Process for the production of 2,3,3,3-tetrafluoropropene
The present invention relates to a process for producing 2,3,3,3-tetrafluoropropene, comprising the steps of: a) providing a stream A comprising at least one of the compounds selected from the group consisting of 2-chloro-3,3,3-trifluoropropene and 2,3-dichloro-1,1,1-trifluoropropane; b) in a reactor, bringing said stream A into contact with HF in the presence or absence of a fluorination catalyst in order to produce a stream B comprising 2,3,3,3-tetrafluoropropene; characterized in that the electrical conductivity of said stream A provided in step a) is less than 15 mS/cm.
1. A process for producing 2,3,3,3-tetrafluoropropene, comprising the steps of:
a) providing a stream A comprising at least one starting compound selected from the group consisting of 2-chloro-3,3,3-trifluoropropene and 2,3-dichloro-1,1,1-trifluoropropane;
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 2,3,3,3-tetrafluoropropene;
wherein the electrical conductivity of said stream A provided in step a) is less than 15 mS/cm.
2. The process as claimed in claim 1 , wherein step b) is carried out in the gas phase in the presence of a catalyst.
3. The process as claimed in claim 1 , wherein the electrical conductivity of said stream A is less than 10 mS/cm.
4. The process as claimed in claim 1 , wherein step b) is carried out in the presence of a chromium-based catalyst.
5. The process as claimed in claim 1 , wherein the catalyst is based on chromium and also comprises a cocatalyst selected from the group consisting of Ni, Zn, Co, Mn and Mg.
6. The process as claimed in claim 1 , wherein stream A comprises 2-chloro-3,3,3-trifluoropropene, HF and 1,1,1,2,2-pentafluoropropane.
7. The process as claimed in claim 1 , wherein, in addition to 2,3,3,3-tetrafluoropropene, stream B comprises HF, HCl, 2-chloro-3,3,3-trifluoropropene which has not reacted and 1,1,1,2,2-pentafluoropropane.
8. The process as claimed in claim 1 , wherein step b) is carried out at a temperature of between 310° C. and 420° C.
9. The process as claimed in claim 1 , wherein step 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.