Method for preparing high purity tetrafluoromethane through combination of rectification and adsorption
A high-purity tetrafluoromethane and tetrafluoromethane technology, which is applied in the disproportionation separation/purification of halogenated hydrocarbons, can solve problems such as the inability to produce tetrafluoromethane, and achieve low production costs, stable quality, and good use of cooling and heat Effect
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Embodiment 1
[0022] In the fluidized bed of catalyst CrO2F2, crude tetrafluoromethane (300 kg / hour) is continuously supplied by the equipment that generates tetrafluoromethane, and tetrafluoromethane is prepared by gas phase reaction of chlorofluoromethane and hydrogen fluoride, and high-purity tetrafluoromethane is produced through multi-stage reaction. of fluoromethane;
[0023] The first stage of the reaction is made by reacting CF3Cl with HF in a fluidized bed reactor filled with CrO2F2 catalyst at 200°C, or heating CrF3·3H2O at 350°C in the presence of O2; CF 3 The mass ratio of Cl to HF is controlled at 1:2, and the gas space velocity is 10-150h -1 , the reaction temperature is 380°C, the gas generated in the first stage enters the second stage reaction after being washed with water, alkali washed and dried;
[0024] In the second stage of the reaction, HF is introduced again to make CF 3 The mass ratio of Cl and HF is controlled at 1:0.3, and the gas space veloci...
Embodiment 2
[0026] In the catalyst CrO 2 F 2 The fluidized bed is continuously supplied with crude tetrafluoromethane (350 kg / hour) by the equipment that generates tetrafluoromethane, and the gas phase reaction of chlorofluoromethane and hydrogen fluoride is used to prepare tetrafluoromethane, and high-purity tetrafluoromethane is produced through multi-stage reaction ;
[0027] Among them, the first stage of the reaction is filled with CrO 2 F 2 Catalyst in a fluidized bed reactor to make CF 3 Cl reacts with HF at 600°C, or CrF 3 ·3H 2 O in O 2 Prepared by heating at 750°C in the presence of; CF 3 The mass ratio of Cl to HF is controlled at 1:8, and the gas space velocity is 10-150h -1 , the reaction temperature is 420°C, the gas generated in the first stage enters the second stage reaction after being washed with water, alkali washed and dried;
[0028] In the second stage of the reaction, HF is introduced again to make CF 3 The m...
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