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Recovery method and recovery device for sulfur dioxide in sucralose chlorination reaction

A technology of sulfur dioxide and sucralose, which is applied to the recovery of sulfur dioxide in the chlorination of sucralose, the production of sucralose, and the recovery of sulfur dioxide in the chlorination of sucralose, can solve the problem of shortening the service life of cooling devices, The cooling device is highly corrosive and the water content of trichloroethane is high, so as to reduce the loss of equipment, save cost and consumption, and shorten the production cycle

Inactive Publication Date: 2018-08-07
ANHUI JINGHE IND
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  • Claims
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Problems solved by technology

Patent Publication No. CN106466548A provides a method for reclaiming liquid sulfur dioxide by cryogenic method, which saves a large amount of lye consumption and does not generate new waste, but finds that the following problems still exist in production: 1. Secondary The water content of trichloroethane in the condensed condensed gas is relatively high; 2. A small amount of HCl enters the primary condenser and the secondary condenser, which is highly corrosive to the cooling device; 3. The existence of a small amount of HCl not only shortens the cooling time of the cooling device. service life, and there are certain safety hazards

Method used

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  • Recovery method and recovery device for sulfur dioxide in sucralose chlorination reaction

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Embodiment Construction

[0019] like figure 1 As shown, a recovery device for sulfur dioxide in the chlorination reaction of sucralose adopts the following equipment in the existing process: water washing tower, water washing tower circulation condenser, water washing tower pump, gas-liquid separator, Roots blower, primary condensation Condenser, secondary condenser, recovery storage tank, canned pump;

[0020] The sucralose tail gas enters from the bottom of the washing tower through a pipeline and absorbs the washing liquid from the top of the washing tower. Another outlet at the bottom of the washing tower connects the pump of the washing tower and the circulating condenser of the washing tower to the top of the washing tower through a pipeline. Under the action of the water washing tower pump, it is condensed by the circulating condenser of the water washing tower and then participates in circular absorption; the tail gas absorbed by the water washing tower enters the gas-liquid separator through ...

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Abstract

The invention relates to a recovery method for sulfur dioxide in sucralose chlorination reaction. The method includes steps: 1, adding concentrated sulfuric acid into a drying tower, removing moisturefrom tail gas of a gas-liquid separator, and allowing dried sulfur dioxide and trichloroethane tail gas to enter a primary condenser; 2, allowing residual tail gas and condensate flowing through theprimary condenser to enter a trichloroethane separation tank, allowing sulfur dioxide and trichloroethane condensate to enter a collection tank, and enabling tail gas sulfur dioxide to enter a secondary condenser; 3, enabling tail gas and sulfur dioxide condensate flowing through the secondary condenser to enter a tertiary condenser at a temperature ranging from -25 DEG C to -30 DEG C, condensinggaseous sulfur dioxide into liquid sulfur dioxide, and sending into a recovery storage tank. The recovery method has advantages that hydrogen chloride in the tail gas is subjected to three-stage waterabsorption to obtain high-concentration hydrochloric acid while sulfur dioxide and trichloroethane in the tail gas are separated out, and accordingly the product conversion rate is increased, raw material and energy consumption is reduced, and cost is saved to the maximum extent.

Description

technical field [0001] The invention belongs to the field of food additive production, and relates to the production of sucralose, in particular to a recovery device for sulfur dioxide in the chlorination reaction of sucralose, and also relates to a recovery method for sulfur dioxide in the chlorination reaction of sucralose. Background technique [0002] Sucralose-6-ester, as a key intermediate in the production of sucralose, is prepared by chlorinating sucralose-6-ester and a chlorination reagent under suitable conditions. There are two types of commonly used chlorination reagents: one is Vi ls meier chlorination reagent, and the other is thionyl chloride / pyridine / chlorinated hydrocarbon ternary chlorination. Most domestic sucralose manufacturers use the first type of Vi lsmeier chlorination reagent as the raw material for chlorination reaction. [0003] Sulfur dioxide will be produced in the process of preparing Vi l s meier chlorinated reagent. At present, domestic tech...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B7/07C01B17/56C07C17/38C07C19/05
CPCC01B7/0706C01B17/56C07C17/38C07C19/05
Inventor 易健康徐杰
Owner ANHUI JINGHE IND
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