TW201917237A - Method for manufacturing silicon single crystal - Google Patents

Method for manufacturing silicon single crystal Download PDF

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TW201917237A
TW201917237A TW107125107A TW107125107A TW201917237A TW 201917237 A TW201917237 A TW 201917237A TW 107125107 A TW107125107 A TW 107125107A TW 107125107 A TW107125107 A TW 107125107A TW 201917237 A TW201917237 A TW 201917237A
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exhaust port
gas
single crystal
exhaust
silicon single
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TW107125107A
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TWI682077B (en
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金原崇浩
片野智一
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日商Sumco股份有限公司
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    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
    • C30B15/00Single-crystal growth by pulling from a melt, e.g. Czochralski method
    • C30B15/14Heating of the melt or the crystallised materials
    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
    • C30B15/00Single-crystal growth by pulling from a melt, e.g. Czochralski method
    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
    • C30B29/00Single crystals or homogeneous polycrystalline material with defined structure characterised by the material or by their shape
    • C30B29/02Elements
    • C30B29/06Silicon
    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
    • C30B35/00Apparatus not otherwise provided for, specially adapted for the growth, production or after-treatment of single crystals or of a homogeneous polycrystalline material with defined structure

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)

Abstract

To provide a method for manufacturing a silicon single crystal capable of efficiently evacuating gas containing CO and reducing Cs within the silicon single crystal. A silicon single crystal manufacturing method for manufacturing a silicon single crystal by using a pulling apparatus having a chamber, a quartz crucible 3A provided in the chamber, and a heater 5 arranged so as to surround the quartz crucible 3A and heating the quartz crucible 3A, wherein an upper vent 16A for exhausting the gas introduced into the pulling device from the upper portion of the heater 5 and a lower vent 16B for exhausting from the lower portion of the heater 5 are formed in the pulling apparatus, wherein 1:3 ≤ volume of the gas exhausted via the upper vent 16A: volume of the gas exhausted via the lower vent 16B ≤ 6:1.

Description

矽單結晶的製造方法Manufacturing method of silicon single crystal

本發明係關於矽單結晶的製造方法。The present invention relates to a method for producing a silicon single crystal.

矽單結晶中的Cs,在元件製程中成為Ci,再和Oi結合形成CiOi缺陷。CiOi缺陷會成為引起元件不良的原因。在此,已知可以藉由控制從爐内加熱器、石墨坩堝等地高溫碳構件混入到原料熔液中的CO的汙染速度、以及CO從原料熔液的蒸發速度,來降低結晶中的碳濃度。再者,來自高溫碳構件的CO(gas)係基於下記反應式而產生。 SiO(gas)+2C(solid)→CO(gas)+SiC(solid)Cs in the silicon single crystal becomes Ci in the device manufacturing process, and then combines with Oi to form CiOi defects. CiOi defects can cause component failure. Here, it is known that carbon in crystals can be reduced by controlling the pollution rate of CO that is mixed into the raw material melt from high-temperature carbon members such as furnace heaters and graphite crucibles, and the evaporation rate of CO from the raw material melt. concentration. The CO (gas) from the high-temperature carbon member is generated based on the following reaction formula. SiO (gas) + 2C (solid) → CO (gas) + SiC (solid)

因此,在專利文獻1揭露一種技術,其將氬氣等的惰性氣體從拉引裝置的上方導入石英坩堝内,將含有CO的氣體導向較加熱器上端靠上方、並較其下端靠下方,使其從拉引裝置的下方排出。 先行技術文獻 專利文獻:Therefore, Patent Document 1 discloses a technology that introduces an inert gas such as argon into a quartz crucible from above the pulling device, and directs a gas containing CO above the upper end of the heater and below the lower end of the heater, so that It is discharged from under the pulling device. Prior technical literature Patent literature:

專利文獻1:日本特開平05-319976號公報Patent Document 1: Japanese Patent Application Laid-Open No. 05-319976

發明欲解決的問題Invent the problem to be solved

但是,前記專利文獻1所記載的技術中,由於上方的排氣口位於高位置,所以無法充分進行從上方排氣口的排氣,未必能夠有效率地將含有CO的氣體排氣。因此,有無法充分降低矽單結晶中的Cs的課題。However, in the technique described in the aforementioned patent document 1, since the upper exhaust port is located at a high position, exhaust from the upper exhaust port cannot be performed sufficiently, and it is not always possible to efficiently exhaust a gas containing CO. Therefore, there is a problem that Cs in the silicon single crystal cannot be sufficiently reduced.

