Method for preparing perfluoroisobutyronitrile from hexafluoropropylene dipolymer as well as perfluoroisobutyronitrile and application
A technology of hexafluoropropylene dimerization and hexafluoropropylene dimer is applied in perfluoroisobutyronitrile and application fields, and can solve the problem of high equipment cost, unfavorable industrial scale-up production, high cost of electrolytic electrode plate production, and isobutyric anhydride raw material. It is not easy to obtain and other problems, and achieves the effects of low global warming effect, high yield and short reaction route.
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Embodiment 1
[0025] Example 1: Preparation of hexafluoropropylene dimer raw materials: hexafluoropropylene gas was passed through a catalytic reaction tube equipped with NaF / Al2O3 catalyst, the catalyst loading was 10%, the contact time was 0.1s; the temperature of the catalytic reaction tube At 150°C, the reacted mixed gas enters the condenser with a cooling jacket from the gas port inlet, the temperature of the condensed water is 10°C, and the unreacted hexafluoropropylene is circulated to the catalytic reaction tube through the gas outlet. The purity of the liquid hexafluoropropylene dimer in the receiver of the condenser was detected to be 99.3%. The yield of hexafluoropropylene dimer is shown in Table 1.
Embodiment 2
[0026] Example 2: Preparation of hexafluoropropylene dimer raw materials: hexafluoropropylene gas was passed through a catalytic reaction tube equipped with AgF / C catalyst, the catalyst loading was 15%, the temperature of the catalyst packing column was 180°C, and the contact time It is 10s. The reacted mixed gas enters the condenser with cooling jacket from the air inlet, and the temperature of the condensed water is 10°C; the unreacted hexafluoropropylene is circulated to the catalytic reaction column through the outlet. The purity of the liquid hexafluoropropylene dimer in the condenser is 99.2%. The yield of hexafluoropropylene dimer after application is shown in Table 1.
Embodiment 3
[0027] Example 3: Preparation of hexafluoropropylene dimer raw materials: hexafluoropropylene gas was passed through a catalytic reaction tube equipped with KF / C catalyst, the catalyst loading was 20%, the temperature of the catalyst packing column was 220°C, and the contact time It is 30s; the reacted mixed gas enters the condenser with cooling jacket from the air inlet, the temperature of the condensed water is 10°C, and the unreacted hexafluoropropylene is circulated to the catalytic reaction tube through the outlet. The purity of the liquid hexafluoropropylene dimer in the condenser was detected to be 99.3%. The yield of hexafluoropropylene dimer after application is shown in Table 1.
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