Controllable polymerization method and device of hexafluoropropene trimer
A technology of hexafluoropropylene trimer and hexafluoropropylene, applied in chemical instruments and methods, preparation of halogenated hydrocarbons, organic chemistry, etc., can solve the problems of cumbersome post-processing and achieve low cost, strong controllability, and utilization rate-boosting effect
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Embodiment 1
[0018] Embodiment 1: Preparation of raw material of hexafluoropropylene trimer: pass hexafluoropropylene gas through a catalytic reaction tube equipped with NaF / Al2O3 catalyst, the loading capacity of the catalyst is 10%, the temperature of the catalytic reaction tube of the catalyst is 260 ° C, contact The time is 0.1s; the reacted mixed gas enters the condenser with a 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 of the catalyst through the outlet. The purity of the liquid hexafluoropropylene trimer in the condenser was detected to be 99.3%. The yield of hexafluoropropylene trimer is shown in Table 1.
Embodiment 2
[0019] Example 2: Preparation of raw materials for hexafluoropropylene trimer: pass hexafluoropropylene gas through a catalytic reaction tube equipped with an AgF / C catalyst, the loading of the catalyst is 15%, the temperature of the catalytic reaction tube of the catalyst is 300 ° C, contact The time is 10s; the reacted mixed gas enters the condenser with a 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 of the catalyst through the outlet. The purity of the liquid hexafluoropropylene trimer in the condenser is 99.3%. The yield of hexafluoropropylene trimer after applying mechanically is shown in Table 1.
Embodiment 3
[0020] Example 3: Preparation of raw materials for hexafluoropropylene trimer: pass hexafluoropropylene gas through a catalytic reaction tube equipped with a KF / C catalyst, the loading of the catalyst is 20%, the temperature of the catalyst catalytic reaction tube is 320 ° C, contact The time is 30s; the reacted mixed gas enters the condenser with a cooling jacket through the air inlet, the temperature of the condensed water is 10°C, and the unreacted hexafluoropropylene is circulated to the catalytic reaction tube of the catalyst through the outlet. The purity of the liquid hexafluoropropylene trimer in the condenser is 99.3%. The yield of hexafluoropropylene trimer after applying mechanically is shown in Table 1.
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