JPH0244799B2 - KETSUSHOSEICHOHOHO - Google Patents

KETSUSHOSEICHOHOHO

Info

Publication number
JPH0244799B2
JPH0244799B2 JP17120581A JP17120581A JPH0244799B2 JP H0244799 B2 JPH0244799 B2 JP H0244799B2 JP 17120581 A JP17120581 A JP 17120581A JP 17120581 A JP17120581 A JP 17120581A JP H0244799 B2 JPH0244799 B2 JP H0244799B2
Authority
JP
Japan
Prior art keywords
crystal
container
concentration
magnetic field
rotation speed
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.)
Expired - Lifetime
Application number
JP17120581A
Other languages
Japanese (ja)
Other versions
JPS5874594A (en
Inventor
Toshihiko Suzuki
Tomio Sato
Yasaburo Kato
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.)
Sony Corp
Original Assignee
Sony Corp
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 Sony Corp filed Critical Sony Corp
Priority to JP17120581A priority Critical patent/JPH0244799B2/en
Priority to CA000414053A priority patent/CA1223798A/en
Priority to GB08230370A priority patent/GB2109267B/en
Priority to FR8217924A priority patent/FR2515216B1/en
Priority to NL8204133A priority patent/NL8204133A/en
Priority to DE19823239570 priority patent/DE3239570C2/en
Publication of JPS5874594A publication Critical patent/JPS5874594A/en
Publication of JPH0244799B2 publication Critical patent/JPH0244799B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • 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
    • C30B15/30Mechanisms for rotating or moving either the melt or the crystal

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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)
  • Liquid Deposition Of Substances Of Which Semiconductor Devices Are Composed (AREA)

Description

【発明の詳細な説明】 本発明は、半導体、誘電体、磁性体等の各種材
料の結晶成長方法に係わり、特にその結晶中にお
ける不純物例えば酸素の濃度を広範囲に且つ正確
に制御することができるようにするものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for growing crystals of various materials such as semiconductors, dielectrics, and magnetic materials, and in particular allows the concentration of impurities such as oxygen in the crystal to be controlled over a wide range and accurately. It is intended to do so.

単結晶、例えばシリコン単結晶を得る方法とし
てチヨクラルスキー法(以下CZ法という。)があ
る。さらにこのCZ法においてその単結晶の育成
を行なう結晶成長用液体に磁場を印加して単結晶
を引上げていくという方法が提案された。この方
法によつて育成された単結晶は、スワール
(swirl)状の欠陥や成長縞の発生が軽減される。
これは結晶成長用液体が電気伝導性を有する場
合、これに磁場が掛けられることによつてその実
効的粘性が高められ、その結晶成長用液体の熱対
流と液面の振動が抑制されることによると思われ
る。すなわち磁場中で電気伝導性を有する流体、
すなわち導体が運動するとこの流体中に電位差が
発生し電流が流れる。そしてこの磁場中を流れる
電流によつてこの電流を担う流体が新しい力を受
ける。この力は流体が動く方向と反対の方向であ
るので流体の動きは鈍くなり見かけ上粘性が上が
つたことになる。これは磁気粘性といわれる。そ
してこのように磁気粘性が生じたことによつて流
体すなわち、結晶成長溶液体に対流が生じにくく
なるものと思われる。尚、この単結晶の育成を磁
場中で行なうことについては、例えばジヤーナ
ル・オブ・アプライド、フイジクス(Journal of
Applied Physics)Vo1.37、No.5、P.2021
(1966)、及びジヤーナル・オブ・マテリアルズ・
サイエンス(Journal of Materials Science)5
(1970)P.822等によつて記載されている。
The Czyochralski method (hereinafter referred to as the CZ method) is a method for obtaining a single crystal, such as a silicon single crystal. Furthermore, in this CZ method, a method has been proposed in which a magnetic field is applied to the crystal growth liquid used to grow the single crystal to pull the single crystal. In the single crystal grown by this method, the occurrence of swirl-like defects and growth stripes is reduced.
This is because when a crystal growth liquid has electrical conductivity, applying a magnetic field to it increases its effective viscosity, suppressing thermal convection and liquid surface vibration of the crystal growth liquid. It seems to be based on. That is, a fluid that has electrical conductivity in a magnetic field,
In other words, when a conductor moves, a potential difference is generated in this fluid, and a current flows. As a result of the current flowing in this magnetic field, the fluid carrying this current receives a new force. Since this force is in the opposite direction to the direction in which the fluid moves, the movement of the fluid becomes slower and its viscosity increases. This is called magnetic viscosity. It is thought that the generation of magnetic viscosity makes it difficult for convection to occur in the fluid, that is, the crystal growth solution. Regarding growing this single crystal in a magnetic field, for example, the Journal of Applied Physics (Journal of Applied Physics)
Applied Physics)Vo1.37, No.5, P.2021
(1966), and Journal of Materials
Science (Journal of Materials Science) 5
(1970) P.822 etc.

