A continuous production process of high-quality cyanide solution and its production system

A production process and production system technology, applied in the continuous production process of high-quality cyanide solution and its production system field, can solve the problem that it is difficult to meet the requirements of high-end users that the product quality is continuous and stable, and the mass transfer of hydrogen cyanide gas is insufficient. , low yield of liquid hydrocyanic acid, etc., to achieve the effect of improving product quality, reducing labor intensity of workers, and good mass transfer and heat transfer effect

Active Publication Date: 2019-12-17
HEBEI CHENGXIN
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, this patent discloses a device that obtains liquid hydrocyanic acid through deamination, pre-cooling, dehydration, and condensation liquefaction, and uses cyanide-containing tail gas to jointly produce sodium cyanide. It does not need steam when purifying and liquefying hydrocyanic acid, which reduces production. The energy consumption of hydrocyanic acid, while the tail gas is absorbed by a series of alkali-packed absorption towers, but the yield of liquid hydrocyanic acid is low
[0009] Although the above process or equipment can satisfy the preparation of hydrocyanic acid and sodium (potassium) cyanide to a certain extent, these processes all have short mass exchange time, partial solution and Insufficient mass transfer of hydrogen cyanide gas leads to incomplete partial reaction of hydrogen cyanide, which accumulates on the wall of the reaction vessel or in the dead zone of mass exchange, polymerizes and discolors, which has a periodic or long-term impact on product quality, and is difficult to meet High-end users' requirements for continuous and stable product quality have also caused a waste of resources and brought considerable economic losses to the company
Then when absorbing with water, there is a violent mass transfer process in the above-mentioned equipment and technology, thereby causing the concentration of the hydrocyanic acid aqueous solution to be low, generally only about 2%, and then going to distill to prepare liquid hydrocyanic acid, which requires high energy consumption. The cost is high, so it is urgent to develop an excellent production process and equipment to solve these long-standing technical problems

Method used

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  • A continuous production process of high-quality cyanide solution and its production system
  • A continuous production process of high-quality cyanide solution and its production system
  • A continuous production process of high-quality cyanide solution and its production system

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Hydrocyanic acid gas and 32% sodium hydroxide produced by the cracking method of light oil without purification are input into the static mixer at the same time according to the molar ratio of 1:1.01, and then enter the pipeline reactor for a reaction residence time of 20s. The temperature is 40~45℃ and the reaction pressure is 0.01~0.05MPa. Sampling and detection of sodium cyanide content at the end of the reaction is 32.11%, and free OH- content is 0.104%, reaching the end of the reaction;

[0038] The feed liquid after the above reaction is completed is introduced into the gas-liquid separator for separation, and the operating pressure of the gas-liquid separator is controlled to be -0.05~-0.06MPa. The reaction tail gas is drawn from the top of the gas-liquid separator and absorbed by 20% sodium hydroxide. The colorless and transparent finished sodium cyanide solution obtained at the bottom of the gas-liquid separator is pumped into the finished product storage tank f...

Embodiment 2

[0040] The hydrocyanic acid gas and 42% potassium hydroxide produced by the unpurified light oil cracking method are input into the static mixer at the same time according to the molar ratio of 1:1.005, and then enter the pipeline reactor for a reaction residence time of 30s. The temperature is 30~35°C and the reaction pressure is 0.05~0.08MPa. The potassium cyanide content at the end of the reaction is 40.41% and the free OH- content is 0.072% by sampling, reaching the end of the reaction;

[0041] The feed liquid after the above reaction is completed is introduced into the gas-liquid separator for separation, and the operating pressure of the gas-liquid separator is controlled to be -0.075~-0.085MPa. The reaction tail gas is drawn from the top of the gas-liquid separator and absorbed and treated with 30% potassium hydroxide. The colorless and transparent finished potassium cyanide solution obtained at the bottom of the gas-liquid separator is pumped into the finished product ...

Embodiment 3

[0043] Hydrocyanic acid gas and 32% sodium hydroxide produced by cracking light oil without purification and 32% sodium hydroxide are input into the static mixer at the same time according to the molar ratio of 1:1.02, and then enter the pipeline reactor for a reaction residence time of 10s. The temperature is 50~55℃ and the reaction pressure is 0.1~0.15MPa. Sampling and detection of sodium cyanide content at the end of the reaction is 32.06%, and free OH- content is 0.147%, reaching the end of the reaction;

[0044] The feed liquid after the above reaction is completed is introduced into the gas-liquid separator for separation, and the operating pressure of the gas-liquid separator is controlled to be -0.02~-0.04MPa. The reaction tail gas is drawn from the top of the gas-liquid separator and absorbed and treated with 20% sodium hydroxide. The colorless and transparent finished sodium cyanide solution obtained at the bottom of the gas-liquid separator is pumped into the finishe...

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Abstract

The invention relates to a high-quality cyanide solution continuous production process and a production system of the high-quality cyanide solution, and belongs to the technical field of cyanide production. The production system comprises a metering pump, a mass flowmeter, a static mixer 7, a tube reactor 8, a gas-liquid separator 11, and pipeline valves and auto control instruments of the production system. A sampling valve 9 and a pressure auto control system 10 are arranged on a pipeline; a demister is installed inside the gas-liquid separator 11; a reaction tail gas discharging opening 12 having auto pressure control is arranged on the top of the gas-liquid separator; and a material discharging pipe and a circulating returning pipeline are arranged at the bottom of the gas-liquid separator. The method is simple; continuous production can be realize; the reaction time is short; the gas-liquid contact has no dead angle; the mass and heat transfer effects are good; the absorption rate of a raw material hydrogen cyanide is close to 100%; the aggregation discoloration caused by partial aggregation of the hydrogen cyanide gas is avoided particularly; the periodic equipment cleaning process in conventional arts is avoided especially; the labor intensity of workers is decreased; the labor force is saved; the product quality is notably improved as well; the cost is reduced by a certain degree; and accordingly the production process and the production system provided by the invention have good economic and social benefits.

Description

technical field [0001] The invention relates to a continuous production process of high-quality cyanide solution and a production system thereof, belonging to the technical field of cyanide production. Background technique [0002] Cyanide series products are basic chemical raw materials with special properties and uses. They are widely used in organic synthesis, precious metal refining, electroplating, metal heat treatment, medicine, dyes, pigments, and synthetic materials (such as plexiglass, nitrile rubber, etc.) , photography, etc. In addition, it can also be used in metal abrasives, insecticides, fumigants, reducing agents, etc., and the market prospect is very broad. [0003] Cyanide series products use hydrogen cyanide as raw material, mainly including sodium cyanide, potassium cyanide, liquid hydrocyanic acid and other products. Their main production methods are divided into tank reaction process and tower reaction process. For example, "Lanhua Science and Technolo...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01C3/10C01C3/04
CPCC01C3/04C01C3/10
Inventor 张辰亮程丽华董浩浩刘少华殷军利彭艳丽李静董津张盖飞杨扬
Owner HEBEI CHENGXIN
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