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Method of separating and recycling SiO2 and ammonium fluorosilicate from fluorine-containing dust

A technology of silicon dioxide and ammonium fluorosilicate, applied in the directions of silicon dioxide, silicon oxide, fluorosilicic acid, etc., can solve the problems of high processing cost, difficult separation and recovery of valuable components, secondary pollution, etc., and achieve the production process. Simple process, reduce evaporation of solution, reduce the effect of waste liquid treatment

Active Publication Date: 2018-12-04
SHENZHEN SHENTOU ENVIRONMENT TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The semiconductor industry produces a large amount of this kind of fluorine-containing ammonium silicate, ammonium fluoride and silica dust every year. The particles of this kind of dust are small, the specific surface area is large and fluffy, and it is easy to form a gel when it meets water, and it is difficult to separate and recover valuable components.
At present, the industry mainly adopts lime neutralization method to remove fluorine for this kind of fluorine-containing dust, but it will produce a large amount of calcium fluoride slag and silica slag, the amount of sludge is large, the treatment cost is high, and it is easy to cause secondary pollution

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] Take a batch of CVD fluorine-containing dust, measure 3 parts with whiteness lower than 80%, and 7 parts with whiteness ≥ 80%, which are regarded as two types.

[0030] First, add the two types of fluorine-containing dust obtained in the above step into different leaching tanks separately, heat water to dissolve, control the leaching liquid-solid ratio to 1:2, heat the solution to 90°C during the process, and fully stir and leaching for 2 hours.

[0031] Next, filter the leach slurry obtained in the above step while it is hot or press filter, and separate the leachate and filter residue.

[0032] Again, mix the leaching solution obtained in the above step, and put it into the crystallization reactor to cool and crystallize. The cooling crystallization temperature is 40°C. After sufficient crystallization, separate the crystal and the crystallization mother liquor.

[0033] Then, repeat the above steps for secondary leaching and secondary crystallization, the leaching li...

Embodiment 2

[0036] Take a batch of CVD fluorine-containing dust, measure 2 parts with whiteness lower than 80%, and 8 parts with whiteness ≥ 80%, which are regarded as two types.

[0037] First, add the two types of fluorine-containing dust obtained in the previous step into separate leaching tanks, add ammonium fluorosilicate crystallization mother liquor (20°C crystallization mother liquor) to dissolve, control the ratio of leaching liquid to solid to 1:5, and heat during the process Solution to 60 ° C, fully stirred and leached for 1h.

[0038] Next, filter the leach slurry obtained in the above step while it is hot or press filter, and separate the leachate and filter residue.

[0039] Again, mix the net filtrate obtained in the above step, and add it to the crystallization reactor for cooling and crystallization. The cooling crystallization temperature is 20°C. After sufficient crystallization, separate the crystals and the crystallization mother liquor.

[0040] Then, repeat the ab...

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PUM

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Abstract

The invention provides a method of separating and recycling SiO2 and ammonium fluorosilicate from fluorine-containing dust, which includes: 1) independently adding two types of fluorine-containing dust, which are sorted according to whiteness of 80%, respectively to different leaching troughs, adding water, circulating washing liquid or crystallization mother liquid for dissolution, wherein the solution is heated during the process with complete stirring, thus leaching the substance; 2) filtering or press-filtering the leached slurry while hot, and separating a leachate and filter residue; 3)adding the leachate into a crystallization kettle for cooling crystallization, and after the substance is completely crystallized, separating the crystal and the crystallization mother liquid; 4) carrying out heat-leaching to the filter residue with the crystallization mother liquid again and performing secondary cooling crystallization; 5) performing multistage countercurrent washing to the filter residue, produced from the material with whiteness being higher than 80%, and drying and crushing the product to obtain SiO2; 6) mixing the crystallization mother liquid and primary concentrated washing liquid of the filter residue, and performing evaporative concentration-cooling crystallization to a part of the solution to obtain the ammonium fluorosilicate.

Description

technical field [0001] The invention relates to a fluorine-containing waste treatment technology in hazardous waste treatment, in particular to a method for separating and recovering silicon dioxide and ammonium fluorosilicate from fluorine-containing ammonium silicate dust after chemical vapor deposition tail gas treatment. Background technique [0002] Chemical vapor deposition technology (Chemical Vapor Deposition, referred to as CVD) is a new technology for the preparation of inorganic materials developed in recent decades. Chemical vapor deposition has been widely used to purify substances, develop new crystals, and deposit various single crystal, polycrystalline or glassy inorganic thin film materials. These materials can be oxides, sulfides, nitrides, carbides, or binary or multi-component interelement compounds, and their physical functions can be precisely controlled by the deposition process of vapor phase doping. At present, the materials prepared by CVD technolo...

Claims

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Application Information

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IPC IPC(8): C01B33/18C01B33/10
CPCC01B33/103C01B33/18C01P2006/80
Inventor 米永红周兆安张赫刘达马千里苏渊益钟淼鸣
Owner SHENZHEN SHENTOU ENVIRONMENT TECH CO LTD
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