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Method for reducing harmful materials in by-product hydrochloric acid in production process of chlorobenzene

A technology of production process and harmful substances, which is applied in the field of reducing harmful substances in by-product hydrochloric acid, can solve the problems of not meeting the production demand of hydrochloric acid, poor quality of by-product hydrochloric acid, and increasing production costs, so as to improve resource utilization and reduce production costs , the effect of reducing material loss

Inactive Publication Date: 2019-01-01
ANHUI DONGZHI GUANGXIN AGROCHEMICAL CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the traditional process of producing chlorinated benzene, benzene and chlorine gas are mixed and reacted in a chlorination reactor under the action of a catalytic iron ring catalyst. The method converts hydrochloric acid into gaseous hydrogen chloride and takes it out from the chlorination solution, and then absorbs the by-product hydrochloric acid through water, but the separated hydrogen chloride gas will entrain organic substances such as benzene and chlorinated benzene, making the quality of by-product hydrochloric acid poor, which cannot meet the requirements for hydrochloric acid. demanding production needs
A small amount of organic matter remaining in the by-product hydrochloric acid is taken out of the system with the hydrochloric acid, resulting in waste of raw materials and increasing production costs. At the same time, the brought in organic matter causes unsafe hidden dangers in the hydrochloric acid system

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] The method for reducing harmful substances in the by-product hydrochloric acid in the chlorinated benzene production process of this embodiment: pressurize the atmospheric pressure hydrogen chloride gas separated from the chlorinated benzene system to 0.08MPa by a Roots blower, and condense it through a primary condenser. Condensate water and low-boiling point substances, and separate them through the gas-liquid separator. The gaseous hydrogen chloride will continue to be pressurized to 1MPa through the compressor, and the organic impurities will be further removed by the secondary condenser, and then enter the adsorption tower from the bottom of the adsorption tower equipped with adsorbents. , the qualified hydrogen chloride gas is produced from the top of the tower, the hydrogen chloride gas is absorbed by the absorption tower to obtain the qualified by-product hydrochloric acid, which is cooled by the cooler and then enters the hydrochloric acid storage tank, and the r...

Embodiment 2

[0019] The method for reducing harmful substances in the by-product hydrochloric acid in the chlorinated benzene production process of this embodiment: pressurize the atmospheric pressure hydrogen chloride gas separated from the chlorinated benzene system to 0.12MPa by a Roots blower, and condense it through a primary condenser. Condensate water and low-boiling point substances, and separate and treat them through the gas-liquid separator. The gaseous hydrogen chloride is further pressurized to 1.5MPa through the compressor, and the organic impurities are further removed through the secondary condenser, and then enters the adsorption tower from the bottom of the adsorption tower equipped with adsorbents. Qualified hydrogen chloride gas is produced from the top of the tower, and the hydrogen chloride gas is absorbed by the absorption tower to obtain qualified by-product hydrochloric acid, which is cooled by the cooler and then enters the hydrochloric acid storage tank, and the re...

Embodiment 3

[0021] The method for reducing harmful substances in the by-product hydrochloric acid in the chlorinated benzene production process of this embodiment: pressurize the normal pressure hydrogen chloride gas separated from the chlorinated benzene system to 0.1 MPa by a Roots blower, and condense it through a primary condenser. Condensate water and low-boiling point substances, and separate them through the gas-liquid separator. The gaseous hydrogen chloride will continue to be pressurized to 1.2MPa through the compressor, and the organic impurities will be further removed by the secondary condenser. Qualified hydrogen chloride gas is produced from the top of the tower, and the hydrogen chloride gas is absorbed by the absorption tower to obtain qualified by-product hydrochloric acid, which is cooled by the cooler and then enters the hydrochloric acid storage tank, and the recovered benzene series organic matter enters the benzene recovery tank and returns to the chlorination process...

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PUM

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Abstract

The invention provides a method for reducing harmful materials in by-product hydrochloric acid in a production process of chlorobenzene. The method comprises the following steps: compressing normal-temperature hydrogen chloride gas separated by a chlorobenzene system to 0.08-0.12MPa through a Roots blower, condensing the hydrogen chloride gas through a primary condenser, condensing water and low-boiling-point materials, separating the hydrogen chloride gas through a gas-liquid separator, then continuously compressing the hydrogen chloride gas to 1-1.5MPa through a compressor, condensing the hydrogen chloride gas through a secondary condenser for further removing organic impurities, filling the hydrogen chloride gas into an adsorption tower from the bottom of the adsorption tower with adsorbent, removing other impurities to obtain qualified hydrogen chloride gas, absorbing the qualified hydrogen chloride gas through water and then obtaining industrial pure hydrochloric acid. The purityof hydrogen chloride obtained by the method is high; the quality of the by-product hydrochloric acid is high; the wastewater is not generated; the enterprise income is increased; meanwhile, the methodis simple in process and easy to operate; the benzene-series organic matters recycled from the by-product hydrochloric acid enter a benzene recycling tank and return to the chlorination process for recycling, so that the material loss is reduced, and the production cost is reduced.

Description

technical field [0001] The invention relates to the technical field of pesticide production, in particular to a method for reducing harmful substances in by-product hydrochloric acid in the production process of chlorinated benzene. Background technique [0002] Chlorobenzene, also called chlorobenzene, is a colorless, transparent, volatile liquid with a bitter almond smell. Melting point -45.6°C, boiling point 131.6°C, relative density 1.107 (20 / 4°C), refractive index 1.5248, flash point 23°C, autoignition point 637.78°C, flammable. The explosion limit in air is 1.83-9.23% (volume). Insoluble in water, easily soluble in alcohol, ether, benzene and chloroform, etc. Toxic, moderately toxic. [0003] Chlorinated benzene is an important basic organic synthesis raw material, used as dyes, medicines, pesticides, and organic synthesis intermediates. It is used in the manufacture of phenol, nitrochlorobenzene, dinitrochlorobenzene, aniline, nitrophenol and the pesticide DDT, et...

Claims

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Application Information

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IPC IPC(8): C01B7/19
CPCC01B7/197
Inventor 陈永贵黄中桂蔡小林袁晓林杨镭王先武罗立忠袁树林章子虎张俊丁锐
Owner ANHUI DONGZHI GUANGXIN AGROCHEMICAL CO LTD
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