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

Pending Publication Date: 2020-09-15
ANHUI JINGHE IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The purpose of the present invention is to solve the defects caused by the treatment of sucralose chlorination tail gas into hydroc

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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

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PUM

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Abstract

The invention relates to a method for producing chloromethyl ether from sucralose chlorination tail gas. The method comprises the following steps: a, carrying out primary condensation, concentrated sulfuric acid dehydration and pressurized separation on tail gas generated by a sucralose chlorination reaction, and then condensing to -35 DEG C or below to obtain a sulfur dioxide liquid and a pure hydrogen chloride gas; b, continuously introducing the hydrogen chloride gas into a primary reaction tower, and carrying out a circular spraying reaction on the hydrogen chloride gas, formaldehyde and amethylal solution to form a chloromethyl ether solution; c, continuously layering the chloromethyl ether solution extracted from the bottom of the primary reaction tower to obtain a chloromethyl ether crude product; and d, rectifying and purifying the chloromethyl ether crude product to obtain chloromethyl ether with the purity of 99.5% and the water content of less than 100 ppm. The method has the following advantages: the reaction efficiency of hydrogen chloride can reach 95%, the high-quality chloromethyl ether product can be obtained, the industrial chain of a company is extended, and thetreated tail gas can be discharged after reaching the standard; and the treatment cost of the waste hydrochloric acid is greatly reduced.

Description

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Claims

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Application Information

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Owner ANHUI JINGHE IND
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