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A kind of method of processing o-sulfonamidobenzoic acid methyl ester crystallization mother liquor

A technology of methyl benzoate and crystallization mother liquor, which is applied in the direction of organic chemistry, can solve the problems that methyl o-sulfonamide benzoate cannot be recovered, increases the cost of sewage treatment, and is difficult to pass, so as to achieve environmental protection and reduce sewage Disposal cost, organic matter reduction effect

Active Publication Date: 2016-02-17
三门峡环宇生化科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Because the separated waste liquid also dissolves methyl o-sulfonamide benzoate, which contains more organic matter, so that this part of methyl o-sulfonamide benzoate cannot be recovered, which will cause waste
In addition, a large amount of organic matter of methyl o-sulfonamide benzoate enters the sewage treatment system, which is difficult to pass, increases the cost of sewage treatment, and causes environmental pollution

Method used

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  • A kind of method of processing o-sulfonamidobenzoic acid methyl ester crystallization mother liquor

Examples

Experimental program
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Effect test

Embodiment 1

[0021] 3000kg from the production of methyl o-sulfonamide benzoate concentration, the crystallization mother liquor of the intermediate methyl o-sulfonamide benzoate produced in the crystallization process is vacuum pumped into the enamel distillation still of 5000L volume, and 30% sodium hydroxide solution (liquid caustic soda) is added ) to pH = 9, then heated to above 64°C, distilled methanol, stopped heating and distillation when the temperature of the kettle reached 90°C, opened the reactor jacket and circulated water to cool down to 25°C, added water to adjust the Baume degree to 8Be, filtered, Add 30% sulfuric acid to the filtrate until pH = 1, and a white powdery solid is precipitated. After qualitative analysis, the white powdery solid is insoluble saccharin. 211kg of insoluble saccharin is separated by drying, and the waste liquid flows into the sewage treatment station for treatment. After testing, the content of insoluble saccharin after drying (on a dry basis) is ...

Embodiment 2

[0023] With 300g from the intermediate methyl o-sulfonamidobenzoate crystallization mother liquor produced in the process of producing methyl o-sulfonamide benzoate crystallization refining process, vacuum into the glass still of 1000ml capacity, add potassium hydroxide to pH=9, then Heat to above 64°C, distill methanol, stop heating and distillation when the kettle temperature reaches 90°C, cool down to 23°C in a cold water bath, filter out calcium sulfate, add water to the filtrate to adjust the Baume degree to 7Be, then add 30% hydrochloric acid to When pH=1, a white powdery solid is precipitated, and the qualitative analysis shows that the white powdery solid is insoluble saccharin. Dry and separate 20.5 g of insoluble saccharin, and discard the waste liquid. After testing, the content of insoluble saccharin after drying (on a dry basis) is 98.19%.

Embodiment 3

[0025] 300g of the intermediate methyl o-sulfonamide benzoate crystallization mother liquor produced during the concentration and crystallization process from the production of methyl o-sulfonamide benzoate is vacuum pumped into a glass still with a volume of 1000ml, calcium hydroxide is added to pH=9, and then Heat to above 64°C, distill methanol, stop heating and distillation when the temperature of the kettle reaches 90°C, cool down to 24°C in a cold water bath, add water to adjust Baume to 6Be, filter, add 30% hydrochloric acid to the filtrate until pH = 1, A white powdery solid was precipitated, which was found to be insoluble saccharin through qualitative analysis. Dry and separate 20.3 g of insoluble saccharin, and discard the waste liquid. After testing, the content of insoluble saccharin after drying (on a dry basis)) is 98.06%.

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Abstract

The invention relates to a method for treating a methyl 2-(aminosulfonyl)benzoate crystallization mother solution, which comprises the following steps: performing chemical reaction on sodium hydroxide or a sodium hydroxide solution or potassium hydroxide or calcium hydroxide or calcium oxide and a methyl 2-(aminosulfonyl)benzoate crystallization mother solution generated in the concentration, crystallization or purification process during methyl 2-(aminosulfonyl)benzoate production, thus generating saccharin salt; heating to distill out methanol, cooling to 30 DEG C or below, and adding water until the Baume degree is regulated to 12Be or below; and filtering, and adding acid into the filtrate until the pH value is 1.0-2.0 to precipitate insoluble saccharin, wherein the recovered insoluble saccharin can be used as a raw material for methyl 2-(aminosulfonyl)benzoate production or saccharin sodium production. The production process of the treatment method is simple and quick in reaction and simple to operate, can lower the production cost, reduce organic substances in effluent waste water and lower the sewage treatment cost, and also can reduce environmental pollution, thereby being beneficial to environmental protection.

Description

technical field [0001] The present invention relates to a kind of processing method of the crystalline mother liquor intermediate that produces in chemical industry, especially a kind of method of processing o-sulfonamide benzoic acid methyl ester crystalline mother liquor. Background technique [0002] The crystallization mother liquor of methyl o-sulfonamide benzoate is an intermediate separated during the concentration, crystallization, or refining process of the production of methyl o-sulfonamide benzoate. apply while processing is required. [0003] The main components of the methyl o-sulfonamide benzoate crystallization mother liquor are methanol, sulfuric acid, water, dissolved methyl o-sulfonamide benzoate and impurities, and the pH of the mother liquor is less than or equal to 0.5. The method of processing the mother liquor of methyl o-sulfonamide benzoate crystallization is usually to distill out methanol by heating, then crystallize at lower temperature to separa...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07D275/06
CPCC07D275/06
Inventor 张卫民
Owner 三门峡环宇生化科技有限公司