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:
Jun. 08, 2021

Filed:

Nov. 08, 2018
Applicant:

Arkema France, Colombes, FR;

Inventors:

Bertrand Collier, Montbard, FR;

Dominique Deur-Bert, Charly, FR;

Anne Pigamo, Francheville, FR;

Laurent Wendlinger, Soucieu en Jarrest, FR;

Assignee:

Arkema France, Colombes, FR;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 17/25 (2006.01); B01J 23/26 (2006.01); C07C 17/20 (2006.01); C07C 21/18 (2006.01);
U.S. Cl.
CPC ...
C07C 17/25 (2013.01); B01J 23/26 (2013.01); C07C 17/206 (2013.01); C07C 21/18 (2013.01);
Abstract

The present invention relates to a process for the production of 2,3,3,3-tetrafluoropropene comprising the stages: i) in a first reactor, bringing 2-chloro-3,3,3-trifluoropropene into contact with hydrofluoric acid in the gas phase in the presence of a catalyst, in order to produce a stream A comprising 2,3,3,3-tetrafluoropropene, HF and unreacted 2-chloro-3,3,3-trifluoropropene; and ii) in a second reactor, bringing hydrofluoric acid into contact, in the gas phase in the presence or absence of a catalyst, with at least one chlorinated compound selected from the group consisting of 1,1,1,2,3-pentachloropropane, 2,3-dichloro-1,1,1-trifluoropropane, 2,3,3,3-tetrachloropropene and 1,1,2,3-tetrachloropropene, in order to produce a stream B comprising 2-chloro-3,3,3-trifluoropropene, characterized in that the stream A obtained in stage i) feeds said second reactor used for stage ii); and in that the pressure at the inlet of said first reactor of stage i) is greater than the pressure at the inlet of said second reactor of stage ii).


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