Process for producing 2-chloro-3,3,3-trifluoropropene
The present invention relates to a process for the production of 2-chloro-3,3,3-trifluoropropene comprising the stages of: a) providing a stream A comprising at least one of the compounds selected from the group consisting of 2,3-dichloro-1,1,1-trifluoropropane, 1,1,1,2,3-pentachloropropane, 1,1,2,3-tetrachloropropene and 2,3,3,3-tetrachloropropene; b) in a reactor, bringing said stream A into contact with HF in the presence or absence of a catalyst in order to produce a stream B comprising 2-chloro-3,3,3-trifluoropropene; characterized in that the electrical conductivity of said stream A provided in stage a) is less than 15 mS/cm.
1. A process for the production of 2-chloro-3,3,3-trifluoropropene comprising the stages of:
a) providing a stream A comprising at least one of the compounds selected from the group consisting of 2,3-dichloro-1,1,1-trifluoropropane, 1,1,1,2,3-pentachloropropane, 1,1,2,3-tetrachloropropene and 2,3,3,3-tetrachloropropene;
b) in a reactor, bringing said stream A into contact with HF in the presence or absence of a catalyst in order to produce a stream B comprising 2-chloro-3,3,3-trifluoropropene;
wherein the electrical conductivity of said stream A provided in stage a) is less than 15 mS/cm.
2. The process as claimed in claim 1 , wherein stage b) is carried out in the gas phase in the presence or absence of a catalyst.
3. The process as claimed in claim 1 , wherein stage b) is carried out in the liquid phase in the presence of a catalyst.
4. The process as claimed in claim 1 , wherein the electrical conductivity of said stream A is less than 10 mS/cm.
5. The process as claimed in claim 1 , wherein stage b) is carried out in the presence of a chromium-based catalyst.
6. The process as claimed in claim 5 , wherein the catalyst is based on chromium and also comprises a cocatalyst selected from the group consisting of Ni, Zn, Co, Mn and Mg.
7. The process as claimed in claim 1 , wherein the stream B comprises, besides 2-chloro-3,3,3-trifluoropropene, HCl, HF, 2,3,3,3-tetrafluoropropene, and optionally 2,3-dichloro-3,3-difluoropropene, 2,3,3-trichloro-3-fluoropropene and/or 1,1,1,2,2-pentafluoropropane.
8. The process as claimed in claim 1 , wherein stage b) is carried out at a temperature of between 320° C. and 440° C.
9. The process as claimed in claim 1 , wherein stage b) is carried out in the presence of hydrofluoric acid having an electrical conductivity of less than 10 mS/cm.
10. The process as claimed in claim 1 , wherein the process further comprises a step of reducing the concentration of electrolytes in stream A until the electrical conductivity of stream A is less than 15 mS/cm.