Process for producing hydrofluoroolefin

1. A method for producing a hydrofluoroolefin, the method comprising:

reacting a chlorofluoroolefin of formula (1) with hydrogen in the presence of a catalyst supported on a carrier, to obtain a hydrofluoroolefin of formula (2):

CZX═CClY  (1)

wherein

X is a fluorine atom or a chlorine atom,

Y is a fluorine atom, a chlorine atom or a hydrogen atom, and

Z is a fluorine atom or CF3;

CZX′═CHY′  (2)

wherein

X′ is a fluorine atom when X is a fluorine atom, or X′ is a hydrogen atom when X is a chlorine atom,

Y′ is a fluorine atom when Y is a fluorine atom, or Y′ is a hydrogen atom when Y is a chlorine atom or a hydrogen atom, and

Z is the same as Z in the formula (I);

wherein

the chlorofluoroolefin of formula (I) does not comprise chlorotrifluoroethylene;

the catalyst comprises an alloy containing at least one platinum group element selected from the group consisting of palladium and platinum, and at least one second element selected from the group consisting of copper, potassium, silver, zinc, tin, lead, and bismuth;

a content mass ratio of the at least one platinum group element to the at least one second element in the alloy is from 60:40 to 99:1, and

the reacting is carried out while a maximum temperature of the catalyst supported on the carrier is controlled to be at most 130° C.

2. The method according to claim 1 , wherein the at least one second element is selected from the group consisting of copper, tin, and bismuth.

3. The method according to claim 1 , wherein the catalyst comprises an alloy of palladium and at least one second element selected from the group consisting of copper, tin, and bismuth.

4. The method according to claim 1 , wherein the carrier is at least one member selected from the group consisting of activated carbon, carbon black, and carbon fibers.

5. The method according to claim 1 , wherein the carrier is at least one member selected from the group consisting of alumina, silica, titania, and zirconia.

6. The method according to claim 1 , wherein an amount of the catalyst is from 0.1 to 10 mass % based on the carrier.

7. The method according to claim 1 , wherein the chlorofluoroolefin and hydrogen are introduced to a catalyst layer packed with the carrier supporting the catalyst, and reacted in a gaseous phase.

8. The method according to claim 7 , wherein the chlorofluoroolefin and hydrogen are introduced to a gas introduction part of the catalyst layer, and hydrogen is introduced from at least one point between the gas introduction part and a gas discharge part of the catalyst layer.

9. The method according to claim 7 , wherein said reacting is carried out while a maximum temperature of the catalyst layer is at most 130 C.

10. The method according to claim 7 , wherein a molar ratio of hydrogen to the chlorofluoroolefin introduced to the catalyst layer [H2]/[Cl] is from 0.1 to 0.7, where [H2] is a total number of moles of hydrogen and [C1] is a number of moles of chlorine atoms in the chlorofluoroolefin.

11. The method according to claim 1 , wherein the chlorofluoroolefin and hydrogen are reacted in a liquid phase in the presence of the carrier supporting the catalyst.

12. The method according to claim 1 , wherein the chlorofluoroolefin is at least one member selected from the group consisting of trans-1,2-dichloro-1,2-difluoroethylene, cis-1,2-dichloro-1,2-difluoroethylene, 1-dichloro-2,3,3,3-tetrafluoropropene, and 1-chloro-2,3,3,3-tetrafluoropropene.

13. The method according to claim 1 , wherein the hydrofluoroolefin is 2,3,3,3-tetrafluoropropene and the chlorofluoroolefin is 1,1-dichloro-2,3,3,3-tetrafluoropropene.

14. The method according to claim 1 , wherein the at least one second element is bismuth.