Method for producing chloromethyl ether from sucralose chlorination tail gas
A technology of sucralose and chlorinated tail gas, applied in chlorine/hydrogen chloride, chemical instruments and methods, chlorine/hydrogen chloride purification, etc., to maximize product profits, reduce processing costs, and reduce production costs
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Example Embodiment
[0020] Example 1:
[0021] Such as figure 1 As shown, the tail gas produced by the chlorination reaction of sucralose is first condensed (condensed to 1-5°C) to remove the organic solvent 1,1,2-trichloroethane in the tail gas, and then dehydrated by concentrated sulfuric acid. The hydrogen chloride and sulfur dioxide gas is pressurized to 0.6MPa by a compressor, and then sent to the freezer to be condensed to -35°C to obtain sulfur dioxide liquid and pure hydrogen chloride gas.
[0022] Add the prepared formaldehyde and methylal solution into the first-stage reaction tower, and continuously pass the hydrogen chloride gas after freezing and separation into the first-stage reaction tower, and add the prepared 37% formaldehyde and methylal into the first-stage reaction tower. The aldehyde solution is sprayed and reacted to form a chloromethyl ether solution. The temperature of the first-stage reaction tower is controlled at 5℃~12℃, and the liquid level is controlled at 35%;
[0023] Afte
Example Embodiment
[0027] Example 2:
[0028] Add the prepared 37% formaldehyde and methylal solution to the primary reaction tower, and the purified hydrogen chloride gas from the chlorination tail gas and the chloromethyl ether, formaldehyde and methylal solution from the secondary reaction tower are in a molar ratio of 1.2: 0.5: 0.5 enters the tower, the chloromethyl ether, formaldehyde, and methylal solutions from the secondary reaction tower enter from the inlet of the tower at a flow rate of 1.5m³ / h, and hydrogen chloride gas flows from the bottom gas phase at a flow rate of 60m³ / h The formaldehyde and methylal solution pre-filled at the bottom of the tower are lifted to the top of the tower by a circulating pump at the bottom of the tower for cyclic absorption. After the materials are cyclically absorbed for about 5 hours, they will be sampled and analyzed, and then continuously extracted. 2 The graphite heat exchanger cools the circulating liquid at the bottom of the tower, the temperature
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.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap