JPH04349128A - Method for growing crystal - Google Patents

Method for growing crystal

Info

Publication number
JPH04349128A
JPH04349128A JP15248891A JP15248891A JPH04349128A JP H04349128 A JPH04349128 A JP H04349128A JP 15248891 A JP15248891 A JP 15248891A JP 15248891 A JP15248891 A JP 15248891A JP H04349128 A JPH04349128 A JP H04349128A
Authority
JP
Japan
Prior art keywords
crucible
single crystal
layer
crystal
melt
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP15248891A
Other languages
Japanese (ja)
Inventor
Toshinori Rokusha
六車 俊範
Hiroshi Fujita
浩史 藤田
Masahiko Okui
正彦 奥井
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP15248891A priority Critical patent/JPH04349128A/en
Publication of JPH04349128A publication Critical patent/JPH04349128A/en
Pending legal-status Critical Current

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  • Crystals, And After-Treatments Of Crystals (AREA)
  • Liquid Deposition Of Substances Of Which Semiconductor Devices Are Composed (AREA)

Abstract

PURPOSE:To enhance the quality of a single crystal grown by increasing the concn. of oxygen in a melt layer and increasing the concn. of oxygen taken in the single crystal. CONSTITUTION:A heater 12 is set around a crucible 11, this crucible 11 is filled with starting material for a crystal and powdery or lump SiO2 and the upper parts of them are melted to form a melt layer 17. The thickness of the melt layer 17 is controlled by regulating the position of the heater 12 or the crucible 11 and a single crystal 16 is pulled up from the layer 17 and grown.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、例えば半導体材料とし
て用いられるシリコン単結晶等の結晶を成長させる方法
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for growing crystals such as silicon single crystals used as semiconductor materials, for example.

【0002】0002

【従来の技術】一般にこの種の結晶の成長方法としては
チョクラルスキー法 (CZ法) が広く用いられてい
る。 図5は従来のCZ法に用いられる結晶成長装置を示す模
式的縦断面図であり、11はチャンバ内に配設された坩
堝を示している。坩堝11は有底円筒状をなす石英製の
内層保持容器11aとこの内層保持容器11aの外側に
嵌合された黒鉛製の外層保持容器11bとから構成され
ており、坩堝11の外側には抵抗加熱式のヒータ12が
同心円筒状に配設されている。坩堝11にはヒータ12
により溶融させた原料の溶融液13が充填されており、
この溶融液13中に引上げ棒又はワイヤ等からなる引上
げ軸14にて吊り下げた種結晶15を浸し、これを回転
させつつ上方に引上げることにより、種結晶15の下端
に溶融液13を凝固させて単結晶16を成長せしめるよ
うになっている。
2. Description of the Related Art Generally, the Czochralski method (CZ method) is widely used as a method for growing this type of crystal. FIG. 5 is a schematic vertical cross-sectional view showing a crystal growth apparatus used in the conventional CZ method, and 11 indicates a crucible disposed in a chamber. The crucible 11 is composed of an inner layer holding container 11a made of quartz and having a cylindrical shape with a bottom, and an outer layer holding container 11b made of graphite fitted on the outside of the inner layer holding container 11a. A heating type heater 12 is arranged in a concentric cylindrical shape. A heater 12 is installed in the crucible 11.
It is filled with a melt 13 of the raw material melted by
The seed crystal 15 suspended by a pulling shaft 14 made of a pulling rod or wire is immersed in this melt 13, and the seed crystal 15 is pulled upward while rotating, thereby solidifying the melt 13 at the lower end of the seed crystal 15. This causes the single crystal 16 to grow.