本發明提供矽單結晶的製造方法,其能夠有效率地使得含有CO的氣體排氣,以降低矽單結晶中的Cs。 解決問題的手段The invention provides a method for manufacturing silicon single crystal, which can efficiently exhaust a gas containing CO to reduce Cs in the silicon single crystal. Problem solving

本發明的矽單結晶的製造方法,其係為使用具備反應室、設置於前記反應室内的石英坩堝、及配置為包圍前記石英坩堝並將前記石英坩堝加熱的加熱器之拉引裝置,以製造矽單結晶的矽單結晶的製造方法,在前記拉引裝置形成將已被導入前記拉引裝置内的氣體從前記加熱器的上部排氣的上部排氣口、以及從前記加熱器的下部排氣的下部排氣口;其中,1:3≦從前記上部排氣口之氣體的排氣量:從前記下部排氣口之氣體的排氣量≦6:1。 在本發明中,1:2≦從前記上部排氣口之氣體的排氣量:從前記下部排氣口之氣體的排氣量≦3:1為佳。The method for producing a silicon single crystal according to the present invention is to use a quartz crucible provided with a reaction chamber, the quartz crucible provided in the pre-reaction chamber, and a pulling device arranged to surround the pre-quartz crucible and heat the pre-quartz crucible to produce A method for manufacturing a silicon single crystal of a silicon single crystal includes forming an upper exhaust port for exhausting gas that has been introduced into the former drawing apparatus from the upper part of the former heater, and exhausting the lower part of the former heater from the upper part of the former heater. The lower exhaust port of the gas; where 1: 3 ≦ the exhaust volume of the gas from the upper exhaust port of the previous record: the exhaust volume of the gas from the lower exhaust port of the previous record ≦ 6: 1. In the present invention, it is preferable that 1: 2 ≦ the exhaust gas amount from the upper exhaust port in the foregoing description: the exhaust gas amount from the lower exhaust port in the previous description ≦ 3: 1.

依據此發明,使得從上部排氣口排氣的氣體之排氣量為1:3≦從上部排氣口之氣體的排氣量:從下部排氣口之氣體的排氣量≦6:1,藉此,能夠使得從上部排氣口的排氣優先進行。因此,能夠有效率地排出流入石英坩堝内的矽熔液表面的含有CO的氣體,能夠降低矽單結晶中的Cs。 尤其,使其為1:2≦從上部排氣口之氣體的排氣量:從下部排氣口之氣體的排氣量≦3:1,藉此能夠有效率地排出石英坩堝内的含有CO的氣體。According to this invention, the exhaust volume of the gas exhausted from the upper exhaust port is 1: 3 ≦ the exhaust volume of the gas exhausted from the upper exhaust port: the exhaust volume of the gas exhausted from the lower exhaust port ≦ 6: 1 With this, it is possible to make the exhaust from the upper exhaust port preferential. Therefore, the CO-containing gas flowing into the surface of the silicon melt in the quartz crucible can be efficiently discharged, and Cs in the silicon single crystal can be reduced. In particular, it is set to 1: 2 ≦ the exhaust gas volume from the upper exhaust port: the exhaust gas volume from the lower exhaust port ≦ 3: 1, so that the CO contained in the quartz crucible can be efficiently discharged. gas.

