Method for removing hexafluoro-chlorobutylene from trifluoro-dichloroethane
A technology of trifluorodichloroethane and hexafluorochlorobutene is applied in the field of purification using photocatalytic oxidation, which can solve the problems such as failure to solve the recycling and reuse of adsorbents, and achieves fast reaction speed, high processing efficiency, and high retention rate. short time effect
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Embodiment 1
[0027] Add 3L of R123 containing about 1% hexafluorochlorobutene in a 5L glass reactor, pass in about 17g of chlorine gas under stirring to dissolve in the bottom liquid, and then pass oxygen into the reactor at a speed of 200 ml / min , the molar ratio of oxygen to hexafluorochlorobutene is 1:1, and the high-pressure mercury lamp is turned on, and the mercury lamp is placed in the middle of the quartz tube, and the lamp tube is cooled with compressed air. Under the control of mercury lamp heating and air cooling or water cooling, the photocatalytic liquid phase oxidation reaction is carried out at 20°C, the substance A produced by the reaction and the mixed gas produced by the vaporization of R123 due to the heat of the mercury lamp and the heat of reaction flow from the top of the reactor Continuous discharge, the discharged gas is cooled at -20°C, R123 is condensed and returned to the reactor, and the uncondensed substance A is collected after compression and condensation.
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Embodiment 2
[0030] The reaction is carried out in a φ50mm, L=500mm glass reactor, a φ25mm, L=400mm quartz tube is placed in the middle of the reactor, a 500w mercury lamp is placed in the middle of the quartz tube, and the lamp tube is cooled with compressed air. Add chlorine gas with a molar ratio of 1% (based on R123) to R123 containing about 1% hexafluorochlorobutene by mass ratio, mix uniformly and vaporize, and enter the reactor after being measured by a flow meter with a flow rate of 1200ml / min. Feed oxygen into the reactor, the flow rate of oxygen is 20ml / min, the molar ratio of oxygen to hexafluorochlorobutene is 2: 1, and a 500W mercury lamp is turned on to carry out photocatalytic gas-phase oxidation reaction at 100°C; the reacted substance A is three Fluoroacetyl chloride gas is hydrolyzed and absorbed, and trifluoroacetyl chloride is hydrolyzed into trifluoroacetic acid. After concentration, the finished product of trifluoroacetic acid is obtained. Hexafluorochlorobutene impur...
Embodiment 3
[0032]Add 3L of R123 containing about 1ppm hexafluorochlorobutene in a 5L glass reactor as the bottom liquid, then pass oxygen into the reactor at a speed of 20 ml / min, the molar ratio of oxygen to hexafluorochlorobutene The ratio is 5:1, and a 400w high-pressure mercury lamp is turned on to carry out photocatalytic liquid-phase oxidation reaction at 0°C. The substance A produced by the reaction and the mixed gas produced by the gasification of R123 due to the heat of the mercury lamp and the heat of reaction are continuously discharged from the top of the reactor. After the discharged gas is cooled at -20°C, R123 is condensed and returned to the reactor, and the uncondensed substance A is collected after being compressed and condensed. The bottom liquid was analyzed by chromatography, and no hexafluorochlorobutene impurity was detected.
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