本発明は、このような磁場中において結晶の引
上げを行なう結晶成長方法において、その育成さ
れた結晶中の不純物の濃度、例えば酸素濃度を前
述したように広範囲に且つ正確に制御できるよう
にするものである。すなわち、CZ法による場合、
その結晶成長用液体が収容される容器、例えば石
英容器の構成成分の例えば酸素が、その育成され
た結晶中に混入することが認められたものである
が、従来一般の、磁場が与えられない状態で結晶
育成がなされるCZ法による場合においても、引
上げる結晶の回転数や、るつぼの回転数やその相
対的回転方向やさらにるつぼの温度を制御するこ
とによつて結晶中の酸素濃度の制御は可能である
が、このような磁場が与えられないCZ法では、
前述したようにその結晶成長用液体の粘性が低く
これに対流が生じやすいために、この液体と石英
るつぼとの相対的移動による擦れ合いが大きく、
これがため液体中への酸素の取込み量が大となつ
て育成された結晶中の酸素濃度は高濃度での範
囲、すなわちおよそ1〜2×1018atoms/cm3とい
うせまい範囲のものである。
The present invention is a method for growing a crystal in which the crystal is pulled in a magnetic field, in which the concentration of impurities, such as oxygen concentration, in the grown crystal can be controlled over a wide range and accurately as described above. It is. In other words, when using the CZ method,
Although it has been recognized that oxygen, a component of the container in which the crystal growth liquid is stored, such as a quartz container, is mixed into the grown crystal, conventional magnetic fields are not applied. Even in the case of the CZ method, in which crystals are grown in Although control is possible, the CZ method does not provide such a magnetic field.
As mentioned above, since the viscosity of the crystal growth liquid is low and convection is likely to occur in it, there is a large amount of friction between this liquid and the quartz crucible due to relative movement.
Therefore, the oxygen concentration in the crystal grown by increasing the amount of oxygen taken into the liquid is in a high concentration range, that is, in a narrow range of approximately 1 to 2×10 18 atoms/cm 3 .

一方、半導体単結晶、例えばシリコン単結晶中
の酸素は、その濃度と分布に応じてこれより得る
半導体装置の特性、或いはこれを製造する過程で
の熱処理において様々な効果をもたらす。例えば
この酸素濃度が比較的高い場合は、熱処理によつ
て積層欠陥や酸素の析出物を発生させ、半導体装
置の特性に悪影響を及ぼす。ところがこのような
欠陥を半導体装置の活性領域以外に設けて熱処理
を行なうときは、逆に有害不純物例えばFe、Cu、
Au等の金属不純物をゲツタリングするいわゆる
イントリンシツク・ゲツタリング作用をなし、半
導体装置の特性を向上させる効果がある。また酸
素の析出物が発生しない程度に高い酸素濃度で
は、酸素クラスターによる転位の発生と増加を抑
制する効果をもつ。すなわち、半導体装置の製造
時の熱処理中の転位の発生と増加を抑制し得る。
さらに結晶中の酸素濃度が高い場合に所要の温度
例えば450℃の熱処理でシリコン中の酸素はサー
マルドナーを発生し、n型化する効果を有する
が、低い酸素濃度ではこのサーマルドナーの発生
を低くでき、従来フローテイングゾーン法(FZ
法)によつて得ていた高抵抗率の結晶を得ること
ができ、高耐圧、高出力半導体装置の製造も可能
となる。因みにFZ法による結晶は、大直径化が
困難であり、CZ法による場合、その大直径化が
比較的容易であるので酸素濃度の制御がCZ法に
よつてなされることは、各種半導体装置を廉価に
得る上において有利なものとなる。
On the other hand, oxygen in a semiconductor single crystal, such as a silicon single crystal, has various effects depending on its concentration and distribution on the characteristics of the semiconductor device obtained therefrom or on the heat treatment during the manufacturing process. For example, when this oxygen concentration is relatively high, stacking faults and oxygen precipitates are generated by heat treatment, which adversely affects the characteristics of the semiconductor device. However, when such defects are created outside the active region of a semiconductor device and heat treatment is performed, harmful impurities such as Fe, Cu, etc.
It performs a so-called intrinsic gettering action to getter metal impurities such as Au, and has the effect of improving the characteristics of semiconductor devices. Furthermore, at an oxygen concentration high enough not to generate oxygen precipitates, it has the effect of suppressing the generation and increase of dislocations due to oxygen clusters. That is, the occurrence and increase of dislocations during heat treatment during manufacturing of semiconductor devices can be suppressed.
Furthermore, when the oxygen concentration in the crystal is high, the oxygen in the silicon generates thermal donors by heat treatment at the required temperature, e.g. 450°C, and has the effect of converting it to n-type. However, at low oxygen concentrations, the generation of thermal donors is reduced. The conventional floating zone method (FZ)
It is now possible to obtain crystals with high resistivity, which was obtained by the method (method), and it also becomes possible to manufacture high-voltage, high-output semiconductor devices. Incidentally, it is difficult to increase the diameter of crystals produced by the FZ method, whereas it is relatively easy to increase the diameter of crystals produced by the CZ method.The fact that oxygen concentration can be controlled by the CZ method is useful for various semiconductor devices. This is advantageous in terms of obtaining it at a low price.