本發明中以此為佳:藉由改變各排氣口的開口面積,而調整從前記上部排氣口及前記下部排氣口之氣體的排氣量。 依據此發明,只要改變上部排氣口及下部排氣口的開口面積,就能夠調整各排氣口之氣體的排氣量,所以能夠簡單地調整從上部排氣口及下部排氣口之氣體的排氣量。In the present invention, this is preferable: by changing the opening area of each exhaust port, the amount of gas exhausted from the upper exhaust port and the lower exhaust port of the preamble is adjusted. According to this invention, as long as the opening areas of the upper and lower exhaust ports are changed, the amount of gas exhausted from each exhaust port can be adjusted, so the gas from the upper and lower exhaust ports can be easily adjusted. Displacement.

本發明中以此為佳:前記拉引裝置具備排氣流路,其係為配置於前記反應室内,形成了前記上部排氣口及前記下部排氣口,由碳構件所構成。 依據此發明,拉引裝置具備排氣流路,藉此含有CO的氣體不會漏出到其他部位而可以進行排氣,能夠確實降低被拉引的矽單結晶中的Cs。In the present invention, it is preferable that the pre-drawing device includes an exhaust flow path, which is arranged in the pre-reaction chamber, forms the pre-exhaust upper exhaust port and the pre-lower exhaust vent, and is composed of a carbon member. According to this invention, the pulling device has an exhaust flow path, so that the gas containing CO can be exhausted without leaking to other parts, and Cs in the drawn silicon single crystal can be reliably reduced.

[1]矽單結晶的拉引裝置1之構造 圖1中顯示了表示可適用本發明的實施形態之矽單結晶的製造方法的矽單結晶拉引裝置1之構造的一例的模式圖。拉引裝置1,係為依據丘克拉斯基法拉引矽單結晶10的裝置,其具備構成外廓的反應室2、及配置於反應室2之中心部的坩堝3。 坩堝3,係為由内側的石英坩堝3A和外側的石墨坩堝3B構成的雙層構造,其固定於可回轉及升降的支持軸4之上端部。[1] Structure of silicon single crystal pulling device 1 FIG. 1 is a schematic diagram showing an example of a structure of a silicon single crystal pulling device 1 to which a method for manufacturing a silicon single crystal according to an embodiment of the present invention can be applied. The pulling device 1 is a device for pulling silicon single crystals 10 according to the Chuklasky method, and includes a reaction chamber 2 constituting an outer profile, and a crucible 3 disposed at a center portion of the reaction chamber 2. The crucible 3 has a double-layer structure composed of an inner quartz crucible 3A and an outer graphite crucible 3B, and is fixed to an upper end portion of the support shaft 4 which can be rotated and raised.

在坩堝3的外側設置了圍住坩堝3的阻抗加熱式的加熱器5,在其外側設置有沿著反應室2的内面作為外筒的隔熱材6。 在坩堝3的上方設置了在與支持軸4同軸上依逆方向或同一方向以所定速度回轉的金屬絲等的拉引軸7。在此拉引軸7的下端安裝了種結晶8。A resistance heating heater 5 surrounding the crucible 3 is provided on the outside of the crucible 3, and a heat insulating material 6 along the inner surface of the reaction chamber 2 as an outer tube is provided on the outside. Above the crucible 3 is provided a pulling shaft 7 of a wire or the like which rotates at a predetermined speed coaxially with the support shaft 4 in the reverse direction or the same direction. A seed crystal 8 is attached to the lower end of the pulling shaft 7.

在反應室2内配置了筒狀的熱遮蔽體12。 熱遮蔽體12的作用為:對於育成中的矽單結晶10,遮擋來自坩堝3内的矽熔液9或加熱器5或坩堝3的側壁之高溫的輻射熱,並且對於作為結晶成長界面的固液界面的附近,抑制向外部的熱擴散,控制單結晶中心部及單結晶外周部的拉引軸方向之溫度梯度。 另外,熱遮蔽體12也有作為整流筒的功能,其藉由從爐上方導入的惰性氣體將來自矽熔液9的蒸發部向爐外排氣。A cylindrical heat shield 12 is arranged in the reaction chamber 2. The role of the heat shield 12 is to: for the silicon single crystal 10 being grown, shield the high temperature radiant heat from the silicon melt 9 in the crucible 3 or the heater 5 or the side wall of the crucible 3, and for the solid-liquid as the interface for crystal growth In the vicinity of the interface, thermal diffusion to the outside is suppressed, and the temperature gradient in the direction of the pull axis of the single crystal central portion and the single crystal outer peripheral portion is controlled. In addition, the heat shield 12 also functions as a rectifier, and exhausts the evaporation portion from the silicon melt 9 to the outside of the furnace by an inert gas introduced from above the furnace.