【0003】半導体単結晶をこの方法で成長させる場合
、単結晶16の電気抵抗率、電気伝導型を調整するため
に、引上げ前に溶融液13中に不純物元素を添加するこ
とが多い。ところが、添加した不純物は単結晶16の結
晶成長方向に偏析するという現象が生じ、その結果、結
晶成長方向に均一な電気的特性を有する単結晶16が得
られないという問題があった。この偏析は、溶融液13
と単結晶16との成長界面における単結晶16中の不純
物濃度CS と溶融液13中の不純物濃度CL との比
CS /CL 、即ち実効偏析係数Ke が1でないこ
とに起因する。例えばKe <1の場合には単結晶16
が成長するに伴って溶融液13中の不純物濃度が高くな
り、単結晶16に偏析が生じる。
When a semiconductor single crystal is grown using this method, impurity elements are often added to the melt 13 before pulling in order to adjust the electrical resistivity and electrical conductivity type of the single crystal 16. However, a phenomenon occurs in which the added impurities segregate in the crystal growth direction of the single crystal 16, and as a result, there is a problem in that the single crystal 16 having uniform electrical characteristics in the crystal growth direction cannot be obtained. This segregation is caused by melt 13
This is because the ratio CS /CL between the impurity concentration CS in the single crystal 16 and the impurity concentration CL in the melt 13 at the growth interface between the single crystal 16 and the single crystal 16, that is, the effective segregation coefficient Ke is not 1. For example, if Ke <1, single crystal 16
As the single crystal 16 grows, the impurity concentration in the melt 13 increases, causing segregation in the single crystal 16.

【0004】このような偏析を抑制する方法として溶融
層法が知られている。図6は溶融層法に用いられる結晶
成長装置の模式的縦断面図である。溶融層法はヒータ1
2の制御によって坩堝11の下部に結晶用原料の固体層
18を、またその上方に結晶用原料の溶融液層17を共
存させ、溶融液層17中の不純物濃度を一定に保持した
状態で溶融液層17に種結晶15を浸し、これを引上げ
て単結晶16を成長せしめる方法である。溶融液層17
中の不純物濃度を一定に保持する方法として、溶融層厚
一定法及び溶融層厚変化法が提案されている。溶融層厚
一定法は、単結晶16の引上げに伴い固定層18を溶融
させて溶融液層17の層厚を一定に保持し、不純物を連
続的に添加して溶融液層17中の不純物濃度を一定に保
持する方法であり、特公昭34−8242 号、実開昭
61−150862 号、特公昭62−880号及び特
開昭63−252989 号公報等に開示されている。 また、溶融層厚変化法は単結晶16の成長に伴い坩堝1
1又はヒータ12を昇降させ、溶融液層17の層厚を変
化させることにより、単結晶16の引上げ中に不純物を
添加することなく溶融液層17中の不純物濃度を一定に
保持する方法であり、特開昭61−205691 号、
特開昭61−205692 号、特開昭61− 215
285号公報等に開示されている。
[0004] A fused layer method is known as a method for suppressing such segregation. FIG. 6 is a schematic longitudinal sectional view of a crystal growth apparatus used in the fused layer method. The fused layer method uses heater 1
2, a solid layer 18 of the raw material for crystallization coexists in the lower part of the crucible 11, and a molten liquid layer 17 of the raw material for crystallization coexists above the solid layer 18, and the impurity concentration in the molten liquid layer 17 is kept constant. In this method, a seed crystal 15 is immersed in a liquid layer 17 and pulled up to grow a single crystal 16. Molten liquid layer 17
As a method for keeping the impurity concentration in a constant value, a constant melt layer thickness method and a melt layer thickness change method have been proposed. In the constant melt layer thickness method, the fixed layer 18 is melted as the single crystal 16 is pulled up to keep the layer thickness of the melt layer 17 constant, and impurities are continuously added to adjust the impurity concentration in the melt layer 17. This is a method of keeping the value constant, and is disclosed in Japanese Patent Publication No. 34-8242, Japanese Utility Model Application Publication No. 61-150862, Japanese Patent Publication No. 62-880, and Japanese Patent Application Publication No. 63-252989. In addition, in the molten layer thickness change method, as the single crystal 16 grows, the crucible 1
This method maintains the impurity concentration in the melt layer 17 constant without adding impurities during pulling of the single crystal 16 by raising and lowering the heater 12 or the heater 12 to change the layer thickness of the melt layer 17. , Japanese Patent Publication No. 61-205691,
JP-A-61-205692, JP-A-61-215
It is disclosed in Publication No. 285 and the like.

