Process for the preparation of 1,1,1,3,3,3-hexafluoropropane and at least one of 1,1,1,2,3,3-hexafluoropropane and 1,1,1,2,3,3,3-heptafluoropropane

1. A process for the manufacture of 1,1,1,3,3,3-hexafluoropropane and at least one compound selected from the group consisting of 1,1,1,2,3,3-hexafluoropropane and 1,1,1,2,3,3,3-heptafluoropropane, comprising:

(a) reacting HF, Cl 2 , and at least one halopropene of the formula CX 3 CCl═CX 2 , wherein each X is independently selected from the group consisting of F and Cl, to produce a product comprising CF 3 CCl 2 CF 3 and CF 3 CClFCClF 2 , wherein said CF 3 CCl 2 CF 3 and CF 3 CClFCClF 2 are produced in the presence of a chlorofluorination catalyst comprising at least one composition selected from the group consisting of (i) compositions comprising ZnCr 2 O 4 and crystalline α-chromium oxide, (ii) compositions comprising a zinc halide and α-chromium oxide and (iii) compositions of (i) or (ii) which have been treated with a fluorinating agent;

(b) reacting CF 3 CCl 2 CF 3 and CF 3 CClFCClF 2 produced in (a) with hydrogen, optionally in the presence of HF, to produce a product comprising CF 3 CH 2 CF 3 and at least one compound selected from the group consisting of CHF 2 CHFCF 3 , and CF 3 CHFCF 3 ; and

(c) recovering from the product produced in (b), CF 3 CH 2 CF 3 and at least one compound selected from the group consisting of CHF 2 CHFCF 3 and CF 3 CHFCF 3 .

2. The process of claim 1 wherein the halopropene reactant is contacted with Cl 2 and HF in a pre-reactor.

3. The process of claim 1 wherein the halopropene reactant is contacted with HF in a pre-reactor.

4. The process of claim 1 wherein the reaction of (b) is conducted in a reaction zone which is unpacked or packed with a nickel alloy at a temperature of from about 350° C. to about 600° C.

5. The process of claim 1 wherein the reaction of (b) is conducted in a reaction zone containing a hydrogenation catalyst at a temperature of from about 100° C. to about 350° C.

6. The process of claim 1 wherein in (a) the catalyst is selected from the group consisting of (i) compositions comprising ZnCr 2 O 4 and crystalline α-chromium oxide and (iii) compositions of (i) which have been treated with a fluorinating agent.

7. The process of claim 6 wherein the amount of zinc relative to the total of chromium and zinc in the catalyst composition is from about 1 atom % to about 25 atom %.

8. The process of claim 6 wherein the catalyst is selected from the group consisting of (i) compositions comprising ZnCr 2 O 4 and crystalline α-chromium oxide wherein the ZnCr 2 O 4 contains between about 10 atom percent and 67 atom percent of the chromium in the composition and at least about 70 atom percent of the zinc in the composition, and wherein at least about 90 atom percent of the chromium present as chromium oxide in the composition is present as ZnCr 2 O 4 or crystalline α-chromium oxide and (iii) compositions of (i) which have been treated with a fluorinating agent.

9. The process of claim 1 wherein in (a) the catalyst is selected from the group consisting of (ii) compositions comprising a zinc halide and α-chromium oxide and (iii) compositions of (ii) which have been treated with a fluorinating agent.

10. The process of claim 9 wherein the amount of zinc relative to the total of chromium and zinc in the catalyst composition is from about 0.1 atom % to about 25 atom %.

11. The process of claim 9 wherein the catalyst is selected from the group consisting of (ii) compositions wherein a zinc halide is supported on a support comprising α-chromium oxide and (iii) compositions of (ii) which have been treated with a fluorinating agent; and wherein the amount of zinc relative to the total of chromium and zinc in the catalyst composition is from about 2 atom % to about 10 atom %.