在反應室2的上部設置了將氬氣(以下稱為Ar氣體)等的惰性氣體導入到反應室2内的氣體導入口13。在反應室2的下部設置了藉由未圖示的真空泵之驅動而將反應室2内的氣體吸引並排出的排氣口14。 從氣體導入口13導入到反應室2内的惰性氣體,在育成中的矽單結晶10和熱遮蔽體12之間下降,經過熱遮蔽體12的下端和矽熔液9的液面的縫隙之後,朝向熱遮蔽體12的外側、再向坩堝3的外側流動,之後於坩堝3的外側下降,從排氣口14排出。A gas introduction port 13 for introducing an inert gas such as argon (hereinafter referred to as an Ar gas) into the reaction chamber 2 is provided in the upper part of the reaction chamber 2. An exhaust port 14 is provided at the lower portion of the reaction chamber 2 to suck and discharge the gas in the reaction chamber 2 by driving of a vacuum pump (not shown). The inert gas introduced into the reaction chamber 2 from the gas introduction port 13 descends between the silicon single crystal 10 and the heat shield 12 during the incubation, and passes through the gap between the lower end of the heat shield 12 and the liquid surface of the silicon melt 9 , Flows toward the outside of the heat shield 12, and then flows toward the outside of the crucible 3, and then descends outside the crucible 3 and is discharged from the exhaust port 14.

使用此種拉引裝置1製造矽單結晶10時,在將反應室2内維持在減壓下的惰性氣體環境的狀態下,藉由加熱器5的加熱使得填充於坩堝3的多結晶矽等的固形原料熔融,以形成矽熔液9。在坩堝3内形成矽熔液9時,使拉引軸7下降將種結晶8浸漬於矽熔液9中,使坩堝3及拉引軸7依所定方向回轉,同時將拉引軸7緩緩拉引,藉此育成與種結晶8相連的矽單結晶10。When a silicon single crystal 10 is produced using such a pulling device 1, the polycrystalline silicon and the like filled in the crucible 3 are heated by the heater 5 while the inside of the reaction chamber 2 is maintained under an inert gas atmosphere under reduced pressure. The solid material is melted to form a silicon melt 9. When the silicon melt 9 is formed in the crucible 3, the pulling shaft 7 is lowered, and the seed crystal 8 is immersed in the silicon melt 9, the crucible 3 and the pulling shaft 7 are rotated in a predetermined direction, and the pulling shaft 7 is slowly By pulling, a silicon single crystal 10 connected to the seed crystal 8 is produced.

[2]排氣流路的構造 圖2及圖3中顯示形成於前述拉引裝置1的排氣流路之構造。圖2為垂直方向剖面圖,圖3為水平方向剖面圖。 排氣管15由如圖3所示般由剖面C字狀的長尺構件所構成,排氣管15的C字的凸緣先端接合於配置在加熱器5外側的内筒16。排氣管15配置為,設置在内筒16周邊的4處,以石英坩堝3A的中心為中心,相鄰的排氣管15成90°角度。[2] Structure of Exhaust Flow Path FIG. 2 and FIG. 3 show the structure of the exhaust flow path formed in the pulling device 1 described above. FIG. 2 is a vertical sectional view, and FIG. 3 is a horizontal sectional view. The exhaust pipe 15 is composed of a long member having a C-shaped cross section as shown in FIG. 3. The C-shaped flange of the exhaust pipe 15 is joined to the inner tube 16 disposed outside the heater 5 at the tip. The exhaust pipe 15 is disposed at four positions around the inner cylinder 16, with the center of the quartz crucible 3A as the center, and the adjacent exhaust pipes 15 are at an angle of 90 °.