【0005】CZ法により引上げられた単結晶16中は
、上述の不純物元素の他に1017〜1018atom
s ・cm−3の酸素を含有している。単結晶16中の
酸素はウエハの機械的強度の増加又は重金属の汚染物質
を吸着するためのゲッタリング源として不可欠であり、
石英製の内層保持容器11aの一部が溶融液13に溶解
して酸素が溶出することにより供給される。図7は溶融
液13の対流による酸素輸送状態を示した模式図である
。溶出した酸素は図7に示した如く、熱対流a、単結晶
16の回転による強制対流b、坩堝11の回転による強
制対流c及び表面張力差により働くマランゴニ対流dに
より溶融液13全体に輸送される。このとき溶融液13
中の酸素濃度の制御は、坩堝11の回転及び単結晶16
の回転による対流制御、磁場をかけることによる対流制
御(電子材料、1987年9月p.111〜115)、
ヒータ12の加熱制御による熱対流及び酸素溶出量制御
等により行われる。
In addition to the above-mentioned impurity elements, the single crystal 16 pulled by the CZ method contains 1017 to 1018 atoms.
It contains s·cm−3 of oxygen. Oxygen in the single crystal 16 is essential for increasing the mechanical strength of the wafer or as a gettering source for adsorbing heavy metal contaminants;
Oxygen is supplied by dissolving a part of the inner layer holding container 11a made of quartz into the melt 13 and eluting oxygen. FIG. 7 is a schematic diagram showing the state of oxygen transport by convection of the melt 13. As shown in FIG. 7, the dissolved oxygen is transported throughout the melt 13 by thermal convection a, forced convection b due to the rotation of the single crystal 16, forced convection c due to the rotation of the crucible 11, and Marangoni convection d caused by the difference in surface tension. Ru. At this time, the melt 13
The oxygen concentration in the crucible 11 is controlled by the rotation of the crucible 11 and the single crystal 16.
convection control by rotation of , convection control by applying a magnetic field (Electronic Materials, September 1987, p. 111-115),
This is performed by thermal convection by controlling the heating of the heater 12, oxygen elution amount control, and the like.

【0006】[0006]

【発明が解決しようとする課題】前述した如き溶融層法
においては、坩堝11下部に固体層18が存在するため
、CZ法と比較して坩堝11と溶融液層17との接触面
積が少なく、引上げた単結晶16中に取り込まれる酸素
濃度が低いという問題があった。従って、CZ法により
成長させた単結晶16と比較して機械的強度が弱くなり
、重金属等の汚染物質がウエハの素子活性領域から除去
されず、ウエハ上に形成された素子の特性を低下させる
一因となっていた。本発明は斯かる事情に鑑みてなされ
たものであり、坩堝内に結晶用原料を充填するときに粉
状又は塊状のSiO2 を混入して溶融層法により結晶
を成長させることにより、単結晶に取り込まれる酸素濃
度を高くして単結晶の品質を向上させることができる結
晶成長方法を提供することを目的とする。
In the molten layer method as described above, since the solid layer 18 is present at the bottom of the crucible 11, the contact area between the crucible 11 and the molten liquid layer 17 is smaller than in the CZ method. There was a problem in that the concentration of oxygen taken into the pulled single crystal 16 was low. Therefore, compared to the single crystal 16 grown by the CZ method, the mechanical strength is weaker, and contaminants such as heavy metals are not removed from the device active region of the wafer, which deteriorates the characteristics of the devices formed on the wafer. This was a contributing factor. The present invention was made in view of the above circumstances, and it is possible to grow a single crystal by mixing powdered or lumpy SiO2 when filling a crucible with crystal raw materials and growing the crystal by the molten layer method. An object of the present invention is to provide a crystal growth method that can increase the concentration of oxygen taken in and improve the quality of a single crystal.

【0007】[0007]

【課題を解決するための手段】本発明に係る結晶成長方
法は、周囲にヒータを設置した坩堝内に結晶用原料を充
填し、該結晶用原料の上部を溶融して溶融液層を形成し
、前記ヒータ又は前記坩堝の位置を調節して前記溶融液
層の層厚を制御しつつ、該溶融液層から結晶を引上げて
成長させる結晶成長方法において、前記坩堝内に結晶用
原料を充填するときに、粉状又は塊状のSiO2 を混
入させることを特徴とする。
[Means for Solving the Problems] A crystal growth method according to the present invention includes filling a crucible with a heater around the crucible, and melting the upper part of the crystal raw material to form a molten liquid layer. , in a crystal growth method in which a crystal is grown by pulling up from the melt layer while controlling the layer thickness of the melt layer by adjusting the position of the heater or the crucible, the crucible is filled with a crystal raw material; It is sometimes characterized by mixing powdered or lumpy SiO2.

