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:
Feb. 15, 2022

Filed:

Jun. 06, 2019
Applicant:

Arkema France, Colombes, FR;

Inventors:

Bertrand Collier, Pierre-Benite, FR;

Dominique Deur-Bert, Pierre-Benite, FR;

Anne Pigamo, Pierre-Benite, FR;

Audrey Riehl, Pierre-Benite, FR;

Laurent Wendlinger, Pierre-Benite, FR;

Assignee:

Arkema France, Colombes, FR;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 21/18 (2006.01); B01J 8/04 (2006.01); C07C 17/20 (2006.01);
U.S. Cl.
CPC ...
C07C 21/18 (2013.01); B01J 8/0453 (2013.01); B01J 8/0492 (2013.01); B01J 8/0496 (2013.01); C07C 17/206 (2013.01); B01J 2208/00495 (2013.01);
Abstract

A process for producing 2,3,3,3-tetrafluoropropene comprises the steps: i) in a first adiabatic reactor comprising a fixed bed composed of an inlet and an outlet, bringing 2-chloro-3,3,3-trifluoropropene into contact with hydrofluoric acid in the gas phase in the presence of a catalyst 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 adiabatic reactor comprising a fixed bed composed of an inlet and an outlet, bringing hydrofluoric acid into contact in the gas phase, optionally in the presence of a catalyst, with at least one chlorinated compound to produce a stream B comprising 2-chloro-3,3,3-trifluoropropene. The stream A obtained in step i) feeds said second reactor. The inlet temperature of the fixed bed of one of said first or second reactors is between 300° C. and 400° C. The longitudinal temperature difference between the inlet and the outlet of the fixed bed in question is less than 20° C.


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