内筒16為由石墨等的碳構件構成的圓筒狀體。在内筒16上,如圖2所示般,於加熱器5的上端之上方形成上部排氣口16A,於加熱器5的下端之下方形成下部排氣口16B。 4支排氣管15的4個上部排氣口16A之氣體的排氣量及下部排氣口16B之氣體的排氣量為,1:3≦從上部排氣口16A的氣體的排氣量:從下部排氣口16B的氣體的排氣量≦6:1,較佳為,1:2≦從上部排氣口16A的氣體的排氣量:從下部排氣口16B的氣體的排氣量≦3:1。The inner tube 16 is a cylindrical body made of a carbon member such as graphite. As shown in FIG. 2, in the inner cylinder 16, an upper exhaust port 16A is formed above the upper end of the heater 5, and a lower exhaust port 16B is formed below the lower end of the heater 5. The exhaust gas volume of the four upper exhaust ports 16A and the lower gas exhaust port 16B of the four exhaust pipes 15 is 1: 3 ≦ the exhaust gas volume of the gas from the upper exhaust port 16A : Exhaust gas from the lower exhaust port 16B ≦ 6: 1, preferably 1: 2 ≦ exhaust gas from the upper exhaust port 16A: exhaust gas from the lower exhaust port 16B The amount is ≦ 3: 1.

再者,本實施形態中將排氣管15設置於4處,但並非以此為限,也可以為3處,也可以為8處,只要有複數排氣管15即可。另外,上部排氣口16A及下部排氣口16B的氣體的排氣量,可以藉由改變上部排氣口16A及下部排氣口16B的開口面積來加以調整。Furthermore, in this embodiment, the exhaust pipes 15 are provided at four places, but it is not limited thereto, and may be three or eight, as long as there are a plurality of exhaust pipes 15. In addition, the gas exhaust amounts of the upper exhaust port 16A and the lower exhaust port 16B can be adjusted by changing the opening areas of the upper exhaust port 16A and the lower exhaust port 16B.

在此種排氣流路中,從石英坩堝3A之上部的氣體導入口13(參照圖1)導入的惰性氣體係沿著矽熔液9的熔液表面向外側擴散,含有CO的氣體則沿著石英坩堝3A的内周面上升。 然後,如圖2所示含有CO的氣體的一部分流入由内筒16及熱遮蔽體12圍住的空間,形成高CO氣體濃度環境區域。此高CO氣體濃度環境區域内的含有CO的氣體,從上部排氣口16A進入排氣管15的内部,向下方流動並從排氣口14排出。In such an exhaust flow path, the inert gas system introduced from the gas introduction port 13 (see FIG. 1) above the quartz crucible 3A diffuses outward along the melt surface of the silicon melt 9, and the gas containing CO flows The inner peripheral surface of the quartz crucible 3A rises. Then, as shown in FIG. 2, a part of the CO-containing gas flows into the space surrounded by the inner tube 16 and the heat shield 12 to form a high CO gas concentration environment region. The CO-containing gas in the high CO gas concentration environment region enters the inside of the exhaust pipe 15 from the upper exhaust port 16A, flows downward, and is discharged from the exhaust port 14.

另一方面,含有CO的氣體的另外一部分,流過加熱器5的内側,如圖2所示般,在坩堝3的下方形成高CO氣體濃度環境區域。此CO氣體濃度環境區域内之含有CO的氣體,從下部排氣口16B進入排氣管15的内部,向下方流動並從排氣口14排出。 而且,藉由調整從上部排氣口16A排氣的氣體的排氣量、和從下部排氣口16B排氣的氣體的排氣量,能夠有效率地排出流入石英坩堝3A内的矽熔液9之表面之含有CO的氣體,結果能夠降低拉引得到的矽單結晶10中的Cs。 [實施例]On the other hand, another part of the CO-containing gas flows through the inside of the heater 5 and, as shown in FIG. 2, an environment region with a high CO gas concentration is formed below the crucible 3. The CO-containing gas in the CO gas concentration environment region enters the inside of the exhaust pipe 15 from the lower exhaust port 16B, flows downward, and is discharged from the exhaust port 14. Furthermore, by adjusting the amount of gas exhausted from the upper exhaust port 16A and the amount of gas exhausted from the lower exhaust port 16B, the silicon melt flowing into the quartz crucible 3A can be efficiently discharged. The gas containing CO on the surface of 9 can reduce Cs in the silicon single crystal 10 obtained by drawing. [Example]