【0008】[0008]

【作用】通常、酸素は以下に示す(1)〜(3)のプロ
セスを経て溶融液層中から単結晶中に取り込まれる。 (1)溶融液と石英坩堝との界面における石英の溶解に
より酸素が溶出する(SiO2 →Si+2O)。 (2)対流により酸素が溶融液層内で移動する。 (3)溶融液層と雰囲気との界面(溶融液層表面)にお
いて、酸素はSiOとして蒸発する(Si+O→SiO
↑)、又は溶融液層と単結晶との界面(成長界面)にお
いて単結晶中に取り込まれる(O(in Melt )
→O(inCrystal))。本発明においては、溶
融層法にあって溶融液層における(1)のプロセスのみ
でなく、固体層からも酸素が供給されるので、溶融液層
中の酸素濃度が高くなる。従って、引上げた単結晶中の
酸素濃度が高くなる。
[Operation] Oxygen is normally taken into the single crystal from the melt layer through the following processes (1) to (3). (1) Oxygen is eluted due to dissolution of quartz at the interface between the melt and the quartz crucible (SiO2 → Si+2O). (2) Oxygen moves within the melt layer due to convection. (3) At the interface between the melt layer and the atmosphere (melt layer surface), oxygen evaporates as SiO (Si+O→SiO
↑), or incorporated into the single crystal at the interface (growth interface) between the melt layer and the single crystal (O(in Melt)
→O(inCrystal)). In the present invention, in the molten layer method, oxygen is supplied not only from the process (1) in the molten layer but also from the solid layer, so that the oxygen concentration in the molten layer increases. Therefore, the oxygen concentration in the pulled single crystal increases.

【0009】[0009]

【実施例】以下本発明をその実施例を示す図面に基づき
具体的に説明する。図1は本発明に係る結晶成長装置の
模式的縦断面図であり、図中21はチャンバである。チ
ャンバ21は略円筒形状の真空容器であり、チャンバ2
1の略中央位置には坩堝11が配設されている。坩堝1
1は有底円筒形状の石英製の内層保持容器11aとこの
内層保持容器11aの外側に嵌合された有底円筒形状の
黒鉛製の外層保持容器11bとから構成されている。こ
の外層保持容器11bの下面には坩堝11を回転及び昇
降させる軸22が着設されており、坩堝11の外周には
、抵抗加熱式等のヒータ12が昇降可能に配設されてい
る。さらにヒータ12の外部には保温筒23が周設され
ている。坩堝11とヒータ12との相対的な上下方向位
置調節により坩堝11内に溶融液層17及び固体層18
を夫々の厚みを相対的に調節して形成し得るようになっ
ている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below with reference to drawings showing embodiments thereof. FIG. 1 is a schematic longitudinal sectional view of a crystal growth apparatus according to the present invention, and numeral 21 in the figure is a chamber. The chamber 21 is a substantially cylindrical vacuum container;
A crucible 11 is disposed approximately at the center of the crucible 1 . Crucible 1
1 is composed of an inner layer holding container 11a made of quartz and having a cylindrical shape with a bottom, and an outer layer holding container 11b made of graphite and having a cylindrical shape with a bottom fitted on the outside of the inner layer holding container 11a. A shaft 22 for rotating and raising and lowering the crucible 11 is installed on the lower surface of the outer layer holding container 11b, and a heater 12, such as a resistance heating type, is arranged on the outer periphery of the crucible 11 so as to be movable up and down. Further, a heat retaining cylinder 23 is provided around the outside of the heater 12. A molten liquid layer 17 and a solid layer 18 are formed in the crucible 11 by adjusting the relative vertical positions of the crucible 11 and the heater 12.
can be formed by relatively adjusting their respective thicknesses.

