CN102408112A - A method and equipment for purifying polysilicon by electron beam melting under a high-purity silicon substrate - Google Patents
A method and equipment for purifying polysilicon by electron beam melting under a high-purity silicon substrate Download PDFInfo
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- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 title claims abstract description 52
- 229910021420 polycrystalline silicon Inorganic materials 0.000 title claims abstract description 52
- 229910052710 silicon Inorganic materials 0.000 title claims abstract description 52
- 239000010703 silicon Substances 0.000 title claims abstract description 52
- 238000000034 method Methods 0.000 title claims abstract description 45
- 229920005591 polysilicon Polymers 0.000 title claims abstract description 43
- 238000010894 electron beam technology Methods 0.000 title claims abstract description 38
- 239000000758 substrate Substances 0.000 title claims abstract description 36
- 238000002844 melting Methods 0.000 title abstract description 9
- 230000008018 melting Effects 0.000 title abstract description 9
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 51
- 239000011574 phosphorus Substances 0.000 claims abstract description 51
- 239000002210 silicon-based material Substances 0.000 claims abstract description 29
- 238000003723 Smelting Methods 0.000 claims abstract description 27
- 239000007788 liquid Substances 0.000 claims abstract description 16
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000012535 impurity Substances 0.000 claims abstract description 14
- 239000000463 material Substances 0.000 claims abstract description 14
- 238000000746 purification Methods 0.000 claims abstract description 10
- 238000002360 preparation method Methods 0.000 claims abstract description 8
- 238000009792 diffusion process Methods 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 8
- 229910002804 graphite Inorganic materials 0.000 claims description 7
- 239000010439 graphite Substances 0.000 claims description 7
- 238000007711 solidification Methods 0.000 claims description 5
- 230000008023 solidification Effects 0.000 claims description 5
- 239000000498 cooling water Substances 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims 1
- 239000012634 fragment Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 abstract description 4
- 238000010923 batch production Methods 0.000 abstract 1
- 238000004134 energy conservation Methods 0.000 abstract 1
- 238000005272 metallurgy Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 7
- 229910052739 hydrogen Inorganic materials 0.000 description 5
- 239000001257 hydrogen Substances 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 229910000077 silane Inorganic materials 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000009776 industrial production Methods 0.000 description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- HIVGXUNKSAJJDN-UHFFFAOYSA-N [Si].[P] Chemical compound [Si].[P] HIVGXUNKSAJJDN-UHFFFAOYSA-N 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 238000009616 inductively coupled plasma Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 238000012827 research and development Methods 0.000 description 2
- 229910021422 solar-grade silicon Inorganic materials 0.000 description 2
- ZDHXKXAHOVTTAH-UHFFFAOYSA-N trichlorosilane Chemical compound Cl[SiH](Cl)Cl ZDHXKXAHOVTTAH-UHFFFAOYSA-N 0.000 description 2
- 239000005052 trichlorosilane Substances 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229910003902 SiCl 4 Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052796 boron Inorganic materials 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000011031 large-scale manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Silicon Compounds (AREA)
Abstract
Description
技术领域 technical field
本发明属于用物理冶金技术提纯多晶硅的技术领域,特别涉及一种高纯硅衬底作用下进行电子束熔炼提纯多晶硅,去除多晶硅中的杂质磷的方法;另外本发明还涉及其设备。 The invention belongs to the technical field of purifying polysilicon by physical metallurgical technology, and particularly relates to a method for purifying polysilicon by electron beam smelting under the action of a high-purity silicon substrate and removing impurity phosphorus in polysilicon; in addition, the invention also relates to its equipment.