繼之,說明本發明的實施例。再者,本發明並不限定於以下説明的實施例。 [1]由於排氣位置造成的矽單結晶10之碳濃度的變化 使用實施形態中已説明的矽單結晶10的拉引裝置1,改變從上部排氣口16A、下部排氣口16B的排氣流路,拉引矽單結晶10,並測定已拉引的矽單結晶10中的碳濃度。Next, embodiments of the present invention will be described. The present invention is not limited to the embodiments described below. [1] Change in carbon concentration of silicon single crystal 10 due to exhaust position Using the pulling device 1 of silicon single crystal 10 described in the embodiment, the discharge from the upper exhaust port 16A and the lower exhaust port 16B is changed. The air flow path pulls the silicon single crystal 10 and measures the carbon concentration in the pulled silicon single crystal 10.

實施例:使上部排氣口16A為開、下部排氣口16B為開。再者,使得從上部排氣口16A的氣體的排氣量:從下部排氣口16B的氣體的排氣量=4:1。 比較例1:使上部排氣口16A為閉、下部排氣口16B為開。 比較例2:使上部排氣口16A為開、下部排氣口16B為閉。 再者,在實施例及比較例1、2中,原料補充量為400kg,拉引390kg的矽單結晶10。另外,使氬氣流量為200L/min,使爐内壓為4000Pa(將30Torr換算後的値)。結果顯示如圖4。Example: Make the upper exhaust port 16A open and the lower exhaust port 16B open. In addition, the exhaust amount of the gas from the upper exhaust port 16A: the exhaust amount of the gas from the lower exhaust port 16B = 4: 1. Comparative Example 1: The upper exhaust port 16A is closed and the lower exhaust port 16B is opened. Comparative Example 2: The upper exhaust port 16A was opened and the lower exhaust port 16B was closed. In addition, in Examples and Comparative Examples 1 and 2, the raw material replenishment amount was 400 kg, and 390 kg of silicon single crystal 10 was pulled. In addition, the argon gas flow rate was set to 200 L / min, and the furnace internal pressure was set to 4000 Pa (30 Torr converted into krypton). The results are shown in Figure 4.

從圖4可知,可確認相較於比較例1的僅有下排氣的情況,在實施例的上+下排氣的情況下,矽單結晶10中的碳濃度大幅降低。 另一方面,比較例2的僅有上排氣的情況,其矽單結晶10中的碳濃度較比較例1的僅有下排氣的情況還要增加。這是因為,由石英坩堝3A及石墨坩堝3B的反應而產生的CO氣體都被吸到上部,所以矽熔液9附近的CO濃度上升,其結果導致矽單結晶10中的碳濃度上升。As can be seen from FIG. 4, it can be confirmed that the carbon concentration in the silicon single crystal 10 is significantly lowered in the case of the upper + lower exhaust than in the case of only the lower exhaust in Comparative Example 1. On the other hand, in the case where only the upper exhaust gas is used in Comparative Example 2, the carbon concentration in the silicon single crystal 10 is higher than that in the case where only the lower exhaust gas is used in Comparative Example 1. This is because the CO gas generated by the reaction of the quartz crucible 3A and the graphite crucible 3B is sucked to the upper part, so the CO concentration near the silicon melt 9 increases, and as a result, the carbon concentration in the silicon single crystal 10 increases.

[2]上部排氣口16A及下部排氣口16B的氣體的排氣量之比率 繼之,使用STR公司的熱流動解析程式CGSim,模擬在改變上部排氣口16A及下部排氣口16B之氣體的排氣量的比率時,矽熔液9中的碳濃度會如何變化。結果顯示於表1及圖5。[2] The ratio of the exhaust gas volume of the upper exhaust port 16A and the lower exhaust port 16B is followed by using the thermal flow analysis program CGSim of STR to simulate the change of the upper exhaust port 16A and the lower exhaust port 16B. How the carbon concentration in the silicon melt 9 changes when the ratio of the gas exhaust amount is changed. The results are shown in Table 1 and Fig. 5.

