Process for preparing 2,3,3,3-tetrafluoropropene
The present invention provides a process for producing 2,3,3,3-tetrafluoropropene including the step of dehydrofluorinating 1,1,1,2,3-pentafluoropropane, wherein 1,3,3,3-tetrafluoropropene and 1,1,3,3,3-pentafluoropropane are supplied together with 1,1,1,2,3-pentafluoropropane to a reactor containing a catalyst to simultaneously perform dehydrofluorination reaction and isomerization reaction. According to the process of the present invention, 2,3,3,3-tetrafluoropropene (HFO-1234yf) can be efficiently produced by effectively using the by-products of the dehydrofluorination reaction.
1. A process for producing 2,3,3,3-tetrafluoropropene comprising a step of dehydrofluorinating 1,1,1,2,3-pentafluoropropane,
wherein 1,3,3,3-tetrafluoropropene and 1,1,3,3,3-pentafluoropropane are supplied together with 1,1,1,2,3-pentafluoropropane to a reactor containing a catalyst to simultaneously perform a dehydrofluorination reaction and a isomerization reaction to produce the 2,3,3,3-tetrafluoropropene.
2. The process according to claim 1 , wherein the 1,3,3,3-tetrafluoropropene and the 1,1,3,3,3-pentafluoropropane supplied to the reactor are by-products of the dehydrofluorination reaction of 1,1,1,2,3-pentafluoropropane.
3. The process according to claim 1 , which comprises the steps of:
supplying 1,1,1,2,3-pentafluoropropane in a reactor containing a catalyst therein to conduct a dehydrofluorination reaction and obtain a reaction product;
subjecting the reaction product to distillation to separate the reaction product into a first stream containing 2,3,3,3-tetrafluoropropene as a main component and a second stream containing 1,3,3,3-tetrafluoropropene and 1,1,3,3,3-pentafluoropropane as main components; and
supplying the 1,3,3,3-tetrafluoropropene and the 1,1,3,3,3-pentafluoropropane obtained from the second stream to the reactor together with the 1,1,1,2,3-pentafluoropropane to produce the 2,3,3,3-tetrafluoropropene.
4. The process according to claim 1 , wherein the catalyst in the reactor is a chromium oxide catalyst or a fluorinated chromium oxide catalyst.
5. The process according to claim 1 , wherein the catalyst in the reactor is a highly fluorinated chromium oxide catalyst having a fluorine content of not less than 30 weight %.