背景技术 Background technique
太阳能电池可以将太阳能转化为电能,在常规能源紧缺的今天,太阳能具有巨大的应用价值。太阳能级多晶硅材料是制备太阳能电池片的重要原材料之一。目前,世界范围内制备太阳能电池用多晶硅材料已形成规模化生产,主要技术路线有: Solar cells can convert solar energy into electrical energy. In today's shortage of conventional energy sources, solar energy has great application value. Solar grade polysilicon material is one of the important raw materials for making solar cells. At present, the preparation of polysilicon materials for solar cells has formed a large-scale production worldwide, and the main technical routes are as follows:
(1)改良西门子法:西门子法是以盐酸(或氢气、氯气)和冶金级工业硅为原料,由三氯氢硅,进行氢还原的工艺。现在国外较成熟的技术是西门子法,并且已经形成产业。该法已发展至第三代,现在正在向第四代改进。第一代西门子法为非闭合式,即反应的副产物氢气和三氯氢硅,造成了很大的资源浪费。现在广泛应用的第三代改良西门子工艺实现了完全闭环生产,氢气、三氯氢硅硅烷和盐酸均被循环利用,规模也在1000吨每年以上。但其综合电耗高达170kw·h/kg,并且生产呈间断性,无法在Si的生产上形成连续作业。 (1) Improved Siemens method: The Siemens method uses hydrochloric acid (or hydrogen, chlorine gas) and metallurgical grade industrial silicon as raw materials to perform hydrogen reduction from trichlorosilane. Now the relatively mature technology in foreign countries is the Siemens method, and it has already formed an industry. The law has been developed to the third generation and is now being improved to the fourth generation. The first-generation Siemens method is non-closed, that is, the by-products of the reaction are hydrogen and trichlorosilane, resulting in a great waste of resources. The widely used third-generation improved Siemens process has achieved complete closed-loop production, hydrogen, trichlorohydrosilane and hydrochloric acid are all recycled, and the scale is more than 1,000 tons per year. However, its comprehensive power consumption is as high as 170kw h/kg, and the production is intermittent, so it is impossible to form a continuous operation in the production of Si.
(2)硅烷法:是以氟硅酸(H2SiF6)、钠、铝、氢气为主要原材料制取硅烷(SiH4),然后通过热分解生产多晶硅的工艺。该法基于化学工艺,能耗较大,与西门子方法相比无明显优势。 (2) Silane method: It is a process of preparing silane (SiH 4 ) with fluosilicic acid (H 2 SiF 6 ), sodium, aluminum, and hydrogen as the main raw materials, and then producing polysilicon through thermal decomposition. This method is based on a chemical process, which consumes a lot of energy, and has no obvious advantages compared with the Siemens method.
(3)流态化床法:是以SiCl4(或SiF4)和冶金级硅为原料,生产多晶硅的工艺。粒状多晶硅工艺法是流态化床工艺路线中典型的一种。但是该工艺的技术路线正在调试阶段。 (3) Fluidized bed method: It is a process for producing polysilicon with SiCl 4 (or SiF 4 ) and metallurgical grade silicon as raw materials. The granular polysilicon process is a typical one in the fluidized bed process route. But the technical route of the process is in the debugging stage.
(4)冶金法:以定向凝固等工艺手段,去除金属杂质;采用等离子束熔炼方式去除硼;采用电子束熔炼方式去除磷、碳,从而得到生产成本低廉的太阳能级多晶硅。这种方法能耗小,单位产量的能耗不到西门子法的一半,现在日本、美国、挪威等多个国家从事冶金法的研发,其中以日本JFE的工艺最为成熟,已经投入了产业化生产。 (4) Metallurgical method: use directional solidification and other technological means to remove metal impurities; use plasma beam smelting to remove boron; use electron beam smelting to remove phosphorus and carbon, so as to obtain solar-grade polysilicon with low production costs. This method consumes less energy, and the energy consumption per unit output is less than half of the Siemens method. Now Japan, the United States, Norway and other countries are engaged in the research and development of metallurgical methods. Among them, Japan's JFE technology is the most mature and has been put into industrial production. .
