Preparation method for 1,1,1,3,3-pentafluoropropane
A technology for pentafluoropropane and trifluoropropane, which is applied in the field of synthesis of hydrofluorochlorocarbons, can solve the problems of difficult preparation of raw materials, high cost of raw materials, etc., and achieves the effects of high conversion rate, good selectivity and high efficiency
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Embodiment 1
[0033] Add 4.32 moles of fluorinated antimony pentachloride and 12.96 moles of anhydrous hydrofluoric acid into a 2L liquid-phase reactor, heat up to 80°C, and add 3,3-dichloro-1,1,1-trifluoropropane (0.72 mol / hour) and anhydrous hydrofluoric acid (3.6 mol / hour) are continuously fed into the reactor at a molar ratio of 1:5 for reaction, and the pressure of the reactor is maintained at 0.6MPa, and the gas phase reaction product is collected and cooled , washing with water and washing with alkali to obtain 1,1,1,3,3-pentafluoropropane product. After continuing the reaction for 72 hours, the collected products were analyzed, and the reaction conversion rate was 97.8%, and the selectivity was 98.7%.
Embodiment 2
[0035] Add 6 moles of fluorinated tin tetrachloride and 12 moles of anhydrous hydrofluoric acid into a 2L liquid-phase reactor, heat up to 120°C, add 3,3-dichloro-1,1,1-trifluoropropane (0.6 mol / hour) and anhydrous hydrofluoric acid (1.2 mol / hour) are continuously fed into the reactor at a molar ratio of 1:2 for reaction, and the pressure of the reactor is maintained at 1.0MPa, and the gas phase reaction product is collected and cooled , washing with water and washing with alkali to obtain 1,1,1,3,3-pentafluoropropane product. After continuing the reaction for 72 hours, the collected products were analyzed, and the reaction conversion rate was 94.2%, and the selectivity was 95.1%.
Embodiment 3
[0037] Add 0.6 moles of fluorinated titanium tetrachloride and 3.6 moles of anhydrous hydrofluoric acid into a 1L liquid-phase reactor, heat up to 100°C, add 3,3-dichloro-1,1,1-trifluoropropane (0.3 mol / hour) and anhydrous hydrofluoric acid (3 mol / hour) are continuously fed into the reactor at a molar ratio of 1:10 for reaction, and the pressure of the reactor is maintained at 0.8MPa, and the gas phase reaction product is collected and cooled , washing with water and washing with alkali to obtain 1,1,1,3,3-pentafluoropropane product. After continuing the reaction for 72 hours, the collected products were analyzed, and the reaction conversion rate was 94.2%, and the selectivity was 96.0%.
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