Recovery system of dichloroethane in thiophanate-methyl production

By using a negative pressure distillation vessel and stirring unit in the production of thiophanate-methyl, combined with a demulsifier, the problem of azeotropic reaction between dichloroethane and water was solved, achieving efficient recovery and reduced energy consumption, thus improving the quality and production efficiency of dichloroethane.

CN224672102UActive Publication Date: 2026-08-25INNER MONGOLIA GUANSHIDA CHEM CO LTD
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Patent Information

Application Number
CN202521926431.0
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-09-08
Publication Date
2026-08-25
Estimated Expiration
2035-09-08

AI Technical Summary

Technical Problem

In the existing technology, during the dichloroethane recovery process in the production of methyl thiophanate, atmospheric distillation causes dichloroethane to azeotropically react with water, which increases energy consumption and easily triggers side reactions. Furthermore, the distillation of the water azeotrope wastes steam.

Method used

A distillation vessel using a negative pressure pump to provide a vacuum environment, combined with a stirring unit and a demulsifier, reduces the pressure inside the distillation vessel by negative pressure, widens the boiling point difference between dichloroethane and water, reduces the formation of azeotropes, and improves separation efficiency by using a stirring tube and a demulsifier.

Benefits of technology

This technology enables efficient recovery of dichloroethane, reduces water content and energy consumption, avoids the decomposition of methyl thiophanate due to excessively high temperatures, and improves product quality and production efficiency.

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Abstract

The application provides a recovery system of dichloroethane in thiophthalimide production, comprising a distillation kettle, a heat exchanger, a storage tank and a negative pressure pump; the top of the distillation kettle is provided with a feeding port and a gas phase outlet, the gas phase outlet is communicated with the storage tank through the heat exchanger, and the top of the storage tank is connected with the negative pressure pump; and the bottom of the distillation kettle is provided with a liquid discharge port. The application realizes efficient recovery of dichloroethane and reduces energy consumption.
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