在众多制备硅材料的方法中,已经可以投入产业化生产的只有改良西门子法、硅烷法、冶金法。但改良西门子法和硅烷法的设备投资大、成本高、污染严重、工艺复杂,不利于太阳能电池的普及性应用,相比而言冶金法具有生产周期短、污染小、成本低的特点,是各国竞相研发的重点。电子束熔炼是冶金法提纯多晶硅的重要方法之一,它可以有效降低多晶硅中的杂质磷,但是目前电子束熔炼提纯多晶硅过程中,熔炼坩埚一般直接使用水冷坩埚,直接使用水冷坩埚不仅能量损失严重,能耗大,成本高,而且容易造成外来杂质的污染,使得多晶硅的纯度降低。 Among the many methods for preparing silicon materials, only the improved Siemens method, silane method, and metallurgical method can be put into industrial production. However, the improved Siemens method and silane method require large equipment investment, high cost, serious pollution, and complicated processes, which are not conducive to the popular application of solar cells. In comparison, the metallurgical method has the characteristics of short production cycle, low pollution, and low cost. The focus of research and development in various countries. Electron beam smelting is one of the important methods for metallurgical purification of polysilicon. It can effectively reduce the impurity phosphorus in polysilicon. However, in the current process of electron beam smelting and purification of polysilicon, water-cooled crucibles are generally used directly for melting crucibles. Direct use of water-cooled crucibles not only causes serious energy losses , high energy consumption, high cost, and easy to cause contamination by foreign impurities, which reduces the purity of polysilicon.
发明内容 Contents of the invention
本发明克服上述不足问题,提供一种高纯硅衬底下电子束熔炼提纯多晶硅的方法,先利用电子束熔炼在水冷坩埚内部形成一层高纯硅衬底,然后在此高纯硅衬底之上熔炼提纯多晶硅,减少能耗,避免坩埚的污染,有效提高多晶硅的纯度。本发明的另一目的是提供一种高纯硅衬底下电子束熔炼提纯多晶硅的设备,结构简单,操作方便,提纯效果好。 The present invention overcomes the above disadvantages and provides a method for purifying polysilicon by electron beam smelting under a high-purity silicon substrate. First, a layer of high-purity silicon substrate is formed inside a water-cooled crucible by electron beam smelting, and then Melting and purifying polysilicon, reducing energy consumption, avoiding crucible pollution, and effectively improving the purity of polysilicon. Another object of the present invention is to provide an equipment for purifying polysilicon by electron beam smelting under a high-purity silicon substrate, which has simple structure, convenient operation and good purification effect.
本发明为实现上述目的所采用的技术方案是:一种高纯硅衬底下电子束熔炼提纯多晶硅的方法,具体工艺是: The technical solution adopted by the present invention to achieve the above object is: a method for purifying polysilicon by electron beam smelting under a high-purity silicon substrate, and the specific process is:
第一步备料及预处理:首先在水冷坩埚中装满高纯硅料,关闭炉门后,抽取真空室真空至0.002Pa以下; The first step of material preparation and pretreatment: first fill the water-cooled crucible with high-purity silicon material, and after closing the furnace door, vacuum the vacuum chamber to below 0.002Pa;
第二步形成高纯硅衬底:然后开启电子束束流为200-500mA完全熔化高纯硅料,缓慢降低束流为零,即在水冷坩埚中形成高纯多晶硅锭,调节电子束束斑位于水冷坩埚中心位置,此后开启电子束束流为150-300mA熔化高纯多晶硅锭,2-5min后形成一层高纯硅衬底; The second step is to form a high-purity silicon substrate: then turn on the electron beam current of 200-500mA to completely melt the high-purity silicon material, slowly reduce the beam current to zero, that is, form a high-purity polycrystalline silicon ingot in a water-cooled crucible, and adjust the electron beam spot It is located in the center of the water-cooled crucible, and then the electron beam current is turned on at 150-300mA to melt the high-purity polysilicon ingot, and a layer of high-purity silicon substrate is formed after 2-5 minutes;
第三步熔炼提纯:最后开启加料装置,高磷硅料连续缓慢落入熔池中,此时加大束流至300-700mA,同时调节电子束束斑位置,使其右侧在熔池中熔炼,其左侧用于熔化下落中和刚落入熔池的高磷硅料,高磷硅料熔化后形成高磷硅液,高磷硅液熔炼后杂质磷得到去除,此后从导流口流入坩埚之中,得到低磷硅液,凝固后得到低磷的多晶硅锭。 The third step of smelting and purification: finally turn on the feeding device, and the high-phosphorus silicon material will continuously and slowly fall into the molten pool. At this time, increase the beam current to 300-700mA, and at the same time adjust the position of the electron beam spot so that the right side is smelted in the molten pool , the left side is used to melt the high-phosphorus silicon material that has just fallen into the molten pool. After the high-phosphorus silicon material is melted, a high-phosphorus silicon liquid is formed. After the high-phosphorus silicon liquid is smelted, impurity phosphorus is removed, and then flows into In the crucible, a low-phosphorus silicon liquid is obtained, and after solidification, a low-phosphorus polysilicon ingot is obtained.
