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A kind of process method for clean disposal of high arsenic hazardous waste

A technology of hazardous waste and process method, which is applied in the direction of arsenic compounds, chemical instruments and methods, sulfur preparation/purification, etc. It can solve the problems of high risk of secondary pollution, large amount of waste gas and waste water, poor adaptability of raw materials, etc., and improve the utilization of equipment High efficiency, reduced energy consumption, rapid heating effect

Active Publication Date: 2022-07-22
防城港厚旺环保科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Both the wet method and the fire method have the following problems: poor adaptability of raw materials, high disposal cost, harsh production environment, and a large amount of waste gas and wastewater will be generated during the production process; the risk of secondary pollution is extremely high, and it is not friendly to the environment

Method used

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  • A kind of process method for clean disposal of high arsenic hazardous waste
  • A kind of process method for clean disposal of high arsenic hazardous waste
  • A kind of process method for clean disposal of high arsenic hazardous waste

Examples

Experimental program
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Effect test

Embodiment 1

[0062] The soot is disposed of by the process of the present invention, specifically: the temporary storage section and the heating section of the distillation furnace are fed with hot nitrogen to raise the temperature of the material in the furnace to 280°C, and the As in the material 2 O 3 Sublimation; then heating the materials in the temporary storage section and heating section to 350 °C by nitrogen heating, so that arsenide and high-valent arsenic oxide are reduced to metallic arsenic; It is oxidized to arsenic trioxide and sublimated at 350℃; the crude arsenic trioxide is obtained by condensation and recovery.

[0063] The yield of distillation slag is 52.80%, arsenic 4.04% (calculated as arsenic), sulfur 0.26%, copper 6.12%, lead 20.68%, zinc 4.75%, bismuth 2.95%. In the crude arsenic trioxide, the volatilization rate of arsenic was 94.29% (calculated as arsenic), and copper, lead, zinc and bismuth were not lost.

Embodiment 2

[0065] The black copper powder is treated by the process of the present invention, specifically: reducing arsenide, arsenate, etc. to elemental arsenic under the low temperature condition of 350 °C; Arsenic is oxidized to As at 300-400℃ 2 O 3 Sublimation; condensation recovery to obtain crude arsenic trioxide.

[0066] The yield of distillation slag was 61.15%, arsenic was 1.86% (calculated as arsenic), and copper was 65.81%. In the crude arsenic trioxide, the volatilization rate of arsenic is 94.98% (calculated as arsenic), and copper, lead, zinc and bismuth are not lost.

Embodiment 3

[0068] Arsenic sulfide is disposed of by the process of the present invention, specifically: the raw materials are first slurried with water, and CaCO is slowly added. 3 Neutralize the powder to pH=4.5, then slowly add lime milk to neutralize to pH=7.0, then add the required amount of sodium carbonate and carbon powder, filter, dry and sieve to obtain the material, thus avoiding the distillation process generate a lot of SO 3 , in addition, the filtrate of the pressure filtration can be recycled; hot nitrogen gas is introduced into the distillation furnace to raise the temperature of the material in the furnace to 280 ° C, so that the arsenic in arsenic sulfide is reduced to elemental substance; after the reduction, the temperature is heated to 350 ° C by hot nitrogen gas , the incoming nitrogen is filled with an appropriate amount of oxygen, so that the metal arsenic is oxidized into arsenic trioxide sublimation at 350 ℃; the crude arsenic trioxide is recovered by condensatio...

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Abstract

The invention discloses a process method for cleaning and disposing of high arsenic hazardous waste, which includes the steps of raw material pretreatment, heating reduction, sublimation, condensation and the like, so as to refine the crude arsenic trioxide to obtain arsenic trioxide, metal arsenic, sulfur and other products. The method adopts the intermittent operation mode of low-temperature reduction--medium-temperature sublimation, uses nitrogen heated by an electric hot blast stove to directly heat the material, and the condensed exhaust gas is returned to the electric hot blast stove after treatment to make up for heat recycling; the method saves investment in equipment, low disposal costs, and The raw materials are highly adaptable, the arsenic volatilization rate is high, the operating conditions are mild, the degree of automation is high, and the waste gas, waste water and waste residue are zero discharged, which is easy to realize industrialized production, and conforms to the national hazardous waste disposal principle of "reduction, harmlessness, and recycling".

Description

technical field [0001] The invention belongs to the technical field of arsenic waste treatment, and in particular relates to a process method for clean disposal of high-arsenic hazardous waste. Background technique [0002] Arsenic is widely found in nature, and hundreds of arsenic minerals have been found. Arsenic-containing compounds have a strong toxic effect on the environment. With the rapid development of mining, selection, refining of heavy metal minerals and the rapid development of many industries such as coal, chemical industry, and petroleum, the output of high-arsenic hazardous waste will increase. Improper disposal will cause harm to the environment and threaten human health. . [0003] At present, there are two main methods for the disposal of high arsenic hazardous wastes: wet method and fire method. Both wet and fire disposal processes have the following problems: poor adaptability of raw materials, high disposal costs, harsh production environment, and a ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01G28/00C01B17/02C22B30/04C22B7/00A62D3/37A62D101/41
CPCC01G28/005C01B17/02A62D3/37C22B30/04C22B7/001A62D2101/40
Inventor 杨裕祥程习叶序屋余海林
Owner 防城港厚旺环保科技有限公司