising the unsaturated aldehyde and feeding said stream to a first hydrogenation reactor () operated under conditions such that at least some of the unsaturated aldehyde is converted to 2-alkylalkanol; recovering the stream from the first hydrogenation reactor () comprising the 2-alkylalkanol, one or more of unreacted acrolein, alkylalkenol and alkylalkanal and heavies; passing the stream recovered from the first hydrogenation reactor () to a first distillation zone () where at least some of the heavies are separated from the stream; recovering a stream from the first distillation zone () comprising the 2-alkylalkanol, one or more of unreacted acrolein, alkylalkenol and alkylalkanal, said stream having a reduced heavies content when compared to the stream fed to the first distillation zone (), and feeding said stream to a second hydrogenation reactor () operated under conditions such that at least one of the unreacted acrolein, alkylalkenol and alkylalkanal are converted to 2-alkylalkanol; and recovering a stream from the second hydrogenation reactor () comprising an increased 2-alkylalkanol content compared to the stream fed to the second hydrogenation reactor ().


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