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Method for recycling chloroform in process of producing methyl isocyanate

A technology of methyl isocyanate and recovery method, which is applied in the direction of chlorine/hydrogen chloride, chlorine/hydrogen chloride purification, disproportionation separation/purification of halogenated hydrocarbons, etc., can solve the problems of waste of chloroform, increase of chloroform amount, etc., achieve cost saving, simple method, Practical effect

Inactive Publication Date: 2015-04-29
安道麦股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Because chloroform is easy to produce highly toxic phosgene when exposed to light, the existing tail gas treatment method generally uses water to dissolve HCl and destroy the generated phosgene, and only recycles HCl hydrochloric acid aqueous solution
However, this method causes a large amount of waste of chloroform, and the amount of chloroform that needs to be used in the production of methyl isocyanate increases greatly

Method used

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  • Method for recycling chloroform in process of producing methyl isocyanate

Examples

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Comparison scheme
Effect test

Embodiment 1

[0012] A method for recovering chloroform in the process of producing methyl isocyanate. Methyl isocyanate is obtained by reacting phosgene with monomethylamine to generate methylcarbamoyl chloride, and then decomposing it with chloroform as a solvent. It is characterized in that: the exhaust gas after the decomposition is completed After being cooled to 30°C by the cooler, it enters the layerer. The chloroform and hydrochloric acid in the tail gas are layered in the layerer. The chloroform with a large specific gravity flows into the chloroform receiving tank to receive and circulate for the production of methyl isocyanate. Hydrochloric acid is recovered separately. When the chloroform in the chloroform receiving tank accumulates to 300-400L, the chloroform is discharged into the recovery bucket. Avoid chloroform entering the hydrochloric acid tank with hydrochloric acid. The recovery process of the tail gas is carried out under the condition of avoiding light.

Embodiment 2

[0014] A method for recovering chloroform in the process of producing methyl isocyanate. Methyl isocyanate is obtained by reacting phosgene with monomethylamine to generate methylcarbamoyl chloride, and then decomposing it with chloroform as a solvent. It is characterized in that: the exhaust gas after the decomposition is completed After being cooled to 40°C by the cooler, it enters the layerer. The chloroform and hydrochloric acid in the tail gas are layered in the layerer. The chloroform with a large specific gravity flows into the chloroform receiving tank to receive and circulate for the production of methyl isocyanate. Hydrochloric acid is recovered separately.

Embodiment 3

[0016] A method for recovering chloroform in the process of producing methyl isocyanate. Methyl isocyanate is obtained by reacting phosgene with monomethylamine to generate methylcarbamoyl chloride, and then decomposing it with chloroform as a solvent. It is characterized in that: the exhaust gas after the decomposition is completed After being cooled to 35°C by the cooler, it enters the layerer. The chloroform and hydrochloric acid in the tail gas are layered in the layerer. The chloroform with a large specific gravity flows into the chloroform receiving tank to receive and circulate for the production of methyl isocyanate. Hydrochloric acid is recovered separately.

[0017] Using the method of the present invention to treat tail gas in the process of producing methyl isocyanate and recycling chloroform can reduce the ton consumption of chloroform relative to methyl isocyanate products from 90Kg / t to 60Kg / t, greatly saving costs.

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PUM

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Abstract

The invention provides a method for recycling chloroform in a process of producing methyl isocyanate. The methyl isocyanate is prepared by reacting phosgene with monomethylamine to generate methylaminoformyl chloride, and decomposing methylaminoformyl chloride by taking chloroform as a solvent. The method for recycling chloroform in the process of producing methyl isocyanate is characterized by comprising the following steps: cooling decomposed tail gas to 30-40 DEG C by a cooler, then introducing the tail gas into a layering device, layering chloroform and hydrochloric acid in the tail gas in the layering device, enabling chloroform with high specific gravity to flow into a chloroform receiving kettle, receiving and circulating the chloroform for producing methyl isocyanate, and independently recycling hydrochloric acid with low specific gravity. The tail gas generated in the process of producing methyl isocyanate firstly flows through a falling-film absorption tower, HCl is absorbed into water, and then chloroform is quickly precipitated in a hydrochloric acid solution, so that the layering of hydrochloric acid and chloroform in the layering device is facilitated, and further hydrochloric acid and chloroform can be independently recycled; the recycled chloroform can be used for producing methyl isocyanate again; plenty of cost can be reduced. The method is simple and high in practicability.

Description

technical field [0001] The invention relates to the field of methyl isocyanate production methods, in particular to a method for recovering chloroform in the process of producing methyl isocyanate. Background technique [0002] The domestic production method of methyl isocyanate is generally at a temperature of 250-260 °C, phosgene reacts with monomethylamine to generate methylcarbamoyl chloride CH 3 After NHCOCl, it is obtained by decomposing it with chloroform as a solvent. The equation of the decomposition reaction is as follows: [0003] [0004] This method needs to use a large amount of chloroform as solvent in the production process. A large amount of chloroform and hydrochloric acid are included in the tail gas after the reaction is completed. Because chloroform is easy to produce highly toxic phosgene when exposed to light, the existing tail gas treatment method generally uses water to dissolve HCl and destroy the generated phosgene, and only recycles HCl hydro...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C19/04C07C17/38C01B7/07
Inventor 李子平许自松王成顾军
Owner 安道麦股份有限公司
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