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Treatment method and system of byproduct hydrochloric acid in chlorination process of toluene or chloro-toluene

A by-product hydrochloric acid, production process technology, applied in the direction of chlorine/hydrogen chloride, chlorine/hydrogen chloride purification, chemical instruments and methods, etc., can solve problems that affect the economic benefits of chlorine products, fail to meet industrial requirements, pollute the environment, and achieve realization Effects of circular economy development, resource conservation and environmental protection

Pending Publication Date: 2018-04-06
NANJING ZHONGTENG CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] In the chlorination industry, especially in the production process of toluene and chlorotoluene chlorination, a large amount of by-product hydrogen chloride (HCl) will be produced. Most of these chlorine gases absorb by-product hydrochloric acid with water, because of containing a certain amount of organic impurities, toluene and chlorotoluene, It does not meet the industrial requirements, and its use is greatly restricted. In some areas, it is even discharged directly after neutralization with alkali, which not only affects the economic benefits of chlorine product production, but also causes waste of resources and pollutes the environment. This method is no longer sustainable.

Method used

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Embodiment 1

[0028] see figure 1 , a treatment system for by-product hydrochloric acid in the chlorination production process of toluene or chlorotoluene, comprising an extraction tower 1, a carbon fiber adsorption tower 2, a storage tank 3, a steam generating device, a condenser 4 and an extraction tank 5, the extraction tower The heavy liquid outlet of 1 is connected with the liquid inlet at the bottom of the carbon fiber adsorption tower 2, and the liquid outlet at the top of the carbon fiber adsorption tower 2 is connected with the storage tank 3; the steam generating device ( figure 1 Not shown in ) is connected with the desorption gas inlet of carbon fiber adsorption tower 2 through steam inlet pipe, the desorption gas outlet of carbon fiber adsorption tower 2 bottom is connected with the intake inlet of condenser 4, and the condensate outlet of condenser 4 is connected with The inlet of the extraction tank 5 is connected, and the outlet of the oil phase of the extraction tank 5 is m...

Embodiment 2

[0033] A kind of processing method of by-product hydrochloric acid in the production process of toluene chlorination, comprises the steps:

[0034] 1) The by-product hydrochloric acid from the toluene chlorination system (including toluene 31-33W / W%, chlorotoluene 31-33W / W% and hydrochloric acid 31-33W / W%) enters from the light liquid inlet at the top of the extraction tower 1, The extraction agent benzene enters from the heavy liquid inlet at the bottom of the extraction tower 1, and the weight ratio of the by-product hydrochloric acid to the extraction agent is 8:5. They are contacted countercurrently in the extraction tower. The temperature in the extraction tower is controlled to be 40°C and the pressure is 0.15Mpa. Benzene absorbs toluene and chlorotoluene in the by-product hydrochloric acid, extracts from the light liquid inlet at the top of the extraction tower, and extracts the raffinate from the heavy liquid outlet of the tower still;

[0035] 2) The raffinate phase e...

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Abstract

The invention discloses a treatment method and system of the byproduct hydrochloric acid in the chlorination process of toluene or chloro-toluene. The byproduct hydrochloric acid produced by a tolueneor chloro-toluene chlorination system enters an extraction tower from the top of the extraction tower, the extractant enters the extraction tower from the bottom of the extraction tower, the hydrochloric acid and the extractant make countercurrent contact with each other in the extraction tower, the extractant absorbs the organic matter in the byproduct hydrochloric acid, and is extracted out from the top of the extraction tower, the raffinate is extracted out from the bottom of the extraction tower, and is fed into the lower part of a carbon fiber adsorption tower, the carbon fiber adsorbs the extractant from the raffinate, after adsorption, the hydrochloric acid purification products, the raffinate, reaches the industrial grade, and is discharged from the top of the carbon fiber adsorption tower into a storage tank; when the carbon fiber penetrates, the carbon fiber adsorption tower is desorbed by water vapor, the high temperature water vapor containing extractant enters a condenserfor condensation, the condensate enters the extraction tank for oil and water separation, the recovered oil is returned to the extraction tower. According to the method, the byproduct hydrochloric acid is treated and reaches the quality requirement of industrial grade, resources are saved, the circular economy development is realized, and environment is protected.

Description

technical field [0001] The invention relates to the field of recovery, utilization and treatment of by-products in the chemical production process, in particular to a treatment method and system for by-product hydrochloric acid in the chlorination production process of toluene or chlorotoluene. Background technique [0002] In the chlorination industry, especially in the production process of toluene and chlorotoluene chlorination, a large amount of by-product hydrogen chloride (HCl) will be produced. Most of these chlorine gases absorb by-product hydrochloric acid with water, because of containing a certain amount of organic impurities, toluene and chlorotoluene, It does not meet the industrial requirements, and its use is greatly limited. In some areas, it is even discharged directly after neutralization with alkali, which not only affects the economic benefits of chlorine product production, but also causes waste of resources and pollutes the environment. This method is no...

Claims

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Application Information

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IPC IPC(8): C01B7/07
CPCC01B7/0718C01B7/0731
Inventor 陈秀珍黄敏朱旭辉陆敏山蔡伟忠束立军
Owner NANJING ZHONGTENG CHEM
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