Method for using trichloroethylene to prepare trifluoro-acetic chloride
A technology of trifluoroacetyl chloride and trichloroethylene, which is applied in the preparation of acyl halides, halogenated hydrocarbons, chemical instruments and methods, etc., can solve the problems of poor selectivity, difficult separation, unsafety and the like, and achieves low cost and simple process. , the effect of less environmental pollution
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0019] A method for preparing trifluoroacetyl chloride from trichlorethylene, comprising the following steps:
[0020] (1) Preparation of 1,1,1-trifluoro-2,2-dichloroethane: Trichlorethylene is fluorinated and thermally chlorinated to obtain a mixed gas, and the mixed gas enters a reaction tank equipped with activated carbon for catalysis Chlorination reaction, the reaction temperature is 180-240 ° C, the speed ratio of chlorine gas and mixed gas is controlled to be 1:10-80 during the reaction catalytic process; the gas after the reaction is washed with water and alkali, and the product is obtained by fractional distillation; the activated carbon is honeycomb activated carbon, the shape Activated carbon is pre-soaked in hydrofluoric acid solution at room temperature for 24-48 hours, then cleaned with distilled water, dried in a drying oven after cleaning, and then used to further remove water or ash with nitrogen, and then activated with chlorine for 24-36 hours;
[0021] (2) ...
Embodiment 2
[0024] The difference of embodiment 2 reaction and experiment 1 is that no shading plate is added below the gas-liquid phase interface of embodiment 2, other conditions are the same as experiment 1, TFAC accounts for 90% in the gas phase product except raw material, oxygen, chlorine and hydrogen chloride gas, altogether 0.95 mol TFAC was produced. The content of 1,1,1-trifluoro-2,2-dichloroethane in the bottom liquid is 94.14%, and the by-product CFC-113a is 6.78%. Glass corrosion was found at the gas-liquid phase interface of the reactor, the gas phase part, and the condensation return pipe.
Embodiment 3
[0026] The difference between reaction and experiment 1 in embodiment 3 is that the mercury lamp power in embodiment 3 is 200w, and other conditions are the same as experiment 1, and TFAC accounts for 96% except raw material, oxygen, chlorine and hydrogen chloride gas in the gas phase product, co-generated 0.92mol TFAC. The content of 1,1,1-trifluoro-2,2-dichloroethane in the bottom liquid is 94.32%, and the by-product CFC-113a is 5.65%. No corrosion was found in the glass of the reactor, condenser, etc.
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com