Technological method for jointly preparing liquid hydrogen cyanide and hydroxynitrile

A technology for the combined preparation of hydroxyacetonitrile, which is applied in chemical instruments and methods, the preparation of organic compounds, and the preparation of carboxylic acid nitriles. Pollution and its harm to the human body, avoidance of decomposition and aggregation, effects of clean production processes

Active Publication Date: 2015-06-24
枣阳市金鹿化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Hydrocyanic acid mixed gas greatly limits its scope of use. For example, in the synthesis of acetone cyanohydrin, in order to obtain high-purity acetone cyanohydrin, high-purity hydrocyanic acid liquid is usually used; butadiene is produced by reacting with hydrocyanic acid Adiponitrile has very high requirements for the purity of hydrocyanic acid, especially for water and oxygen in hydrocyanic acid. For the production of these compounds, hydrogen cyanide mixed gas cannot replace high-purity hydrogen Cyanic acid liquid
In order to obtain high-purity liquid hydrocyanic acid, it is inevitable to adopt the method of absorption and rectification. In the traditional hydrocyanic acid purification process, the method of absorbing hydrocyanic acid is mostly water absorption, which not only requires the absorption of hydrocyanic acid The water is frozen to a lower temperature, resulting in high energy consumption for lowering the temperature, and the concentration of hydr

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] (1) Ammonia removal: Add 35% dilute sulfuric acid aqueous solution into the dilute sulfuric acid metering tank, pass the hydrocyanic acid mixture gas obtained from light oil cracking into the ammonia removal tower from the bottom, and spray dilute sulfuric acid from the top of the ammonia removal tower at the same time, The reaction mixture is absorbed by the ammonia removal liquid countercurrently to remove the ammonia contained in it, and then comes out from the top of the ammonia removal tower; the ammonia removal liquid after absorbing ammonia is cooled and recycled, and new dilute sulfuric acid is replaced regularly;

[0026] (2) Water removal: The mixed gas of hydrocyanic acid from the top of the ammonia removal tower is passed into the cooling tower from the bottom. The cooling temperature of the cooling tower is 10°C to 20°C. Turn into condensed water and stay at the bottom of the tower, and the mixed gas of hydrocyanic acid after partial water removal comes out ...

Embodiment 2

[0030] The difference between this embodiment and embodiment 1 is:

[0031] Cancel the cooling water removal before the sulfuric acid water removal.

[0032] (1) Ammonia removal: add 35% dilute sulfuric acid aqueous solution to the ammonia removal liquid metering tank, pass the hydrogen cyanide mixture gas obtained by cracking light oil into the ammonia removal tower from the bottom, and spray dilute sulfuric acid from the top of the ammonia removal tower at the same time , the reaction mixture is absorbed by the ammonia removal liquid countercurrently to remove the ammonia contained in it, and then comes out from the top of the ammonia removal tower; the ammonia removal liquid after absorbing ammonia is cooled and recycled, and new dilute sulfuric acid is replaced regularly;

[0033](2) Dehydration: Add 70% sulfuric acid into the dehydration metering tank as a dehydrating agent, and the mixed gas of hydrocyanic acid from the top of the ammonia removal tower is passed into the...

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PUM

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Abstract

The invention provides a technological method for jointly preparing liquid hydrogen cyanide and hydroxynitrile. The technological method comprises the steps that a light oil cracking hydrogen cyanide gas mixture is used as a raw material and undergoes an ammonia removal process and a cryogenic process to obtain liquid hydrogen cyanide, wherein in the ammonia removal process, the hydrogen cyanide gas mixture is absorbed with a sulfuric acid aqueous solution; in the cryogenic process, the hydrogen cyanide gas mixture is cooled to minus 10-minus 20 DEG C, after the hydrogen cyanide gas mixture is cooled, a part of the hydrogen cyanide gas becomes liquid to obtain liquid hydrogen cyanide, and the other part of the hydrogen cyanide gas is the tail gas containing hydrogen cyanide; the tail gas containing hydrogen cyanide, which undergoes cryogenic treatment, is absorbed with a formaldehyde aqueous solution containing a catalyst to prepare a hydroxynitrile aqueous solution, and the tail gas absorbed with the formaldehyde aqueous solution directly enters an incinerator to be incinerated. By adopting the technological method, the purification efficiency and the utilization efficiency of hydrogen cyanide can be obviously improved, meanwhile, the energy consumption in the hydrogen cyanide purification process is greatly reduced and can be reduced by 90% at most, and the utilization rate of hydrogen cyanide is more than 99.9%.

Description

technical field [0001] The invention belongs to the field of chemical industry, and relates to a method for purifying hydrocyanic acid from a reaction mixture gas produced by cracking light oil and producing hydroxyacetonitrile by utilizing tail gas. Background technique [0002] Hydrocyanic acid is a widely used chemical raw material, which can be used in many fields such as medicine, pesticides, cosmetics, dyes, fertilizers, electroplating, polymer materials, photography, mining, metallurgy, etc. At present, the main production methods of hydrocyanic acid mainly include light oil cracking method, Andrussow method, BMA method and acrylonitrile by-product method. Light oil cracking is a production method in which light oil (or gasoline), liquid ammonia and caustic soda are used as the main raw materials, and petroleum coke particles and nitrogen are used as auxiliary raw materials. Mixing, preheating to 280°C, immersing the petroleum coke particle layer through the three-ph...

Claims

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Application Information

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IPC IPC(8): C07C253/00C07C255/16C01C3/04
Inventor 王友仁刘海艳杨卓华詹勇
Owner 枣阳市金鹿化工有限公司
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