A kind of trapping device and process for the production of o-chlorobenzonitrile

A technology of o-chlorobenzonitrile and process, which is applied in the field of trapping devices for the production of o-chlorobenzonitrile, can solve the problems of difficult cooling of circulating spray water, high cost of wastewater treatment, and large amount of wastewater treatment.

Active Publication Date: 2021-03-26
常州新日催化剂股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Chinese patents CN201384868 Y and CN101954231 B both adopt the trapping method of water spraying. The biggest problem of this trapping method is that the amount of wastewater to be treated is large, the cost of wastewater treatment is very high, and it is difficult to cool down the circulating spray water
At present, the domestic production of aromatics with nitrile groups and halogenated aromatics by the ammonia oxidation method is mainly thin-walled capture. This capture method is labor-intensive for workers and the working environment on site is harsh, and continuous discharge of products cannot be achieved. , a large amount of wastewater treatment

Method used

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  • A kind of trapping device and process for the production of o-chlorobenzonitrile
  • A kind of trapping device and process for the production of o-chlorobenzonitrile
  • A kind of trapping device and process for the production of o-chlorobenzonitrile

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Experimental program
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Effect test

Embodiment 1

[0034] A trapping device for the production of o-chlorobenzonitrile, comprising a primary trap, a secondary trap, a tertiary trap, a quadruple trap, a rectification tower, a product tank, and a waste water treatment device and tail gas treatment device, the o-chlorobenzonitrile high-temperature mixed product from the reactor enters the primary trap through the feed inlet of the primary trap, and the gas outlet at the top of the primary trap is connected to the The feed port of the secondary trap is connected, the gas outlet at the top of the secondary trap is connected with the feed port of the tertiary trap, the gas outlet at the top of the tertiary trap is connected with the The feed inlet of the four-stage trap is connected, and the gas outlet on the top of the four-stage trap is connected with the tail gas treatment device;

[0035] The discharge port at the bottom of the primary trap is connected to the feed port of the first melting layered tank, the discharge port above...

Embodiment 2

[0051] The difference between embodiment 2 and embodiment 1 is that (two) trapping section:

[0052] S1: The high-temperature mixed product of o-chlorobenzonitrile from the reactor enters the primary trap. At this time, the spray device accurately sprays the refrigerant inside the primary trap according to the temperature of the inlet of the primary trap and the inlet air volume. The eluate was evaporated and cooled, and 77.54g of ammonium chloride solid and 54g of o-chlorobenzonitrile liquefied condensation were precipitated in the primary trap, and the solid-liquid mixture produced in the primary trap was dissolved and washed with 500g hot water at 50°C. layer, in which the upper aqueous phase is cooled and then centrifuged to separate the ammonium chloride solid product and centrifugate, which is used as a solvent for the solid-liquid mixture produced in the primary trap, and the lower organic phase is sent to the rectification tower for purification to obtain purity ≥99.5%...

Embodiment 3

[0058] The difference between embodiment 3 and embodiment 1 is that (two) trapping section:

[0059] S1: The high-temperature mixed product of o-chlorobenzonitrile from the reactor enters the primary trap. At this time, the spray device accurately sprays the refrigerant inside the primary trap according to the temperature of the inlet of the primary trap and the inlet air volume. Evaporate and cool down the eluent, 86.25g of ammonium chloride solid and 118.8g of o-chlorobenzonitrile liquefaction condensation are precipitated in the primary trap, and the solid-liquid mixture produced in the primary trap is dissolved and washed in 500g hot water at 50°C Layering, wherein the upper aqueous phase is cooled and centrifuged to separate the ammonium chloride solid product and centrifugate, the centrifugate is used as a solvent for the solid-liquid mixture generated in the primary trap, and the lower organic phase is sent to the rectification tower for purification to obtain The liqui...

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Abstract

The invention discloses a trapping device and process for production of o-chlorobenzonitrile. The device is simple and reasonable in structural design, high in implementation feasibility and high in practicability, 90% or above of ammonium chloride is captured through a first-stage catcher by a dry capture method, 70% or above of the o-chlorobenzonitrile is captured through a second-stage catcherby a dry capture method,, the first-stage catcher makes full use of latent heat of vaporization of water, and the usage amount of spray liquid-water is small. Besides, about 30% of crude o-chlorobenzonitrile products captured by a third-stage catcher and a fourth-stage catcher is molten with hot water, dehydrated, rectified and purified to obtain an o-chlorobenzonitrile liquid pure product, and the tar generation amount and the solid waste generation amount in the rectification process are small. Compared with a traditional multi-stage wet capture method, the loss amount of the o-chlorobenzonitrile is reduced. Besides, the investment cost of rectification equipment is reduced by more than half, the rectification energy consumption is equivalent to 30% of that of the traditional method, andthe economic benefits are good.

Description

technical field [0001] The invention relates to the technical field of pharmaceutical synthesis, in particular to a trapping device and process for the production of o-chlorobenzonitrile. Background technique [0002] O-chlorobenzonitrile (CBN) is an important intermediate in organic synthesis, mainly used in the synthesis of dye intermediate 2-cyano-4-nitroaniline, and in the pharmaceutical industry for the synthesis of new antimalarial drug nitroquine and various anti-inflammatory and bactericidal drugs , for the preparation of non-peptide anti-angiotensin, etc., and can also be used for the preparation of important carbon steel corrosion inhibitors, etc. [0003] The production of 2-cyano-4-nitroaniline in my country is mainly used for the synthesis of disperse dyes and as a pesticide intermediate: o-chlorobenzonitrile can be nitrated and ammonolysis (aminated) to obtain 2-cyano-4-nitro Aniline, 2-cyano-4-nitroaniline is an important intermediate in the synthesis of dispe...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C255/50C07C253/34
CPCC07C253/34C07C255/50
Inventor 刘先国胡佳魏士新王康军邹红旭陈鹏徐伟金亮
Owner 常州新日催化剂股份有限公司
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