The preparation method of 2,3,3,3-tetrafluoropropene
A technology of tetrafluoropropene and heating method, which is applied in the preparation of halogenated hydrocarbons, chemical instruments and methods, organic chemistry, etc., can solve the problems of complex separation of mixtures, many side reactions, and short production cycle, so as to avoid the production of highly toxic substances Production of fluoroisobutylene, reduction in the probability of side reactions, and the effect of inhibiting carbon formation
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Embodiment 1
[0034] A kind of preparation method of 2,3,3,3-tetrafluoropropene, difluorochloromethane (R 22 ) and monochloromethane (methyl chloride) as raw materials, the cleavage reaction occurs under the condition of diluting with superheated steam to obtain 2,3,3,3-tetrafluoropropene. The chemical reaction equation is as follows:
[0035] 2CHClF 2 +CH 3 Cl→CF 3 CF=CH 2 +3HCl
[0036] Charge 16.8g of monochloromethane and 86.5g of difluorochloromethane into a steel cylinder with a volume of 8L
[0037]Add 6000g of pure water to a 10L jacketed reactor with a thermometer, a pressure gauge, and a pressure reducing valve. The ferrule is equipped with heat-conducting silicone oil and connected to a circulating oil pump. Set the temperature of the circulating oil pump to 130°C so that the jacket The water vapor generated by the temperature gauge connected to the sleeve reactor is passed into the tube furnace, and the temperature of the tube furnace is set at 1000°C to generate superheat...
Embodiment 2
[0041] Embodiment 2: As described in Embodiment 1, the difference is:
[0042] The reaction device is first fed with superheated steam to preheat the reaction pipeline. When the thermometer connected to the reaction pipeline is stable at 700°C, adjust the flow rate of the volume flowmeter connected to the steam pipeline to 209.2ml / s, and adjust the flow rate of the reaction raw materials. The metered flow rate is 41.8ml / s, and the reaction product mixed flow flows out from the reaction tube and then enters the quenching device, the secondary alkali cleaning device, and the drying device. The product flow obtained after drying is collected, and the mixed product is analyzed by gas chromatography. - The mass fraction of tetrafluoropropene is 42.5%.
Embodiment 3
[0043] Embodiment 3: As described in Embodiment 1, the difference is:
[0044] The reaction device is first fed with superheated steam to preheat the reaction pipeline. When the thermometer connected to the reaction pipeline is stable at 700°C, adjust the flow rate of the volume flowmeter connected to the steam pipeline to 225.9ml / s, and adjust the flow rate of the reaction raw material connection. The metered flow rate is 25.1ml / s. The mixed flow of reaction products flows out from the reaction tube and then enters the quenching device, the secondary alkali washing device, and the drying device. The product flow obtained after drying is collected and analyzed by gas chromatography. - The mass fraction of tetrafluoropropene is 45.9%.
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