【0010】一方、坩堝11の上方にはチャンバ21の
上部に連設形成された小形の略円筒形状のプルチャンバ
24を貫通して、引上げ軸14が回転及び昇降可能に垂
設されており、引上げ軸14の下端には種結晶15が装
着されるようになっている。そしてこの種結晶15の下
端を溶融液層17に浸漬させた後、これを回転させつつ
上昇させることにより、種結晶15の下端から単結晶1
6を成長せしめるようになっている。
On the other hand, above the crucible 11, a pulling shaft 14 is vertically installed so as to be able to rotate and move up and down, passing through a small, approximately cylindrical pull chamber 24 that is connected to the upper part of the chamber 21. A seed crystal 15 is attached to the lower end of the shaft 14. After the lower end of the seed crystal 15 is immersed in the molten liquid layer 17, by rotating and raising it, the single crystal 1
6 is made to grow.

【0011】以上の如く構成された装置を使用して単結
晶を成長させる場合、まず坩堝11内に固体原料として
塊状又は顆粒状の多結晶シリコンと粉状又は塊状のSi
O2 とを、引上げる単結晶16の体積から逆算して求
めた必要量だけ充填する。SiO2 は粉状のものの方
が原料シリコン中に均一に混ざりやすく、単結晶16の
軸方向の酸素分布が均一になるので望ましい。また、直
径略10〜50mmの顆粒状のSiO2 を混入させる
と、顆粒が溶けずに単結晶16の成長界面に浮上し、単
結晶16の多結晶化が生じる頻度が増加するので顆粒状
のSiO2 は使用しない方がよい。直径50mm以上
の塊状のSiO2 は使用可能である。塊状のSiO2
 として棒状のものを使用し、坩堝11の軸に平行に立
てるようにして入れると、SiO2 の溶け出し量が一
定になり、また、溶けていないSiO2 が単結晶16
の成長界面に浮上して単結晶16が多結晶化することが
防止される。図2は坩堝11に多結晶シリコンと粉状の
SiO2 を充填した場合を示した模式図、図3は坩堝
11に多結晶シリコンと塊状のSiO2 を充填した場
合を示した模式図である。
When growing a single crystal using the apparatus configured as described above, first, bulk or granular polycrystalline silicon and powder or lump Si are placed in the crucible 11 as solid raw materials.
O2 is filled in the required amount determined by back calculation from the volume of the single crystal 16 to be pulled. It is preferable for SiO2 to be in powder form because it is easier to mix uniformly into the raw silicon and the oxygen distribution in the axial direction of the single crystal 16 becomes uniform. Furthermore, when granular SiO2 with a diameter of about 10 to 50 mm is mixed, the granules do not melt and float to the growth interface of the single crystal 16, increasing the frequency of polycrystallization of the single crystal 16. It is better not to use it. Bulk SiO2 having a diameter of 50 mm or more can be used. lumpy SiO2
If a rod-shaped object is used as a crucible and placed in a position parallel to the axis of the crucible 11, the amount of SiO2 dissolved will be constant, and the unmelted SiO2 will become a single crystal 16.
This prevents the single crystal 16 from floating to the growth interface and becoming polycrystalline. FIG. 2 is a schematic diagram showing a case where the crucible 11 is filled with polycrystalline silicon and powdered SiO2, and FIG. 3 is a schematic diagram showing a case where the crucible 11 is filled with polycrystalline silicon and bulk SiO2.