所述第一步备料及预处理:分别采用机械泵、罗茨泵和扩散泵对设备抽取真空,将真空室抽到高真空0.002Pa以下;向水冷支撑杆、水冷坩埚及水冷支撑底座中通入冷却水,使其温度维持在30-45℃;给电子枪预热,设置高压为30-32kV,高压稳定5-10分钟后,关闭高压,设置电子枪束流为100-200mA进行预热,预热10-15分钟后,关闭电子枪束流。 The first step of material preparation and pretreatment: use mechanical pumps, Roots pumps and diffusion pumps to evacuate the equipment respectively, and evacuate the vacuum chamber to a high vacuum below 0.002Pa; Add cooling water to keep the temperature at 30-45°C; preheat the electron gun, set the high voltage to 30-32kV, after the high voltage is stable for 5-10 minutes, turn off the high voltage, set the beam current of the electron gun to 100-200mA for preheating, preheat After 10-15 minutes of heat, turn off the electron gun beam.
所述高磷硅料为碎块料或粉料。 The high phosphorus silicon material is a broken material or a powder material.
一种高纯硅衬底下电子束熔炼提纯多晶硅的设备,设备由炉门及真空炉壁构成真空设备,真空设备的内腔即为真空室;水冷支撑杆固定安装于真空炉壁底部左侧,水冷坩埚固定安装于水冷支撑杆之上,高纯硅衬底置于水冷坩埚内壁,加料装置安装于真空炉壁顶部左侧,电子枪安装于真空炉壁顶部,其下端正对水冷坩埚;水冷支撑底座固定安装于真空炉壁底部右侧,石墨块固定安装于水冷支撑底座之上,坩埚安装于石墨块之上,水冷坩埚导流口对准坩埚。 An equipment for purifying polysilicon by electron beam smelting under a high-purity silicon substrate. The equipment consists of a furnace door and a vacuum furnace wall to form a vacuum device. The inner cavity of the vacuum device is a vacuum chamber; The water-cooled crucible is fixedly installed on the water-cooled support rod, the high-purity silicon substrate is placed on the inner wall of the water-cooled crucible, the feeding device is installed on the left side of the top of the vacuum furnace wall, the electron gun is installed on the top of the vacuum furnace wall, and its lower end is facing the water-cooled crucible; water-cooled support The base is fixedly installed on the right side of the bottom of the vacuum furnace wall, the graphite block is fixedly installed on the water-cooled support base, the crucible is installed on the graphite block, and the water-cooled crucible guide port is aligned with the crucible.
所述真空炉壁上分别安装机械泵、罗茨泵、扩散泵和放气阀。 A mechanical pump, a Roots pump, a diffusion pump and an air release valve are respectively installed on the wall of the vacuum furnace.