[表1] [Table 1]

從表1及圖5可知,上部排氣口16A之氣體的排氣量:下部排氣口16B之氣體的排氣量=1:3時,矽熔液9中的碳濃度降低到5×1015 (atoms/cm3 )以下。 另一方面,可以確認:上部排氣口16A之氣體的排氣量:下部排氣口16B之氣體的排氣量=6:1為止,能夠降低到5×1015 (atoms/cm3 )以下。 尤其是,在1:2≦上部排氣口16A之氣體的排氣量:下部排氣口16B之氣體的排氣量≦3:1的範圍中,能夠降低到4×1015 (atoms/cm3 )以下,能夠大幅降低矽熔液9中的碳濃度。As can be seen from Table 1 and FIG. 5, when the gas exhaust volume of the upper exhaust port 16A: the gas exhaust volume of the lower exhaust port 16B = 1: 3, the carbon concentration in the silicon melt 9 is reduced to 5 × 10. 15 (atoms / cm 3 ) or less. On the other hand, it can be confirmed that the exhaust gas amount of the gas at the upper exhaust port 16A: the exhaust gas amount of the gas at the lower exhaust port 16B = 6: 1, and can be reduced to 5 × 10 15 (atoms / cm 3 ) or less . In particular, in the range of 1: 2 ≦ the upper exhaust port 16A gas exhaust volume: lower exhaust port 16B gas exhaust volume ≦ 3: 1, it can be reduced to 4 × 10 15 (atoms / cm 3 ) Below, the carbon concentration in the silicon melt 9 can be significantly reduced.

因此,能夠確認:藉由適當改變上部排氣口16A之氣體的排氣量:下部排氣口16B之氣體的排氣量,能夠使得矽熔液9中的碳濃度降低,因此,能夠降低已拉引的矽單結晶10中的碳濃度。Therefore, it can be confirmed that the carbon concentration in the silicon melt 9 can be reduced by appropriately changing the gas exhaust amount of the gas at the upper exhaust port 16A and the gas exhaust amount of the lower exhaust port 16B. Carbon concentration in the drawn silicon single crystal 10.

