Method for preparing 1,1-difluoro-1,2-dichloroethane
A technology of dichloroethane and trichloroethylene, which is applied in the field of preparation of 1,1-difluoro-1,2-dichloroethane, can solve the problems of low reaction conversion rate and selectivity, and high reaction temperature, and achieve The effect of high selectivity and yield, simple method, and easy industrial production
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0019] Put 50Kg of antimony pentachloride fluorination catalyst into the 600L reactor, add 50Kg of anhydrous hydrofluoric acid into the reactor at one time, and then add 4Kg of anhydrous hydrofluoric acid every hour to raise the temperature of the reactor, and the heating time is controlled After 5 hours, when the temperature rises to about 70° C., keep the temperature constant for 3 hours to ensure that the catalyst is activated. Then open the reaction jacket freezing medium to cool the reactor for 4 hours, when the temperature drops to 45°C, drop into the reactor with trichloroethylene and anhydrous hydrofluoric acid to make a primer, and the feeding speed of trichloroethylene is 100Kg / h, the feeding rate of anhydrous hydrofluoric acid is 4 Kg / h, until the trichlorethylene feeding amount reaches 300Kg and finishes at the bottom. Then feed continuously according to trichlorethylene:anhydrous hydrofluoric acid=60:24Kg / h, control the reaction liquid level at 50%, the reaction ...
Embodiment 2
[0021] On the basis of Example 1, the continuous feeding rate ratio of trichlorethylene and anhydrous hydrofluoric acid was changed to 60:16Kg / h, and the remaining reaction conditions were the same as in Example 1. The reaction results are shown in Table 1.
Embodiment 3
[0023] On the basis of Example 1, the continuous feeding rate ratio of trichlorethylene and anhydrous hydrofluoric acid was changed to 60:20Kg / h, and the remaining reaction conditions were the same as in Example 1. The reaction results are shown in Table 1.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More