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Novel crystallizing method of p-acetamidobenzene sulfonyl chloride

A technology of acetaminobenzenesulfonyl chloride and acetanilide, which is applied in the field of chemical purification, can solve problems such as easy scaling, long time for crystallization, uneven grain size, etc., and achieve improved quality, convenient growth speed, and grain growth process smooth effect

Inactive Publication Date: 2019-11-15
新乡市锦源化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Aiming at the deficiencies of the prior art, the present invention provides a new crystallization method for acetaminobenzenesulfonyl chloride, which has the advantages of uniform grain size, fast crystallization speed, and not easy to scale, and solves the problem that the solution is easily affected by the temperature of the cooling liquid and Problems with easy fouling, non-uniform grain size, and longer crystallization times

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] Add acetanilide and chlorosulfonic acid into the reaction kettle. The ratio of acetanilide to chlorosulfonic acid is 1:5.26. Stir acetanilide and chlorosulfonic acid to fully mix them to form a primary slurry. Stir the primary slurry The temperature is 15℃, the stirring speed of the primary slurry is 200 rpm, steam is introduced into the jacket of the reactor, the temperature of the steam in the jacket of the reactor is 61℃, and the primary slurry is heated to 60℃, and Continue to heat and stir for 2 hours. After 2 hours of reaction, a secondary slurry is formed. The secondary slurry is gradually diluted by adding ice water. The temperature of the ice water is 9℃. The ice water is distilled water, and then a tertiary slurry is formed. The temperature of the slurry is 10℃. The three-stage slurry is passed into the first-stage vacuum crystallizer, the first-stage vacuum crystallizer maintains a certain degree of vacuum, the absolute pressure in the first-stage vacuum crysta...

Embodiment 2

[0032] Add acetanilide and chlorosulfonic acid into the reaction kettle. The ratio of acetanilide to chlorosulfonic acid is 1:5.26. Stir acetanilide and chlorosulfonic acid to fully mix them to form a primary slurry. Stir the primary slurry The temperature is 15℃, the stirring speed of the primary slurry is 200 rpm, steam is introduced into the jacket of the reactor, the temperature of the steam in the jacket of the reactor is 61℃, and the primary slurry is heated to 60℃, and Continue to heat and stir for 2 hours. After 2 hours of reaction, a secondary slurry is formed. The secondary slurry is gradually diluted by adding ice water. The temperature of the ice water is 9℃. The ice water is distilled water, and then a tertiary slurry is formed. The temperature of the slurry is 10℃. The three-stage slurry is passed into the first-stage vacuum crystallizer. The first-stage vacuum crystallizer maintains a relatively high degree of vacuum. The absolute pressure in the first-stage vacuu...

Embodiment 3

[0035] Add acetanilide and chlorosulfonic acid into the reaction kettle. The ratio of acetanilide to chlorosulfonic acid is 1:5.26. Stir acetanilide and chlorosulfonic acid to fully mix them to form a primary slurry. Stir the primary slurry The temperature is 15℃, the stirring speed of the primary slurry is 200 rpm, steam is introduced into the jacket of the reactor, the temperature of the steam in the jacket of the reactor is 61℃, and the primary slurry is heated to 60℃, and Continue to heat and stir for 2 hours. After 2 hours of reaction, a secondary slurry is formed. The secondary slurry is gradually diluted by adding ice water. The temperature of the ice water is 9℃, and the ice water is distilled water. Then a tertiary slurry is formed. The temperature of the slurry is 10℃. The three-stage slurry is passed into the first-stage vacuum crystallizer, the first-stage vacuum crystallizer maintains a certain degree of vacuum, the absolute pressure in the first-stage vacuum crysta...

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Abstract

The invention relates to the technical field of chemical purification, and discloses a novel crystallizing method of p-acetamidobenzene sulfonyl chloride. The method includes the steps of adding acetanilide and chlorosulfonic acid into a reaction still to be stirred to form first-stage slurry, conducting continuous thermal insulation stirring to form second-stage slurry, adding ice water to the second-stage slurry to form third-stage slurry, introducing the third-stage slurry into a first-stage vacuum crystallizer, gradually concentrating the third-stage slurry to finally form first-stage magma, and gradually separating crystal grains out of the first-stage magma. By arranging the first-stage vacuum crystallizer and a second-stage vacuum crystallizer, the third-stage slurry and acid liquorare automatically cooled, no heat exchange face needs to be arranged, it is avoided that a large amount of crystal scales are generated by crystal grains on the heat exchange face, and the number andgrowth speed of crystal nucleus are more conveniently controlled; by means of a first-stage ultrasonic auxiliary crystallizer and a second-stage ultrasonic auxiliary crystallizer, the nucleating speed is high, the crystallizing time is shortened, and the prepared crystal grains are uniform in size.

Description

Technical field [0001] The invention relates to the technical field of chemical purification, in particular to a novel crystallization method of paraacetamidobenzenesulfonyl chloride. Background technique [0002] Paraacetamidobenzene sulfonyl chloride is an important chemical intermediate. It is a commonly used pharmaceutical intermediate for the preparation of sulfa bactericidal and fungicidal drugs. It can be used directly to synthesize dyes, and can also be used to synthesize para esters and para amino oils. Dyestuff intermediates are widely used in the fields of medicine, coatings, plastics and pesticides. At present, most of the production of acetaminobenzene sulfonyl chloride adopts the traditional process of excess chlorosulfonic acid method. The synthetic intermediate product hydrolyzed material needs to be diluted with water to precipitate For paraacetamidobenzene sulfonyl chloride crystals, a common method is to use a stirred dilution kettle, storage tank and discharge...

Claims

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Application Information

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IPC IPC(8): C07C303/44C07C303/08C07C309/88
CPCC07C303/08C07C303/44C07C309/88
Inventor 蔡红新闫玲玲陈东梅王书擘刘媛媛
Owner 新乡市锦源化工有限公司