초록 ▼

There is provided a process for producing hexafluoropropylene oxide which is novel and capable of achieving a higher yield. An organic phase comprising hexafluoropropylene (HFP) in an organic solvent and an aqueous phase comprising an oxygen-containing oxidizing agent in water are supplied to a smal

There is provided a process for producing hexafluoropropylene oxide which is novel and capable of achieving a higher yield. An organic phase comprising hexafluoropropylene (HFP) in an organic solvent and an aqueous phase comprising an oxygen-containing oxidizing agent in water are supplied to a small space (or microspace), preferably together with a phase transfer catalyst. The organic phase and the aqueous phase are contacted with each other in the small space, thereby reacting hexafluoropropylene (HFP) with the oxygen-containing oxidizing agent, preferably by an action of the phase transfer catalyst to give hexafluoropropylene oxide (HFPO). After the reaction, the organic phase and the aqueous phase are taken out from the small space to obtain an organic phase comprising the hexafluoropropylene oxide (HFPO).

대표청구항 ▼

1. A process for producing hexafluoropropylene oxide, which comprises passing an organic phase comprising hexafluoropropylene and an aqueous phase comprising an oxygen-containing oxidizing agent through a small space in contact with each other, thereby reacting hexafluoropropylene with the oxygen-c

1. A process for producing hexafluoropropylene oxide, which comprises passing an organic phase comprising hexafluoropropylene and an aqueous phase comprising an oxygen-containing oxidizing agent through a small space in contact with each other, thereby reacting hexafluoropropylene with the oxygen-containing oxidizing agent to obtain hexafluoropropylene oxide. 2. The process according to claim 1, wherein the small space has a passage width of 3 cm or less. 3. The process according to claim 1, wherein the organic phase comprising hexafluoropropylene and the aqueous phase comprising an oxygen-containing oxidizing agent are contacted with each other in the presence of a phase transfer catalyst, thereby reacting hexafluoropropylene with the oxygen-containing oxidizing agent by an action of the phase transfer catalyst. 4. The process according to claim 1, wherein the small space is maintained at −40 to 100° C. and 0.1 to 20 MPa. 5. The process according to claim 1, wherein the organic phase is subjected to conditions of −40 to 100° C. and 0.1 to 20 MPa before the organic phase is supplied to the small space. 6. The process according to claim 5, wherein the organic phase is subjected to temperature and pressure conditions at which hexafluoropropylene is substantially in a liquid state before the organic phase is supplied to the small space. 7. The process according to claim 1, wherein a reaction time in the small space is from 0.01 to 1,000 seconds. 8. The process according to claim 3, wherein the phase transfer catalyst is a quaternary ammonium salt. 9. The process according to claim 1, wherein the oxygen-containing oxidizing agent is a hypochlorite. 10. The process according to claim 2, wherein the organic phase comprising hexafluoropropylene and the aqueous phase comprising an oxygen-containing oxidizing agent are contacted with each other in the presence of a phase transfer catalyst, thereby reacting hexafluoropropylene with the oxygen-containing oxidizing agent by an action of the phase transfer catalyst.