本発明においては、このような各種の効果を得
るために広範囲に亘る酸素濃度の選定を行うこと
のできる結晶、例えばシリコン単結晶を得ること
ができるようにした結晶成長法を提供するもので
ある。
The present invention provides a crystal growth method that makes it possible to obtain crystals, such as silicon single crystals, in which oxygen concentrations can be selected over a wide range in order to obtain these various effects. .

以下本発明を詳細に説明する。第1図を参照し
て本発明方法を実施する結晶成長装置について説
明するに、図中1はその装置を全体として示す。
2は或る程度の電気伝導性を有する結晶成長用の
融液又は溶液による液体例えばSi融液3が収容さ
れた容器、例えば石英るつぼで、この容器2はそ
の中心軸に関して回転するようになされ、更にそ
の回転数が選定されるようになされている。この
容器2の外周には、加熱手段4が配置される。こ
の加熱手段4は、通電ヒーター5が、例えばジグ
ザグパターンに容器2の外周面に沿う円筒面状を
なすように配置される。この加熱手段4の外側に
は必要に応じて例えば円筒状の熱遮蔽体、或いは
水冷等によつて冷却されるジヤケツト6が配置さ
れ、その外側に永久磁石、或いは電磁石より成る
例えば直流磁場発生手段7が配置される。8は単
結晶シード、例えばSi単結晶シードで、9はその
引上げチヤツクである。そして、この引上げチヤ
ツクによつて単結晶シードが容器2の回転中心軸
上で、これに沿つて回転しつつ引上げられるよう
になされている。
The present invention will be explained in detail below. A crystal growth apparatus for carrying out the method of the present invention will be described with reference to FIG. 1. In the figure, numeral 1 indicates the apparatus as a whole.
Reference numeral 2 denotes a container, such as a quartz crucible, in which a crystal growth melt or solution liquid having a certain degree of electrical conductivity, such as a Si melt 3, is contained, and this container 2 is configured to rotate about its central axis. , and furthermore, the number of rotations thereof is selected. A heating means 4 is arranged around the outer periphery of this container 2 . The heating means 4 is arranged such that the energized heaters 5 form a cylindrical surface along the outer peripheral surface of the container 2 in, for example, a zigzag pattern. Outside the heating means 4, for example, a cylindrical heat shield or a jacket 6 cooled by water cooling or the like is disposed as required, and on the outside thereof, for example, a DC magnetic field generating means made of a permanent magnet or an electromagnet is arranged. 7 is placed. 8 is a single crystal seed, for example a Si single crystal seed, and 9 is its pulling chuck. The single crystal seed is pulled up by this pulling chuck while rotating along the central axis of rotation of the container 2.

加熱手段4の通電ヒーター5への通電は、リツ
プル分が4%以下に抑えられたほぼ直流の電流、
或いは1KHz以上の交流又は脈流とする。このよ
うな通電電流とするときは、加熱手段4が磁場と
の作用で生ずる不要の振動を回避できることを確
めた。
Electricity is supplied to the energizing heater 5 of the heating means 4 using a substantially direct current with ripple content suppressed to 4% or less.
Or an alternating current or pulsating current of 1KHz or more. It has been confirmed that when such a current is applied, unnecessary vibrations caused by the interaction of the heating means 4 with the magnetic field can be avoided.

このようにして、Siシード8を、Si融液面から
所要の速度で引上げることによつてSi結晶10の
成長を行う。この場合、上述したようにシード
8、したがつてこれより引上育成される単結晶1
0を回転させながら、その引上げ成長を行うもの
であるが、特に本発明においては、容器2の回転
速度を制御してその引上げを行う。
In this way, the Si crystal 10 is grown by pulling the Si seed 8 from the Si melt surface at a required speed. In this case, as mentioned above, the seed 8 and therefore the single crystal 1 to be grown by pulling
The pulling growth is carried out while rotating the container 2. In particular, in the present invention, the pulling is carried out by controlling the rotational speed of the container 2.

