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A post-processing method for preparing hydroquinone by diazotization hydrolysis method of p-aminophenol

A technology of p-aminophenol and hydroquinone, applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., can solve the problems of difficult operation, pipeline blockage and energy consumption, etc., achieve simple process and reduce production cost With environmental pressure, the effect that there is little tar

Active Publication Date: 2014-10-29
JIANGSU RUIXIANG CHEM +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The object of the present invention is to further improve the post-treatment steps of the process for preparing hydroquinone by diazotization hydrolysis of p-aminophenol, solve the problem of pipeline blockage caused by sublimation crystallization and the increase of energy consumption caused by high vacuum precipitation , difficult problems

Method used

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  • A post-processing method for preparing hydroquinone by diazotization hydrolysis method of p-aminophenol
  • A post-processing method for preparing hydroquinone by diazotization hydrolysis method of p-aminophenol

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] (1) Combine 800g of the extracted oil phase of the reaction part (the content of hydroquinone is 3.5%, the content of impurities is 0.39%) and 480g of the extracted oil (the content of hydroquinone is 10.27%), and the mixture obtained from the above combination is 1280g, of which methyl The content of isobutyl ketone is 93%. Then, under the condition of nitrogen protection, desolvate DS1 to a concentration of 40% under normal pressure, and then slowly lower the temperature to 25°C to crystallize hydroquinone in methyl isobutyl ketone, and recover 963.6g of methyl isobutyl ketone And 23g precipitation recovery water;

[0035] (2) After separating the crystallization mixture from F1, 49.5g of crude hydroquinone and 254.8g of crystallization mother liquor were obtained;

[0036](3) Add 110g of raffinate water, 1.5g of activated carbon, 0.6g of sodium metabisulfite, 0.1g of zinc powder, and 0.3g of sulfuric acid to 49.5g of crude hydroquinone for decolorization DC. After h...

Embodiment 2~5

[0042] Different stripping temperatures were adopted, and other operating conditions were the same as in Example 1, and the obtained results are shown in Table 1.

[0043] Table 1 Effect of stripping temperature on stripping efficiency

[0044]

Embodiment 6

[0046] (1) Merge the extracted oil phase of 800g reaction part (the content of hydroquinone is 3.5%, miscellaneous

[0047] content of 0.39%) and 545g of extracted oil (hydroquinone content is 8.89%), the above combined 1345g of the resulting mixture, the content of n-butyl acetate in the mixture is 93.4%. Then under the condition of nitrogen protection, desolvate DS1 to a concentration of 35% at normal pressure, and then slowly cool down to 20°C to crystallize hydroquinone in n-butyl acetate, recover 1056.8g of n-butyl acetate solvent and 34g desolvent Dissolve water;

[0048] (2) After separating the crystallization mixture from F1, 52.7g of crude hydroquinone and 232.1g of crystallization mother liquor were obtained;

[0049] (3) Add 110g of raffinate water, 1.5g of activated carbon, 0.6g of sodium thiosulfate, 0.1g of zinc powder, and 0.3g of hydroquinone to 52.7g of crude hydroquinone for decolorization DC. Reflux for 1 hour; then separate F2 while it is hot, wash the f...

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Abstract

The invention provides a post-treatment method of hydroquinone prepared by diazotization and hydrolysis of paraaminophenol. The post-treatment method comprises the following steps of: (1) combining extraction oil phase extracted and separated from a reaction part with extraction oil from a step (6), desolventizing under the protection of nitrogen to a certain concentration, slowly cooling to a preset temperature, and crystallizing hydroquinone in a solvent; (2) separating crystal mixed liquid to obtain a crude product and a crystallization mother liquor; (3) decolorizing the hydroquinone crude product, carrying out heat separation, recrystallizing, separating, and drying to obtain hydroquinone; (4) carrying out back extraction to transfer hydroquinone in the crystallization mother liquor to a water layer obtained after back extraction; (5) desolventizing an oil layer obtained after back extraction to recover the solvent, and discharging kettle residues at the same time; and (6) combining the water layer obtained after back extraction with the recrystallizing mother liquor and extracting with the recovered solvent. The method provided by the invention has the advantages of simple flow, low investment, no need for negative-pressure high-temperature process, less tar, low energy consumption, high yield, low requirement on raw material purity, no wastewater generation and easiness in industrialization; the quality of the obtained product meets the national standard; and in particular, the solvent and water are well recycled, zero discharge is realized, and the production cost and environmental protection pressure are reduced.

Description

technical field [0001] The present invention relates to a method for refining hydroquinone, more specifically, relates to a method for preparing high-purity hydroquinone from the diazotization hydrolysis reaction product of p-aminophenol. Background technique [0002] Hydroquinone, also known as hydroquinone (HQ), is a commonly used chemical raw material. It is an important raw material, intermediate and auxiliary agent for medicine, pesticides, dyes and rubber. It is mainly used to prepare developer and anthraquinone dye , azo dyes, rubber antioxidants and monomer polymerization inhibitors, food stabilizers and coating antioxidants, petroleum anticoagulants, synthetic ammonia catalysts, etc., are widely used. [0003] The industrial production methods of hydroquinone mainly include aniline oxidation method, p-diisopropylbenzene oxidation method, phenol acetone method and phenol hydroxylation method. The hydroquinone product produced by the aniline oxidation reaction needs ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C39/08C07C37/70C07C37/72
Inventor 王根林顾志强徐林丁克鸿刘补娥杨进倪世春
Owner JIANGSU RUIXIANG CHEM