Gas-phase catalytic fluorination with chromium catalysts

1. Process for the fluorination of a chlorinated C3 alkane or alkene compound having at least one chlorine atom into a fluorinated C3 alkane or alkene compound having at least one fluorine atom comprising the following steps:

a. contacting, in a reactor, the chlorinated compound with hydrogen fluoride in gas phase in the presence of a fluorination catalyst to produce a fluorinated compound, and

b. regenerating the fluorination catalyst used in step a),

wherein the step (b) of regenerating the fluorination catalyst comprises (c) the treatment of said fluorination catalyst with an oxidizing agent-containing gas flow to form an oxidized fluorination catalyst, and (d) the treatment of the oxidized fluorination catalyst obtained in step (c) with a gaseous mixture comprising a reducing agent and an inert gas; the catalyst regenerated in step b) being reused in step a) and the reducing agent being selected from the group consisting of C 1 -C 10 hydrohalocarbons.

2. Process for the fluorination of a chlorinated C3 alkane or alkene compound having at least one chlorine atom into a fluorinated C3 alkane or alkene compound having at least one fluorine atom comprising the following steps:

(a) contacting, in a reactor, the chlorinated compound with hydrogen fluoride in gas phase in the presence of a fluorination catalyst to produce a fluorinated compound, and

(b) regenerating the fluorination catalyst used in step a),

wherein the step (b) of regenerating the fluorination catalyst comprises (c) the treatment of said fluorination catalyst with an oxidizing agent-containing gas flow to form an oxidized fluorination catalyst, and (d) the treatment of the oxidized fluorination catalyst obtained in step (c) with a gaseous mixture comprising a reducing agent; the catalyst regenerated in step b) being reused in step a) and the reducing agent being selected from the group consisting of C 1 -C 10 hydrohalocarbons.

3. Process according to claim 1 , wherein the reducing agent is selected from the group consisting of C 2 -C 6 hydrohalocarbons.

4. Process according to claim 1 , wherein the inert gas is selected from nitrogen, helium, argon, or mixtures thereof.

5. Process according to claim 1 , wherein the gaseous mixture comprises HF.

6. Process according to claim 1 , wherein the gaseous mixture of step (d) comprises from 1 to 10% by volume of reducing agent based on the total volume of the gaseous mixture.

7. Process according to claim 1 , wherein the gaseous mixture from step (d) comprises hydrogen and nitrogen or argon or the gaseous mixture from step (d) comprises a C2-C6 hydrohalocarbon, nitrogen or argon, and HF.

8. Process according to claim 1 , wherein step d) is carried out at a temperature ranging from 100° C. to 450° C., with a contact time of from 1 to 100 s.

9. Process according to claim 1 , wherein the chlorinated compound is 2-chloro-3,3,3-trifluoro-1-propene (HFCO-1233xf), 1,1,1,2,3-pentachloropropane (HCC-240db), 1,1,2,2,3-pentachloropropane (HCC-240aa), 2,3-dichloro-1,1,1-trifluoropropane (HCFC-243db), 1,1,2,3-tetrachloro-1-propene (HCO-1230xa), 2,3,3,3-tetrachloro-1-propene (HCO-1230xf), 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244bb), 1,1,1,3,3-pentachloropropane (HCC-240fa), 1,1,3,3-tetrachloropropene (HCO-1230za), 1,3,3,3-tetrachloropropene (HCO-1230zd), 1-chloro-3,3,3-trifluoropropene (HCFO-1233zd), 1,1,1,3-tetrachloropropane (HCC-250fb), 1,1,3-trichloropropene (HCO-1240za), 3,3,3-trichloropropene (HCO-1240zf); more preferably the chlorinated compound is selected from the group consisting of 2-chloro-3,3,3-trifluoro-1-propene (HFCO-1233xf), 1,1,1,2,3-pentachloropropane (HCC-240db), 1,1,2,2,3-pentachloropropane (HCC-240aa), 2,3-dichloro-1,1,1-trifluoropropane (HCFC-243db), 1,1,2,3-tetrachloro-1-propene (HCO-1230xa), 2,3,3,3-tetrachloro-1-propene (HCO-1230xf) or 2-chloro-1,1,1,2-tetrafluorocarbons (HCFC-244bb).

10. Process according to claim 1 , wherein the fluorinated compound is 2,3,3,3-tetrafluoro-1-propene (HFO-1234yf), 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244bb), 1,1,1,2,2-pentafluoropropane (HFC-245cb), 1,1,1,3,3-pentafluoropropane (HFC-245fa), 1,1,1,3-tetrafluoro-3-chloropropane (HCFC-244fa), 1-chloro-3,3,3-trifluoropropene (HCFO-1233zd), 1,3,3,3-tetrafluoropropene (HFO-1234ze), 3,3,3-trifluoropropene (HFO-1243zf) or 2-chloro-3,3,3-trifluoro-1-propene (HFCO-1233xf).