本发明先利用电子束熔炼形成高纯多晶硅衬底,然后在此衬底作用下小束流,连续熔炼高磷的多晶硅料,快速去除多晶硅中的杂质磷。此方法中形成的高纯多晶硅衬底将熔炼的硅熔体与水冷坩埚隔离开来,取到了隔热的作用,减少了水冷坩埚带走的热量,提高了熔体底部的温度,加速了杂质磷的扩散挥发去除速率,并且高纯硅衬底减少了水冷坩埚壁上杂质对熔炼多晶硅的污染,提高多晶硅的纯度。该方法提纯效果好,工艺简单,节约能源,降低外来污染,适合批量生产。 The invention first uses electron beam melting to form a high-purity polysilicon substrate, and then continuously melts high-phosphorus polysilicon material with a small beam under the action of the substrate to quickly remove impurity phosphorus in the polysilicon. The high-purity polysilicon substrate formed in this method isolates the smelted silicon melt from the water-cooled crucible, which has the effect of heat insulation, reduces the heat taken away by the water-cooled crucible, increases the temperature at the bottom of the melt, and accelerates the removal of impurities. The diffusion volatilization removal rate of phosphorus is high, and the high-purity silicon substrate reduces the pollution of impurities on the water-cooled crucible wall to the melting polysilicon, and improves the purity of polysilicon. The method has good purification effect, simple process, energy saving, external pollution reduction, and is suitable for mass production.
本发明设备结构简单,构思独特,在水冷坩埚上熔炼得到高纯硅衬底,操作简单,成本低,可实现连续熔炼,生产效率高,适合大规模工业化生产。 The equipment of the present invention has simple structure and unique concept, and the high-purity silicon substrate is obtained by smelting on a water-cooled crucible. The operation is simple, the cost is low, continuous smelting can be realized, the production efficiency is high, and it is suitable for large-scale industrial production.
附图说明 Description of drawings
附图1为一种高纯硅衬底下电子束熔炼提纯多晶硅的设备结构简图。 Accompanying drawing 1 is a kind of schematic diagram of the equipment structure of electron beam smelting purification polysilicon under high-purity silicon substrate.
图中,1. 电子枪,2.导流口,3. 放气阀,4. 扩散泵,5. 罗茨泵,6. 机械泵,7. 真空室,8. 炉门,9. 坩埚,10. 低磷硅液,11. 石墨块,12. 水冷支撑底座,13. 真空炉壁,14. 水冷支撑杆,15. 水冷坩埚,16.高纯硅衬底,17.高磷硅液,18. 高磷硅料,19. 加料装置。 In the figure, 1. Electron gun, 2. Diversion port, 3. Vent valve, 4. Diffusion pump, 5. Roots pump, 6. Mechanical pump, 7. Vacuum chamber, 8. Furnace door, 9. Crucible, 10 . Low-phosphorus silicon liquid, 11. Graphite block, 12. Water-cooled support base, 13. Vacuum furnace wall, 14. Water-cooled support rod, 15. Water-cooled crucible, 16. High-purity silicon substrate, 17. High-phosphorus silicon liquid, 18 . High phosphorus silicon material, 19. Feeding device.
具体实施方式 Detailed ways
下面结合具体实施例及附图详细说明本发明,但本发明并不局限于具体实施例。 The present invention will be described in detail below in conjunction with specific embodiments and drawings, but the present invention is not limited to specific embodiments.
