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:
Dec. 07, 2021

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 17/20 (2006.01); B01J 19/24 (2006.01); C07C 17/269 (2006.01); B01J 19/00 (2006.01); C07C 21/18 (2006.01); C07C 21/04 (2006.01);
U.S. Cl.
CPC ...
C07C 17/206 (2013.01); B01J 19/00 (2013.01); B01J 19/0013 (2013.01); B01J 19/24 (2013.01); B01J 19/242 (2013.01); B01J 19/2415 (2013.01); C07C 17/269 (2013.01); C07C 21/04 (2013.01); C07C 21/18 (2013.01); B01J 2219/00054 (2013.01); B01J 2219/00063 (2013.01); B01J 2219/00155 (2013.01);
Abstract

A process for producing 2,3,3,3-tetrafluoropropene comprises i) in a first adiabatic reactor comprising a fixed bed composed of an inlet and an outlet, bringing hydrofluoric acid into contact, in the gas phase with at least one chlorinated compound in order to produce a stream A comprising 2-chloro-3,3,3-trifluoropropene, ii) in a second adiabatic reactor comprising a fixed bed composed of an inlet and an outlet, bringing the stream A into contact, in the gas phase in the presence of a catalyst, with hydrofluoric acid, to produce a stream B comprising 2,3,3,3-tetrafluoropropene. The temperature at the inlet 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 of the reactor is less than 20° C.


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