IP Library Granted Patent US 9,346,723
Granted Patent B2
US 9,346,723 · App. 14/376,190 · Granted May 24, 2016

Method for producing 2,3,3,3-tetrafluoropropene

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Quick Facts
Patent No.
US 9,346,723
App. No.
14/376,190
Granted
May 24, 2016
Kind
B2
Abstract

The invention concerns a method for producing 2,3,3,3-tetrafluoropropene comprising: a fluoridation reaction of a halopropane and/or halopropene into 2,3,3,3-tetrafluoropropene by means of hydrogen fluoride; the recovery of a gas stream resulting from the reaction; the cooling and partial condensation of the gas stream resulting from the reaction into a partially condensed stream; the separation of the partially condensed stream into a gas fraction and a liquid fraction; the compression of the gas fraction into a compressed gas fraction; the compression of the liquid fraction into a compressed liquid fraction; the distillation of the compressed gas fraction and compressed liquid fraction in order to provide a stream of 2,3,3,3-tetrafluoropropene, a stream of hydrochloric acid, and a stream of unreacted hydrogen fluoride. The invention also concerns an installation suitable for implementing said method.

Claims (31)

1. A method for producing 2,3,3,3-tetrafluoropropene, comprising:

reactively fluorinating a halopropane and/or halopropene to 2,3,3,3-tetrafluoropropene using hydrogen fluoride;

recovering a gaseous stream obtained from the reaction;

cooling and partially condensing the gaseous stream obtained from the reaction, to give a partially condensed stream;

separating the partially condensed stream into a gaseous fraction and a liquid fraction;

compressing the gaseous fraction to give a compressed gaseous fraction;

compressing the liquid fraction to give a compressed liquid fraction;

distilling the compressed gaseous fraction and the compressed liquid fraction to give a 2,3,3,3-tetrafluoropropene stream, a hydrochloric acid stream, and a stream of unreacted hydrogen fluoride.

2. The method as claimed in claim 1 , wherein the stream of unreacted hydrogen fluoride further comprises organic compounds.

3. The method as claimed in claim 1 , wherein the stream of unreacted hydrogen fluoride is recycled to the fluorination reaction.

4. The method as claimed in claim 1 , wherein the fluorination reaction is a gas-phase catalytic fluorination reaction.

5. The method as claimed in claim 1 , wherein the fluorination reaction is carried out at a pressure lower than that of the distillation of the compressed gaseous fraction and the compressed liquid fraction.

6. The method as claimed in claim 1 , wherein the fluorination reaction is carried out at a pressure of from 0.1 to 10 bar abs and/or the distillation is carried out at a pressure of from 5 to 40 bar abs.

7. The method as claimed in claim 1 , wherein the gaseous fraction represents from 25% to 60% of the partially condensed stream, and the liquid fraction represents from 40% to 75% of the partially condensed stream, in proportions by mass.

8. The method as claimed in claim 1 , wherein the distillation step comprises:

distilling the compressed gaseous fraction and the compressed liquid fraction in a first distillation;

recovering the stream of unreacted hydrogen fluoride at the end of the first distillation;

recovering an intermediate stream at the end of the first distillation;

distilling the intermediate stream in a second distillation;

recovering the hydrochloric acid stream at the end of the second distillation; and

recovering the 2,3,3,3-tetrafluoropropene stream at the end of the second distillation.

9. The method as claimed in claim 1 , wherein the distillation step comprises:

distilling the compressed gaseous fraction and the compressed liquid fraction in a first distillation;

recovering the hydrochloric acid stream at the end of the first distillation;

recovering an intermediate stream at the end of the first distillation;

distilling the intermediate stream in a second distillation;

recovering the 2,3,3,3-tetrafluoropropene stream at the end of the second distillation; and

recovering the stream of unreacted hydrogen fluoride at the end of the second distillation.

10. The method as claimed in claim 1 , wherein the compressed gaseous fraction and the compressed liquid fraction are introduced at different sites of a distillation column.

11. The method as claimed in claim 1 , wherein the 2,3,3,3-tetrafluoropropene stream undergoes one or more further purification steps.

12. The method as claimed in claim 1 , wherein the halopropane and/or halopropene comprises a chloropropane and/or chloropropene.

Assignments (2)
CHANGE OF ADDRESS Recorded Jul 4, 2025
From: ARKEMA FRANCE
To: ARKEMA FRANCE
Reel/Frame 071814/0739 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 30, 2014
From: DEUR-BERT, DOMINIQUE; COLLIER, BERTRAND; WENDLINGER, LAURENT
To: ARKEMA FRANCE
Reel/Frame 034070/0877 →