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Purification and preparation method for solar energy polycrystalline silicon raw material

A technology of polysilicon and solar energy, which is applied in the growth of polycrystalline materials, chemical instruments and methods, crystal growth, etc., can solve the problems of high energy consumption, restrictions on the popularization and use of solar cells, and high output costs, so as to reduce energy consumption and improve The effect of high productivity and simple operation

Inactive Publication Date: 2007-10-17
晶湛(南昌)科技有限公司
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Problems solved by technology

But without exception, no matter which process method is used, the average power consumption per kilogram of polysilicon raw materials is about 250-400 degrees. High energy consumption, high input and low output are the main reasons for the high cost of polysilicon raw materials, which are seriously restricted. The widespread use of solar cells

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Embodiment Construction

[0006] The preparation method of the present invention is as follows. Firstly, the reduced metal silicon is pulverized, and then pickled with aqua regia and hydrofluoric acid. The vacuuming facility of the pulling furnace isolates the air, skips the monocrystalline silicon doping process, and increases the lifting speed of the crucible of the pulling furnace (0---30mm / h for single crystal silicon, 20-50mm / h for rough polysilicon extraction) At the same time, the vertical temperature gradient of the monocrystalline silicon pulling furnace is used to remove silicon slag impurities by using the thermal method, so as to achieve the purpose of rough purification of polysilicon raw materials, the purity reaches 99.99%, and greatly reduces energy consumption and greatly increases production capacity; after rough extraction The polysilicon material enters the zone melting furnace to form an interval temperature gradient in the zone melting furnace, and the silicon slag impurities are r...

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Abstract

A process for purifying and preparing solar (radiation) energy polycrystalline silicon raw material comprises the following steps: firstly, pulverizing metallic silicon after a deoxidize processing, then acid cleaning it with aqua regia and fluohydric acid, and transferring it into a monocrystalline silicon extraction-tensile furnace for a extraction-tensile after the acid cleaning, separating air for a purification by utilizing the monocrystalline silicon extraction-tensile furnace for creation of vacuum, after a coarse extraction, transferring the polycrystalline silicon material into a zone founding furnace wherein a interval temperature grads form, eliminating white slime impurity by adopting heat extruding method. And then, a polycrystalline silicon raw material with a purity high than 99.9999%is obtained. Said invention possesses the advantages as follows: the energy consumption is reduced for vast scale and the deliverability is raised greatly by taking full advantage of traditional process equipment such as monocrystalline silicon extraction-tensile furnace and zone founding furnace, without needing reconstructions; the less process steps and the simplicity of operation is suitable for monocrystalline silicon extraction-tensile furnace of any type.

Description

technical field [0001] The invention relates to a method for purifying and preparing solar polysilicon raw materials by using a monocrystalline silicon pulling furnace for rough extraction and then using a zone melting furnace for refining treatment. Background technique [0002] International electronic grade high purity The mainstream technology for the preparation of polysilicon raw materials is the Siemens method, that is, trichlorosilane (SiHCl 3 ) reduction method and silane (SiH 4 ) thermal decomposition method, which utilizes dry hydrogen chloride to react with metallurgical silicon powder in a fluidized bed: Si(s)+3HCl(g)=SiHCl 3 (g)+H 2 (g) (Exothermic) generated SiHCl 3 with PCI 3 and BCl 3 There is a large difference in relative volatility (their boiling points are 31.8 ° C, 74 ° C and 13 ° C, respectively, and can be effectively purified by rectification. Finally, at 1100 ° C with H 2 Reduced SiHCl 3 , the reverse process of prio...

Claims

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Application Information

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IPC IPC(8): C30B29/06C30B28/08C30B28/10
Inventor 罗应明郭力
Owner 晶湛(南昌)科技有限公司
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