实施例1 Example 1
一种高纯硅衬底下电子束熔炼提纯多晶硅的设备,设备由炉门8及真空炉壁13构成真空设备,真空设备的内腔即为真空室7;水冷支撑底座12固定安装于真空炉壁底部右侧,石墨块11固定安装于水冷支撑底座之上,坩埚9安装于石墨块之上;水冷支撑杆14固定安装于真空炉壁底部左侧,水冷坩埚15固定安装于水冷支撑杆14之上,高纯硅衬底16置于水冷坩埚内壁,加料装置19安装于真空炉壁顶部左侧,电子枪1安装于真空炉壁顶部,其下端正对水冷坩埚,机械泵6、罗茨泵5、扩散泵4和放气阀3分别安装于真空炉壁2之上。 An equipment for purifying polycrystalline silicon by electron beam smelting under a high-purity silicon substrate. The equipment consists of a furnace door 8 and a vacuum furnace wall 13 to form a vacuum device. The inner cavity of the vacuum device is the vacuum chamber 7; the water-cooled support base 12 is fixedly installed on the vacuum furnace wall. On the right side of the bottom, the graphite block 11 is fixedly installed on the water-cooled support base, and the crucible 9 is installed on the graphite block; the water-cooled support rod 14 is fixedly installed on the left side of the bottom of the vacuum furnace wall, and the water-cooled crucible 15 is fixedly installed on the top of the water-cooled support rod 14 Above, the high-purity silicon substrate 16 is placed on the inner wall of the water-cooled crucible, the feeding device 19 is installed on the left side of the top of the vacuum furnace wall, the electron gun 1 is installed on the top of the vacuum furnace wall, and its lower end is facing the water-cooled crucible, mechanical pump 6, Roots pump 5 , Diffusion pump 4 and deflation valve 3 are installed on the vacuum furnace wall 2 respectively.
实施例2 Example 2
采用实施例1所述的设备进行高纯硅衬底下电子束熔炼提纯多晶硅的方法,其具体步骤如下: The method for purifying polysilicon by electron beam smelting under a high-purity silicon substrate using the equipment described in Example 1, the specific steps are as follows:
第一步备料及预处理:首先在水冷坩埚15中装满杂质总含量为3ppmw高纯硅料,关闭炉门8后,分别采用机械泵6、罗茨泵5和扩散泵4对设备抽取真空,将真空室7抽到高真空0.0018Pa;向水冷支撑杆14、水冷铜坩埚15及水冷支撑底座12中通入冷却水,使其温度维持在40℃;给电子枪1预热,设置高压为30kV,高压稳定5分钟后,关闭高压,设置电子枪1束流为200mA进行预热,预热15分钟后,关闭电子枪1束流; The first step of material preparation and pretreatment: first fill the water-cooled crucible 15 with high-purity silicon materials with a total impurity content of 3 ppmw, and after closing the furnace door 8, use the mechanical pump 6, Roots pump 5 and diffusion pump 4 to pump vacuum for the equipment respectively , the vacuum chamber 7 is evacuated to a high vacuum of 0.0018Pa; cooling water is introduced into the water-cooled support rod 14, the water-cooled copper crucible 15 and the water-cooled support base 12 to maintain the temperature at 40°C; preheat the electron gun 1, and set the high pressure to 30kV, after the high voltage is stable for 5 minutes, turn off the high voltage, set the electron gun 1 beam current to 200mA for preheating, and after 15 minutes of preheating, turn off the electron gun 1 beam current;
第二步形成高纯硅衬底:然后开启电子束束流为300mA完全熔化高纯硅料,此后缓慢降低束流为零,即在水冷坩埚中形成高纯多晶硅锭,调节电子束束斑使其位于水冷坩埚中心位置,此后开启电子束束流为200mA熔化高纯多晶硅锭, 5min后形成一层高纯硅衬底16; The second step is to form a high-purity silicon substrate: then turn on the beam current of the electron beam to 300mA to completely melt the high-purity silicon material, and then slowly reduce the beam current to zero, that is, form a high-purity polycrystalline silicon ingot in a water-cooled crucible, and adjust the beam spot of the electron beam so that It is located in the center of the water-cooled crucible, after which the electron beam current is turned on to 200mA to melt the high-purity polysilicon ingot, and a layer of high-purity silicon substrate 16 is formed after 5 minutes;
第三步熔炼提纯:最后开启加料装置,磷含量为17ppmw高磷硅料18连续缓慢落入熔池中,此时加大束流至400mA,同时调节电子束束斑位置,使其右侧在熔池中熔炼,其左侧用于熔化下落中和刚落入熔池的高磷硅料18,高磷硅料熔化后形成高磷硅液,高磷硅液熔炼后杂质磷得到去除,此后从导流口流入坩埚之中,得到低磷硅液,凝固后得到低磷的多晶硅锭。 The third step of smelting and purification: finally turn on the feeding device, the phosphorus content is 17ppmw high-phosphorus silicon material 18 continuously and slowly falls into the molten pool, at this time increase the beam current to 400mA, and at the same time adjust the position of the electron beam spot so that the right side is in the molten pool Melting in the pool, the left side is used to melt the high-phosphorus silicon material 18 falling and just falling into the molten pool. After the high-phosphorus silicon material is melted, a high-phosphorus silicon liquid is formed. After the high-phosphorus silicon liquid is smelted, impurity phosphorus is removed, and thereafter from The diversion port flows into the crucible to obtain a low-phosphorus silicon liquid, and after solidification, a low-phosphorus polysilicon ingot is obtained.
