Washing method of high-calcium phosphorous-removed silicon

A high-calcium, metal-silicon technology, applied in chemical instruments and methods, silicon compounds, inorganic chemistry, etc., can solve problems such as danger, low ability to extract phosphorus, spontaneous combustion and explosion

Inactive Publication Date: 2014-03-12
刘荣隆
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Studies have shown that the more calcium is added, the higher the calcium content of the solidified metal silicon, the more obvious the effect of phosphorus extraction, but the silicon with high calcium content is very dangerous. This kind of high calcium metal silicon often has A large amount of silane and hydrogen are produced, and silane will spontaneously ignite when it encounters oxygen at room temperature, and a large amount of silane and hydrogen will explode immediately. Therefore, a suitable cleaning process is necessary
[0007] A method disclosed in U.S. Patent No. 4,539,194, the calcium content in the silicon is 10,000 to 100,000 ppmw, and it is cleaned in two steps, first using FeCl 3 and HCl aqueous solution for leaching, and then HF and HNO 3 Cleaning with aqueous solution, this method fails to control the production of silane and hydrogen well, and it is easy to cause spontaneous combustion and explosion
[0008] Chin

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] The main impurities of silicon after high calcium and phosphorus removal treatment: Fe content 4230ppmw, Al content 917ppmw, Ca content 61200ppmw.

[0034] The first step is to crush the high-calcium metal silicon into 1-10mm particles, then grind to 20 mesh or more, and sieve the 100-20 mesh powder;

[0035] In the second step, the powder in the first step is soaked in hydrochloric acid with a concentration of 15wt%, the stirring speed is 80rpm, cooled by normal temperature water, the reaction time is 3 hours, the solid and liquid are separated, and washed 4 times with deionized water to obtain silicon powder and yellow The primary mixed powder of the reaction product;

[0036] The 3rd step, the primary mixing powder of the 2nd step is soaked with the potassium hydroxide of 2wt%, stirring speed 80rpm, normal temperature water cooling, reaction time 1 hour, solid-liquid separation, and wash 4 times with deionized water, obtain two grade powder;

[0037] The fourth ste...

Embodiment 2

[0042] The main impurities of silicon after high calcium and phosphorus removal treatment: Fe content 4860ppmw, Al content 850.3ppmw, Ca content 152700ppmw.

[0043] The first step is to crush the high-calcium metal silicon into 1-10mm particles, then grind to 20 mesh or more, and sieve the 100-20 mesh powder;

[0044] In the second step, the powder in the first step is soaked in hydrochloric acid with a concentration of 12wt%, the stirring speed is 80rpm, cooled by normal temperature water, the reaction time is 4 hours, the solid and liquid are separated, and washed 4 times with deionized water to obtain silicon powder and yellow The primary mixed powder of the reaction product;

[0045] The 3rd step, the primary mixing powder of the 2nd step is soaked with the potassium hydroxide of 3wt%, stirring speed 80rpm, normal temperature water cooling, reaction time 2 hours, solid-liquid separation, and wash 4 times with deionized water, obtain two grade powder;

[0046] The fourth s...

Embodiment 3

[0051] The main impurities of silicon after high calcium and phosphorus removal treatment: Fe content 5400ppmw, Al content 620.3ppmw, Ca content 196800ppmw.

[0052] The first step is to crush the high-calcium metal silicon into 1-10mm particles, then grind to 20 mesh or more, and sieve the 100-20 mesh powder;

[0053] In the second step, the powder in the first step is soaked in hydrochloric acid with a concentration of 10wt%, the stirring speed is 80rpm, cooled by normal temperature water, the reaction time is 7 hours, the solid and liquid are separated, and washed 6 times with deionized water to obtain silicon powder and yellow The primary mixed powder of the reaction product;

[0054] The 3rd step, the primary mixing powder of the 2nd step is soaked with the potassium hydroxide of 5wt%, stirring speed 80rpm, normal temperature water cooling, reaction time 2 hours, solid-liquid separation, and wash 4 times with deionized water, obtain two grade powder;

[0055] The fourth...

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PUM

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Abstract

The invention discloses a washing method of high-calcium phosphorous-removed silicon. According to the invention, high-calcium metal silicon is crushed into particles; the particles are subject to grinding and sieving, such that powder is obtained; the powder is sampled, and the calcium content is determined; the powder is soaked by using a hydrochloric acid solution; the mixture is stirred, and is subject to solid-liquid separation; the mixture is washed by using deionized water, such that primary mixed powder is obtained; the primary mixed powder is soaked by using an alkali solution; the mixture is stirred, and is subject to solid-liquid separation; the mixture is washed by using deionized water, such that secondary mixed powder is obtained; the secondary mixed powder is soaked by using a mixed acid solution of sulfuric acid and hydrofluoric acid; the mixture is stirred, and is subject to solid-liquid separation; the mixture is washed by using deionized water, such that tertiary mixed powder is obtained; the tertiary mixed powder is soaked by using a mixed acid solution of hydrochloric acid and hydrofluoric acid; the mixture is stirred, and is subject to solid-liquid separation; the mixture is washed by using deionized water, such that quaternary mixed powder is obtained; the quaternary mixed powder is subject to vacuum drying, such that low-phosphorous silicon powder is obtained. With the washing method provided by the invention, on a basis that impurities such as calcium and phosphorous are effectively removed, the generations of flammable and combustible gases are reduced, such that production can be safely preceded.

Description

technical field [0001] The invention relates to the field of polysilicon purification, in particular to a method for cleaning silicon with high calcium and phosphorus removal. Background technique [0002] At present, the requirements for the impurity content of the solar-grade silicon raw materials used in international monocrystalline manufacturing or polycrystalline foundries are as follows according to the application: [0003] use Boron (ppm) Phosphorus (ppm) TMI (ppm) Czochralski / Zone Fusion Single Crystal ≤0.06 ≤0.01 ≤0.01 Polycrystalline ingot ≤0.16 ≤0.01 ≤0.01 [0004] Note: TMI is the total metal content [0005] It can be seen from the above table that phosphorus and boron elements are of great significance to solar grade silicon. When manufacturing high-purity silicon by the Siemens method or the modified Siemens method, the removal of phosphorus and boron is very thorough, so the Siemens method or the modified Siemens method ...

Claims

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Application Information

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IPC IPC(8): C01B33/037
Inventor 刘荣隆叶联蔚
Owner 刘荣隆
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