Preparation process for sodium 1-amino-4-bromoanthraquinone-2-sulfonate

A technology of aminoanthraquinone and preparation process, applied in the chemical field, can solve the problems of affecting the quality of sodium bromamimate products, difficult to handle waste sulfuric acid, consuming more energy, etc., and achieves reduction of refining process, high utilization rate and low boiling point. Effect

Active Publication Date: 2016-11-09
南通市埃唯卡新材料有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] In the existing production process, the direct sulfonation process has many side reactions and low yield, and will produce a large amount of waste sulfuric acid that is difficult to handle
Chinese patent CN102617412.A uses the solvent method sulfonation process, which has the following disadvantages: 1. Although the o-dichlorobenzene solvent can be recycled, it will inevitably increase the impurities in the solvent after repeated use, which will affect the sodium bromide product. 2. Due to the high boiling point of o-dichlorobenzene, more energy will be consumed in the dehydration process and solvent distillation process; 3. The bromination process generally carries out the bromination reaction in 8% to 10% sulfuric acid concentration. During the bromination reaction, hydrogen bromide will be produced at the same time, and the produced hydrogen bromide needs to be absorbed by lye and then oxidized by chlorine gas to recover bromine and improve the utilization rate of bromine

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0014] (1) Sulfonation reaction: Add 450kg of dichloroethane and 4.5kg of copper sulfate into the sulfonation reaction kettle, then add 112kg (content 96%) of 1-aminoanthraquinone, seal the feeding port, heat to boiling, evaporated After the water and dichloroethane are condensed through the condenser, they enter the oil-water separator, the upper layer of oil phase dichloroethane returns to the reaction system, and the lower layer of water separates out of the reaction system. If no water is separated from the oil-water separator, it can be considered The dehydration is over, and the time is about 1 hour. After dehydration is finished, start to slowly add chlorosulfonic acid 64kg to carry out sulfonation reaction, control temperature of reaction 83 0 C~85 0 C, the system is in a slightly boiling state. After the dropwise addition, continue the heat preservation reaction at this temperature for about 3 hours. Take a sample to measure the reaction end point. After the reaction...

Embodiment 2

[0019] (1) Sulfonation reaction: Add 500kg of dichloroethane and 4.7kg of copper sulfate into the sulfonation reaction kettle, then add 112kg (content 96%) of 1-aminoanthraquinone, seal the feeding port, heat to boiling, evaporated After the water and dichloroethane are condensed through the condenser, they enter the oil-water separator, the upper layer of oil phase dichloroethane returns to the reaction system, and the lower layer of water separates out of the reaction system. If no water is separated from the oil-water separator, it can be considered The dehydration is over, and the time is about 1 hour. After dehydration is finished, start to slowly add dropwise 64kg of chlorosulfonic acid to carry out sulfonation reaction. Controlling the reaction temperature 81 0 C~83 0 C, the system is in a slightly boiling state. After the dropwise addition, continue the heat preservation reaction at this temperature for about 3.5 hours. Take a sample to measure the reaction end point...

Embodiment 3

[0024] (1) Sulfonation reaction: Add 500kg of dichloroethane and 5kg of copper sulfate into the sulfonation reaction kettle, then add 112kg of 1-aminoanthraquinone, seal the feeding port, heat to boiling, evaporated water and dichloroethane After condensing through the condenser, it enters the oil-water separator, the upper layer of oil phase dichloroethane returns to the reaction system, and the lower layer of water separates out of the reaction system. If no water is separated from the oil-water separator, it can be considered that the dehydration is complete, and the time is about 1 hours or so. After dehydration is finished, start to slowly add chlorosulfonic acid 64kg to carry out sulfonation reaction, control temperature of reaction 75 0 C~80 0 C, after the dropwise addition, continue the insulation reaction at this temperature for about 3 hours, take a sample to measure the reaction end point, after the reaction is over, cool the reaction solution to 30 0 C~50 0 C, a...

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Abstract

The invention discloses a preparation process for sodium 1-amino-4-bromoanthraquinone-2-sulfonate. The preparation process comprises the following steps: (1) sulfonation: with 1-aminoanthraquinone as a raw material, copper sulfate as a catalyst and dichloroethane as a solvent, carrying out dehydration, then adding chlorosulfonic acid drop by drop for a sulfonation reaction, adding 98% concentrated sulfuric acid after completion of the reaction, extracting 1-aminoanthraquinone-2-sulfonic acid out, allowing 1-aminoanthraquinone-2-sulfonic acid to enter the concentrated sulfuric acid, separating out an acid phase at a lower layer and subjecting the acid phase to a subsequent reaction; (2) bromination: adding bromine into the concentrated sulfuric acid solution of 1-aminoanthraquinone-2-sulfonic acid drop by drop for a reaction so as to obtain the concentrated sulfuric acid solution of bromoamine acid; (3) dilution: adding water into the concentrated sulfuric acid solution of bromoamine acid for dilution and successively carrying out cooling, crystallization and filtering so as to obtain bromoamine acid; and (4) salt formation: adding water to dissolve bromoamine acid and adding sodium sulfite to obtain bromoamine acid sodium salt. The preparation process provided by the invention can reduce energy consumption during solvent recovery; the utilization rate of bromine in bromination is high; sodium sulfite is used for salt formation, so the amount of impurities is reduced; and product quality is high.

Description

technical field [0001] The invention belongs to the field of chemical industry, in particular to a preparation process of sodium 1-amino-4-bromoanthraquinone-2-sulfonate. Background technique [0002] 1-Amino-4-bromoanthraquinone-2-sodium sulfonate, commonly known as sodium bromide, is an important intermediate with a wide range of uses in the dye manufacturing industry. It is widely used in the preparation of high-grade active, acidic, dispersing Anthraquinone-like dyes. [0003] The existing production method of sodium bromide is to use 1-aminoanthraquinone as a raw material, and it is made through sulfonation, bromination, salt formation, refining and other technological steps. Among them, the sulfonation process can be divided into direct sulfonation and solvent sulfonation processes. [0004] In the existing production process, the direct sulfonation process has many side reactions, low yield, and produces a large amount of waste sulfuric acid that is difficult to han...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C303/32C07C309/52
CPCC07C303/08C07C303/22C07C303/32C07C309/52
Inventor 赵觉新徐立群吴海霞
Owner 南通市埃唯卡新材料有限公司
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