11. Process according to claim 1 , wherein the fluorination of the chlorinated compound into a fluorinated compound is:

2-chloro-3,3,3-trifluoro-1-propene (HFCO-1233xf) to 2,3,3,3-tetrafluoro-1-propene (HFO-1234yf);

1,1,1,2,3-pentachloropropane (HCC-240db) to 2,3,3,3-tetrafluoro-1-propene (HFO-1234yf);

1,1,2,2,3-pentachloropropane (HCC-240aa) to 2,3,3,3-tetrafluoro-1-propene (HFO-1234yf);

2,3-dichloro-1,1,1-trifluoropropane (HCFC-243db) to 2,3,3,3-tetrafluoro-1-propene (HFO-1234yf);

1,1,2,3-tetrachloro-1-propene (HCO-1230xa) to 2,3,3,3-tetrafluoro-1-propene (HFO-1234yf);

2,3,3,3-tetrachloro-1-propene (HCO-1230xf) to 2,3,3,3-tetrafluoro-1-propene (HFO-1234yf);

1,1,1,2,3-pentachloropropane (HCC-240db) to 2-chloro-3,3,3-trifluoro-1-propene (HFCO-1233xf);

1,1,2,2,3-pentachloropropane (HCC-240aa) to 2-chloro-3,3,3-trifluoro-1-propene (HFCO-1233xf);

2,3-dichloro-1,1,1-trifluoropropane (HCFC-243db) to 2-chloro-3,3,3-trifluoro-1-propene (HFCO-1233xf);

1,1,2,3-tetrachloro-1-propene (HCO-1230xa) to 2-chloro-3,3,3-trifluoro-1-propene (HFCO-1233xf);

2,3,3,3-tetrachloro-1-propene (HCO-1230xf) to 2-chloro-3,3,3-trifluoro-1-propene (HFCO-1233xf);

2-chloro-3,3,3-trifluoro-1-propene (HFCO-1233xf) to 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244bb);

1,1,1,2,3-pentachloropropane (HCC-240db) to 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244bb);

1,1,2,2,3-pentachloropropane (HCC-240aa) to 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244bb);

2,3-dichloro-1,1,1-trifluoropropane (HCFC-243db) to 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244bb);

1,1,2,3-tetrachloro-1-propene (HCO-1230xa) to 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244bb);

2,3,3,3-tetrachloro-1-propene (HCO-1230xf) to 2-chloro-1,1,1,2-tetrafluoropropane (HCFC-244bb);

1,1,1,2,3-pentachloropropane (HCC-240db) to 1,1,1,2,2-pentafluoropropane (HFC-245cb);

1,1,2,2,3-pentachloropropane (HCC-240aa) to 1,1,1,2,2-pentafluoropropane (HFC-245cb);

2,3-dichloro-1,1,1-trifluoropropane (HCFC-243db) to 1,1,1,2,2-pentafluoropropane (HFC-245cb);

1,1,2,3-tetrachloro-1-propene (HCO-1230xa) to 1,1,1,2,2-pentafluoropropane (HFC-245cb);

2,3,3,3-tetrachloro-1-propene (HCO-1230xf) to 1,1,1,2,2-pentafluoropropane (HFC-245cb).

12. Process according to claim 1 , wherein the fluorination catalyst comprises chromium oxyfluoride, chromium oxides, chromium halides and mixtures thereof.

13. Process according to claim 1 , wherein the fluorination catalyst contains one or more co-catalysts comprising a salt of a transition metal selected from the group consisting of Co, Zn, Mn, Mg, V, Mo, Te, Nb, Sb, Ta, Ni; or a phosphorous salt.

14. Process according to claim 1 , comprising an activation step carried out before step (a) which comprises a first step of contacting the fluorination catalyst with a gas flow containing an oxidizing agent selected from oxygen, air, chlorine or a mixture of oxygen and nitrogen.

15. Process according to claim 14 , wherein the activation step comprises a second step, subsequent to the first step, of treating the fluorination catalyst obtained after the first step with a gaseous mixture containing a reducing agent and an inert gas, said reducing agent being hydrogen or a C 2 -C 6 hydrohalocarbon.

16. Process according to claim 1 , wherein steps (a) and (b) are carried out alternately.

17. Process according to claim 1 , wherein a purge of the reactor is carried out before and/or after step (b), the purge being carried out by introducing a stream of nitrogen in the reactor or by maintaining the reactor under vacuum.