经ELAN DRC-II型电感耦合等离子质谱仪设备(ICP—MS)检测,其磷含量低于0.4ppmw,满足了太阳能级硅材料的使用要求。 According to ELAN DRC-II inductively coupled plasma mass spectrometer equipment (ICP-MS), its phosphorus content is lower than 0.4ppmw, which meets the requirements for the use of solar-grade silicon materials.
实施例3 Example 3
采用实施例1所述的设备进行高纯硅衬底下电子束熔炼提纯多晶硅的方法,其具体步骤如下: The method for purifying polysilicon by electron beam smelting under a high-purity silicon substrate using the equipment described in Example 1, the specific steps are as follows:
第一步备料及预处理:首先在水冷坩埚15中装满杂质总含量为2ppmw高纯硅料,关闭炉门8后,分别采用机械泵6、罗茨泵5和扩散泵4对设备抽取真空,将真空室7抽到高真空0.0015Pa;向水冷支撑杆14、水冷铜坩埚15及水冷支撑底座12中通入冷却水,使其温度维持在40℃;给电子枪1预热,设置高压为30kV,高压稳定5分钟后,关闭高压,设置电子枪1束流为100mA进行预热,预热15分钟后,关闭电子枪1束流; The first step of material preparation and pretreatment: first fill the water-cooled crucible 15 with high-purity silicon materials with a total impurity content of 2 ppmw, and after closing the furnace door 8, use the mechanical pump 6, Roots pump 5 and diffusion pump 4 to pump vacuum for the equipment respectively , pump the vacuum chamber 7 to a high vacuum of 0.0015 Pa; feed cooling water into the water-cooled support rod 14, the water-cooled copper crucible 15 and the water-cooled support base 12 to keep the temperature at 40°C; preheat the electron gun 1 and set the high pressure to 30kV, after the high voltage is stable for 5 minutes, turn off the high voltage, set the electron gun 1 beam current to 100mA for preheating, and after 15 minutes of preheating, turn off the electron gun 1 beam current;
第二步形成高纯硅衬底:然后开启电子束束流为400mA完全熔化高纯硅料,此后缓慢降低束流为零,即在水冷坩埚中形成高纯多晶硅锭,调节电子束束斑使其位于水冷坩埚中心位置,此后开启电子束束流为300mA熔化高纯多晶硅锭, 3min后形成一层高纯硅衬底16; The second step is to form a high-purity silicon substrate: then turn on the beam current of the electron beam to 400mA to completely melt the high-purity silicon material, and then slowly reduce the beam current to zero, that is, form a high-purity polycrystalline silicon ingot in a water-cooled crucible, and adjust the beam spot of the electron beam so that It is located at the center of the water-cooled crucible, after which the electron beam current is turned on to 300mA to melt the high-purity polysilicon ingot, and a layer of high-purity silicon substrate 16 is formed after 3 minutes;
第三步熔炼提纯:最后开启加料装置,磷含量为15ppmw高磷硅料18连续缓慢落入熔池中,此时加大束流至500mA,同时调节电子束束斑位置,使其右侧在熔池中熔炼,其左侧用于熔化下落中和刚落入熔池的高磷硅料18,高磷硅料熔化后形成高磷硅液,高磷硅液熔炼后杂质磷得到去除,此后从导流口流入坩埚之中,得到低磷硅液,凝固后得到低磷的多晶硅锭。 The third step of smelting and purification: finally turn on the feeding device, and the high-phosphorus silicon material 18 with a phosphorus content of 15ppmw will continuously and slowly fall into the molten pool. Melting in the pool, the left side is used to melt the high-phosphorus silicon material 18 falling and just falling into the molten pool. After the high-phosphorus silicon material is melted, a high-phosphorus silicon liquid is formed. After the high-phosphorus silicon liquid is smelted, impurity phosphorus is removed, and thereafter from The diversion port flows into the crucible to obtain a low-phosphorus silicon liquid, and after solidification, a low-phosphorus polysilicon ingot is obtained.
