The Synthetic Method and Application of Bis(2,2,2-Trifluoroethyl) Ether
The technology of a trifluoroethyl group and a synthesis method is applied in the application of lithium battery electrolyte solution and the field of fluorinated organic solvent fluorinated ether, which can solve the problems of difficult storage of production raw materials, less than 99% purity, and high equipment performance requirements, Achieve the effect of increasing competitiveness, reducing production costs and reducing equipment costs
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
preparation example Construction
[0029] The synthetic method of two (2,2,2-trifluoroethyl) ethers comprises the following steps:
[0030] 1) Preparation of 1,1,1-trifluoro-2-chloroethane;
[0031] Preferably, as an implementable manner, the preparation of 1,1,1-trifluoro-2-chloroethane also includes the following steps:
[0032] S1 Add the catalyst to the 1,1,1-trifluoro-2-chloroethane reactor first, and when the temperature of the reactor reaches 100°C with steam, feed hydrogen fluoride, trichloroethylene, and chlorine gas into the reactor at a certain rate Continuously add raw materials to the reactor, control the pressure of the reactor to 0.7-0.8Mpa, and control the reaction temperature to 100-115°C.
[0033] It should be noted that the catalyst used in this step is a catalyst commonly used for halogenated alkanes, which may be antimony pentachloride or other metal halides.
[0034] Preferably, in this step, the ventilation rate is: hydrogen fluoride<250L / h, trichlorethylene<180L / h, chlorine gas 12-15Kg...
Embodiment 1
[0049]The catalyst antimony pentachloride is added to the 1,1,1-trifluoro-2-chloroethane reactor in advance, and when the temperature of the reactor is heated to 100°C with steam, hydrogen fluoride <250L / h, trichloroethylene <180L / h, chlorine gas 12-15Kg / h, continuously add raw materials into the reactor, control the pressure of the reactor to 0.7-0.8Mpa, and the reaction temperature to 100-115°C. Open the valve to the gas buffer tank, and control the temperature of the reaction bubbler to be 65-85°C. Open the water inlet valve of the condenser and control the top temperature of the condenser to 40-45°C. Start the cryogenic system to cool and collect the exhaust gas. The collected crude 1,1,1-trifluoro-2-chloroethane is rectified in a rectification tower to remove alkali and washed with water, and then sent to the alkali hydrolysis section.
[0050] Add 550kg ethylene glycol, 1.1kg potassium hydroxide, 100kg trifluoroethanol in the pressure reactor, seal the reactor, and pa...
Embodiment 2
[0052] The catalyst antimony pentachloride is added to the 1,1,1-trifluoro-2-chloroethane reactor in advance, and when the temperature of the reactor is heated to 100°C with steam, hydrogen fluoride <250L / h, trichloroethylene <180L / h, chlorine gas 12-15Kg / h, continuously add raw materials into the reactor, control the pressure of the reactor to 0.7-0.8Mpa, and the reaction temperature to 100-115°C. Open the valve to the gas buffer tank, and control the temperature of the reaction bubbler to be 65-85°C. Open the water inlet valve of the condenser and control the top temperature of the condenser to 40-45°C. Start the cryogenic system to cool and collect the exhaust gas. The collected crude 1,1,1-trifluoro-2-chloroethane is rectified in a rectification tower to remove alkali and washed with water, and then sent to the alkali hydrolysis section.
[0053] Add 500kg ethylene glycol, 1.0kg potassium hydroxide, 100kg trifluoroethanol to the pressure reactor, seal the reactor, and p...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More - R&D
- Intellectual Property
- Life Sciences
- Materials
- Tech Scout
- Unparalleled Data Quality
- Higher Quality Content
- 60% Fewer Hallucinations
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2025 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com