1‧‧‧拉引裝置1‧‧‧Pull device

2‧‧‧反應室2‧‧‧ reaction chamber

3‧‧‧坩堝3‧‧‧ crucible

3A‧‧‧石英坩堝3A‧‧‧Quartz Crucible

3B‧‧‧石墨坩堝3B‧‧‧Graphite Crucible

4‧‧‧支持軸4‧‧‧ support shaft

5‧‧‧加熱器5‧‧‧ heater

6‧‧‧隔熱材6‧‧‧Insulation

7‧‧‧拉引軸7‧‧‧ Pull shaft

8‧‧‧種結晶8‧‧‧ crystals

9‧‧‧矽熔液9‧‧‧ silicon melt

10‧‧‧矽單結晶10‧‧‧ silicon single crystal

12‧‧‧熱遮蔽體12‧‧‧ heat shield

13‧‧‧氣體導入口13‧‧‧Gas inlet

14‧‧‧排氣口14‧‧‧ exhaust port

15‧‧‧排氣管15‧‧‧ exhaust pipe

16‧‧‧内筒16‧‧‧ Inner tube

16A‧‧‧上部排氣口16A‧‧‧ Upper exhaust port

16B‧‧‧下部排氣口16B‧‧‧Lower exhaust port

[圖1]顯示本發明的實施形態之矽單結晶拉引裝置的構造的模式圖。 [圖2] 顯示前記實施形態中的排氣流路之構造的垂直方向剖面圖。 [圖3] 顯示前記實施形態中的排氣流路之構造水平方向剖面圖。 [圖4] 顯示對應於實施例中的上部排氣口及下部排氣口之氣體的排氣量的矽單結晶中之碳濃度之變化的圖形。 [圖5] 顯示將排氣流路中的上部排氣口之氣體的排氣量和下部排氣口之氣體的排氣量的比變更後的模擬結果之圖形。[Fig. 1] A schematic diagram showing a structure of a silicon single crystal pulling device according to an embodiment of the present invention. [FIG. 2] A vertical cross-sectional view showing the structure of an exhaust gas flow path in the foregoing embodiment. [Fig. 3] A horizontal cross-sectional view showing a structure of an exhaust flow path in the foregoing embodiment. [Fig. 4] A graph showing a change in the carbon concentration in a silicon single crystal corresponding to the exhaust gas amount of the gas in the upper exhaust port and the lower exhaust port in the example. [Fig. 5] A graph showing a simulation result obtained by changing a ratio of an exhaust gas amount of an upper exhaust port and an exhaust gas amount of a lower exhaust port in an exhaust flow path.

Claims (5)

一種矽單結晶的製造方法,其係為使用具備反應室、設置於前記反應室内的石英坩堝、及配置為包圍前記石英坩堝並將前記石英坩堝加熱的加熱器之拉引裝置,以製造矽單結晶的矽單結晶的製造方法, 在前記拉引裝置形成將已被導入前記拉引裝置内的氣體從前記加熱器的上部排氣的上部排氣口、以及從前記加熱器的下部排氣的下部排氣口; 其中,1:3≦從前記上部排氣口之氣體的排氣量:從前記下部排氣口之氣體的排氣量≦6:1。A method for manufacturing a silicon single crystal is to use a quartz crucible provided with a reaction chamber, the quartz crucible provided in the preceding reaction chamber, and a pulling device arranged to surround the preceding quartz crucible and heat the preceding quartz crucible to produce the silicon single crystal. In a method for producing crystalline silicon single crystal, an upper exhaust port for exhausting gas that has been introduced into the former pull apparatus from the upper part of the former heater and a gas exhaust from the lower part of the former heater are formed in the former pull device. Lower exhaust port; where 1: 3 ≦ exhaust gas from the upper exhaust port of the previous note: exhaust gas from the lower exhaust port of the previous note ≦ 6: 1. 如申請專利範圍第1項所記載的矽單結晶的製造方法,其中, 1:2≦從前記上部排氣口之氣體的排氣量:從前記下部排氣口之氣體的排氣量≦3:1。The method for manufacturing a silicon single crystal according to item 1 of the scope of the patent application, wherein 1: 2 ≦ exhaust gas amount of the gas from the upper exhaust port in the foregoing description: exhaust gas amount of the gas from the lower exhaust port in the previous description ≦ 3 :1. 如申請專利範圍第1項所記載的矽單結晶的製造方法, 其中,藉由改變各排氣口的開口面積,而調整從前記上部排氣口及前記下部排氣口之氣體的排氣量。The method for manufacturing a silicon single crystal according to item 1 of the scope of the patent application, wherein the amount of gas discharged from the upper exhaust port and lower exhaust port is adjusted by changing the opening area of each exhaust port. . 如申請專利範圍第2項所記載的矽單結晶的製造方法, 其中,藉由改變各排氣口的開口面積,而調整從前記上部排氣口及前記下部排氣口之氣體的排氣量。The method for manufacturing a silicon single crystal according to item 2 of the scope of patent application, wherein the amount of gas exhausted from the upper exhaust port and lower exhaust port is adjusted by changing the opening area of each exhaust port. . 如申請專利範圍第1到4項中任一項所記載的矽單結晶的製造方法, 前記拉引裝置具備排氣流路,其係為配置於前記反應室内,形成了前記上部排氣口及前記下部排氣口,由碳構件所構成。As described in the method for manufacturing a silicon single crystal according to any one of the claims 1 to 4, the pre-drawing device includes an exhaust flow path, which is arranged in the pre-reaction chamber, forming the pre-exhaust upper exhaust port and The lower exhaust port mentioned above is made of carbon components.
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