经ELAN DRC-II型电感耦合等离子质谱仪设备(ICP—MS)检测,其磷含量低于0.3ppmw,满足了太阳能级硅材料的使用要求。 According to ELAN DRC-II inductively coupled plasma mass spectrometer equipment (ICP-MS), its phosphorus content is lower than 0.3ppmw, which meets the requirements for the use of solar-grade silicon materials.
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103818907A (en) * | 2014-03-04 | 2014-05-28 | 黄道德 | Dephosphorizing method for solar battery polycrystalline silicon |
CN104195636A (en) * | 2014-09-01 | 2014-12-10 | 大连理工大学 | A method for quickly preparing boron master alloy by metallurgical method |
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Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060017203A1 (en) * | 2004-06-03 | 2006-01-26 | Norichika Yamauchi | Refining apparatus for scrap silicon using an electron beam |
CN102120579A (en) * | 2011-01-29 | 2011-07-13 | 大连隆田科技有限公司 | A method and equipment for efficiently and continuously melting and purifying polysilicon by electron beam |
CN102126726A (en) * | 2011-01-29 | 2011-07-20 | 大连隆田科技有限公司 | A method and equipment for efficiently purifying polysilicon powder by electron beam |
-
2011
- 2011-08-03 CN CN2011102207671A patent/CN102408112A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060017203A1 (en) * | 2004-06-03 | 2006-01-26 | Norichika Yamauchi | Refining apparatus for scrap silicon using an electron beam |
CN102120579A (en) * | 2011-01-29 | 2011-07-13 | 大连隆田科技有限公司 | A method and equipment for efficiently and continuously melting and purifying polysilicon by electron beam |
CN102126726A (en) * | 2011-01-29 | 2011-07-20 | 大连隆田科技有限公司 | A method and equipment for efficiently purifying polysilicon powder by electron beam |
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---|---|---|---|---|
CN103818907A (en) * | 2014-03-04 | 2014-05-28 | 黄道德 | Dephosphorizing method for solar battery polycrystalline silicon |
CN104195636A (en) * | 2014-09-01 | 2014-12-10 | 大连理工大学 | A method for quickly preparing boron master alloy by metallurgical method |
CN104528732A (en) * | 2014-12-25 | 2015-04-22 | 大连理工大学 | Novel device and method for reducing energy consumption of electron beam melting technology |
CN104528732B (en) * | 2014-12-25 | 2017-04-12 | 大连理工大学 | Novel device and method for reducing energy consumption of electron beam melting technology |
CN105129804A (en) * | 2015-09-01 | 2015-12-09 | 中国化学工程第六建设有限公司 | Production technology for polycrystalline silicon |
CN105129804B (en) * | 2015-09-01 | 2017-03-08 | 中国化学工程第六建设有限公司 | The production technology of polysilicon |
CN109107492A (en) * | 2018-10-29 | 2019-01-01 | 大连颐和顺新材料科技有限公司 | High-temperature transfer arc granulation equipment and method for diamond wire cutting silicon powder |
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