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:
May. 05, 2026

Filed:

Apr. 06, 2020
Applicants:

Ifp Energies Nouvelles, Rueil-Malmaison, FR;

Compagnie Générale Des Etablissements Michelin, Clermont-Ferrand, FR;

Inventors:

Frederic Augier, Rueil-Malmaison, FR;

Pierre Olivier Dreger, Rueil-Malmaison, FR;

Assignees:

IFP Energies Nouvelles, RueiI-Malmaison Cedex, FR;

Compagnie Générale des Etablissements Michelin, CIermont-Ferrand, FR;

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C07C 29/86 (2006.01); B01D 11/04 (2006.01); C07C 45/80 (2006.01);
U.S. Cl.
CPC ...
B01D 11/0426 (2013.01); B01D 11/0488 (2013.01); B01D 11/0492 (2013.01); C07C 29/86 (2013.01); C07C 45/80 (2013.01);
Abstract

The invention concerns a method for purifying a hydroalcoholic feedstock, comprising: a) a step of counter-current liquid-liquid extraction, comprising an extraction section supplied at the top with said hydroalcoholic feedstock and at least one intermediate raffinate fraction from step b) and at the bottom with an extraction solvent, and producing at the top an extraction stream and at the bottom a raffinate, wherein the extraction section is operated at a mean temperature in the extractor of between 10 and 40° C.; b) a counter-current liquid-liquid back-extraction comprising a back-extraction section supplied at the top with an acidic aqueous solution, having a pH between 0.5 and 5.0, and at the bottom with the extraction stream from step a), and producing at the top an extract and at the bottom the intermediate raffinate, wherein the back-extraction section is operated at a mean temperature between 40 and 80° C.


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