【0012】多結晶シリコンとSiO2 とを充填した
後、これらを上側からヒータ12により溶融させて溶融
液層17を形成し、溶融液層17と固体層18とを共存
させた状態にする。ヒータ12及び坩堝11の位置制御
により溶融液層17の層厚を所定の層厚にし、不純物と
してリンを投入し、リンを拡散させる。そして、溶融液
層17に種結晶15の下端を浸漬し、引上げ軸14を回
転させつつ引上げ、その下端に単結晶16を成長させる
。 このとき溶融液層17と坩堝11との界面における石英
の溶解(SiO2 →Si+2O)と共に、固体層18
より酸素が供給されるため、溶融液層17中の酸素濃度
が高められ、ゲッタリング源として必要な酸素濃度を有
する単結晶16を成長させることができる。
After filling polycrystalline silicon and SiO2, they are melted from above by a heater 12 to form a molten liquid layer 17, so that the molten liquid layer 17 and the solid layer 18 coexist. By controlling the positions of the heater 12 and the crucible 11, the thickness of the melt layer 17 is set to a predetermined thickness, and phosphorus is introduced as an impurity to diffuse the phosphorus. Then, the lower end of the seed crystal 15 is immersed in the melt layer 17 and pulled up while rotating the pulling shaft 14, thereby growing the single crystal 16 at the lower end. At this time, along with the dissolution of quartz at the interface between the molten liquid layer 17 and the crucible 11 (SiO2 → Si+2O), the solid layer 18
Since more oxygen is supplied, the oxygen concentration in the melt layer 17 is increased, and it is possible to grow the single crystal 16 having an oxygen concentration necessary as a gettering source.

【0013】以下に具体的な数値を挙げて説明する。上
述した装置を使用し、坩堝11に略60kgの塊状又は
顆粒状の多結晶シリコンと略10kgの粉状又は塊状の
SiO2 とを充填して、直径6cm、長さ略50cm
のシリコン単結晶16を引上げ、結晶長20cmの位置
における中心部の酸素濃度を測定した。このとき従来の
方法により成長させた単結晶中の酸素濃度も同様にして
測定した。その結果、従来の方法により成長させた単結
晶中の酸素濃度は略1015〜1016atoms ・
cm−3であったのに対し、本発明方法により成長させ
た単結晶中の酸素濃度は略1017〜1019atom
s ・cm−3であった。従って本発明方法が単結晶中
の酸素濃度を向上させる上で有効であることが判った。
[0013] Specific numerical values will be listed and explained below. Using the above-mentioned apparatus, the crucible 11 was filled with approximately 60 kg of polycrystalline silicon in the form of lumps or granules and approximately 10 kg of SiO2 in the form of powder or lumps, and the crucible 11 had a diameter of 6 cm and a length of approximately 50 cm.
The silicon single crystal 16 was pulled up and the oxygen concentration at the center at a crystal length of 20 cm was measured. At this time, the oxygen concentration in the single crystal grown by the conventional method was also measured in the same manner. As a result, the oxygen concentration in a single crystal grown by the conventional method is approximately 1015 to 1016 atoms.
cm-3, whereas the oxygen concentration in the single crystal grown by the method of the present invention was approximately 1017 to 1019 atoms.
It was s·cm-3. Therefore, it was found that the method of the present invention is effective in increasing the oxygen concentration in single crystals.

【0014】図4は原料シリコンに混入させる粉状Si
O2 の量と単結晶中の酸素濃度との関係を示したグラ
フである。SiO2 は量を2.5 kg、5kg、7
.5 kg、10kgと変えて添加し、夫々結晶長20
cmの位置における中心部の酸素濃度を測定した。その
結果、SiO2 の混ぜ方に依存性があるため分布にバ
ラツキがあるが、SiO2 の添加量により単結晶中の
酸素濃度を制御できることが判った。
FIG. 4 shows powdered Si mixed into raw material silicon.
It is a graph showing the relationship between the amount of O2 and the oxygen concentration in a single crystal. The amount of SiO2 is 2.5 kg, 5 kg, 7
.. 5 kg and 10 kg were added, each with a crystal length of 20 kg.
The oxygen concentration in the center at the cm position was measured. As a result, it was found that the oxygen concentration in the single crystal could be controlled by changing the amount of SiO2 added, although there were variations in the distribution due to the dependence on the mixing method of SiO2.

【0015】[0015]

【発明の効果】以上の如く本発明においては坩堝内に結
晶用原料を充填するときに粉状のSiO2 を均一に混
入させるか又は直径50mm以上の塊状のSiO2 を
坩堝の軸に平行に立てるようにして混入させ、溶融層法
により結晶を成長させるので、溶融液層の酸素濃度を高
めて単結晶に取り込まれる酸素濃度を一様に高くし、単
結晶の品質を向上させることができる。そして高品質な
素子を歩留よく製造することが可能になる。また、添加
するSiO2 の量を変えることにより、単結晶中の酸
素濃度を制御することができる等、本発明は優れた効果
を奏するものである。
As described above, in the present invention, when filling a crucible with raw materials for crystallization, powdered SiO2 is uniformly mixed in, or lumpy SiO2 with a diameter of 50 mm or more is erected parallel to the axis of the crucible. Since the crystal is grown by the molten layer method, the oxygen concentration in the molten liquid layer can be increased, the oxygen concentration taken into the single crystal can be uniformly increased, and the quality of the single crystal can be improved. In addition, it becomes possible to manufacture high-quality devices with a high yield. Further, the present invention has excellent effects such as being able to control the oxygen concentration in the single crystal by changing the amount of SiO2 added.

【図面の簡単な説明】[Brief explanation of the drawing]

【図1】本発明に係る結晶成長装置の模式的縦断面図で
ある。
FIG. 1 is a schematic longitudinal sectional view of a crystal growth apparatus according to the present invention.

【図2】坩堝に多結晶シリコンと粉状のSiO2 を充
填した場合を示した模式図である。
FIG. 2 is a schematic diagram showing a crucible filled with polycrystalline silicon and powdered SiO2.

【図3】坩堝に多結晶シリコンと塊状のSiO2 を充
填した場合を示した模式図である。
FIG. 3 is a schematic diagram showing a crucible filled with polycrystalline silicon and bulk SiO2.

【図4】原料シリコンに混入させる粉状SiO2 の量
と単結晶中の酸素濃度との関係を示したグラフである。
FIG. 4 is a graph showing the relationship between the amount of powdered SiO2 mixed into raw silicon and the oxygen concentration in the single crystal.

【図5】従来のCZ法に用いられる結晶成長装置を示す
模式的縦断面図である。
FIG. 5 is a schematic vertical cross-sectional view showing a crystal growth apparatus used in the conventional CZ method.

【図6】溶融層法に用いられる結晶成長装置の模式的縦
断面図である。
FIG. 6 is a schematic vertical cross-sectional view of a crystal growth apparatus used in the fused layer method.

【図7】溶融液の対流による酸素輸送状態を示した模式
図である。
FIG. 7 is a schematic diagram showing the state of oxygen transport by convection of the melt.

【符号の説明】[Explanation of symbols]

11  坩堝 12  ヒータ 14  引上げ軸 15  種結晶 16  単結晶 17  溶融液層 18  固体層 21  チャンバ 23  保温筒 11 Crucible 12 Heater 14 Pulling shaft 15 Seed crystal 16 Single crystal 17 Molten liquid layer 18 Solid layer 21 Chamber 23 Heat insulation cylinder

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  周囲にヒータを設置した坩堝内に結晶
用原料を充填し、該結晶用原料の上部を溶融して溶融液
層を形成し、前記ヒータ又は前記坩堝の位置を調節して
前記溶融液層の層厚を制御しつつ、該溶融液層から結晶
を引上げて成長させる結晶成長方法において、前記坩堝
内に結晶用原料を充填するときに、粉状又は塊状のSi
O2 を混入させることを特徴とする結晶成長方法。
1. A crucible with a heater installed around it is filled with a raw material for crystallization, an upper part of the raw material for crystallization is melted to form a molten liquid layer, and the position of the heater or the crucible is adjusted to In a crystal growth method in which a crystal is grown by pulling up a crystal from a melt layer while controlling the layer thickness of the melt layer, powdery or bulk Si is
A crystal growth method characterized by mixing O2.
JP15248891A 1991-05-27 1991-05-27 Method for growing crystal Pending JPH04349128A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15248891A JPH04349128A (en) 1991-05-27 1991-05-27 Method for growing crystal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15248891A JPH04349128A (en) 1991-05-27 1991-05-27 Method for growing crystal

Publications (1)

Publication Number Publication Date
JPH04349128A true JPH04349128A (en) 1992-12-03

Family

ID=15541577

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15248891A Pending JPH04349128A (en) 1991-05-27 1991-05-27 Method for growing crystal

Country Status (1)

Country Link
JP (1) JPH04349128A (en)

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