すなわち、本発明においては、このように容器
2を回転させ、且つその回転速度を制御すること
によつて引上げられた結晶10中の、上述した容
器2の構成成分の酸素の濃度が変化することを見
出したことに基いてなされた結晶成長法である。
そして、このように、磁場中の結晶引上げにおい
ては容器2の回転によつて結晶10中の例えば酸
素の濃度が変化するのは、容器2の回転によつて
容器2と、これの中に収容され、磁場の印加によ
つて実効的粘性が高められた結晶成長用液体3と
が相対的に回転移行してこの液体3と容器2の内
壁面との間に所要の擦れ合いを生じさせ、これに
よつて容器2の構成成分例えば石英の構成成分の
酸素が液体3中に溶け込み、その擦れ合いが大と
なるほどすなわち容器2の液体3に対する相対的
回転数が増大するほど液体3への溶け込み量が大
となつてこれより引上げられた結晶10中の酸素
濃度が増す。そしてこの結晶中の酸素濃度は、磁
場を与えない場合よりも磁場を与えた状態におい
てその容器の回転数を十分大にすればより高濃度
になし得ることが確認された。
That is, in the present invention, by rotating the container 2 in this way and controlling the rotation speed, the concentration of oxygen, which is a component of the container 2 described above, in the pulled crystal 10 changes. This is a crystal growth method based on the discovery that
In this way, during crystal pulling in a magnetic field, the concentration of, for example, oxygen in the crystal 10 changes due to the rotation of the container 2. and the crystal growth liquid 3 whose effective viscosity has been increased by the application of a magnetic field is rotated relative to each other to cause the required rubbing between the liquid 3 and the inner wall surface of the container 2, As a result, the oxygen in the constituent components of the container 2, such as quartz, dissolves into the liquid 3, and the greater the friction between them, that is, the greater the relative rotational speed of the container 2 with respect to the liquid 3, the more oxygen is dissolved into the liquid 3. As the amount increases, the oxygen concentration in the crystal 10 pulled from this increases. It was also confirmed that the oxygen concentration in this crystal can be made higher than when no magnetic field is applied by sufficiently increasing the number of revolutions of the container when a magnetic field is applied.

尚、引上げる単結晶10は、高温部の熱中心や
熱対称性の上からこれが回転されることが望まれ
るが、この結晶の回転による強制対流が液体3の
容器2の内壁面との接触部に及ぶようなことがあ
ればこれが酸素濃度に影響が生じるが、このよう
な強制対流が容器2の内壁面に及ぶことがないよ
うに結晶と容器2の内壁面との距離を選定するも
のであり、このようにして、容器2の回転によつ
て酸素濃度の制御を行なう。
Note that it is desirable that the single crystal 10 to be pulled is rotated from the viewpoint of the thermal center of the high temperature part and thermal symmetry, but the forced convection caused by the rotation of the crystal causes the liquid 3 to come into contact with the inner wall surface of the container 2. If this occurs, it will affect the oxygen concentration, but the distance between the crystal and the inner wall of the container 2 is selected so that such forced convection does not reach the inner wall of the container 2. In this way, the oxygen concentration is controlled by rotating the container 2.

第2図はこの結晶と容器2の内壁面間の距離を
56mmに選定し、結晶回転数を30rpmに、また石英
るつぼよりなる容器2の回転数を、これとは逆方
向に0.1rpmで回転させた場合において、液体3
すなわちSi融液に与える磁場の強さを変化させた
場合の、その育成された結晶10中の酸素濃度を
測定した結果を示すものである。これより明らか
なように、印加磁場が1500ガウス以上において
は、容器2の回転数が一定であれば、その酸素濃
度にほとんど変化が生じないことがわかる。
Figure 2 shows the distance between this crystal and the inner wall of container 2.
56 mm, the crystal rotation speed is 30 rpm, and the rotation speed of container 2, which is a quartz crucible, is rotated at 0.1 rpm in the opposite direction.
That is, it shows the results of measuring the oxygen concentration in the grown crystal 10 when the strength of the magnetic field applied to the Si melt was varied. As is clear from this, when the applied magnetic field is 1500 Gauss or more, there is almost no change in the oxygen concentration as long as the rotation speed of the container 2 is constant.

また第3図は、結晶10の回転数を変化させた
場合の結晶10中の酸素濃度を測定したものであ
つて、この場合容器2の回転数は0.1rpmとした
場合である。そして第3図中曲線21及び22
は、夫々結晶10と容器2の内壁面との距離を56
mmに選定した場合における磁場印加を行なわない
場合及び3500ガウスの磁場印加を行なつた場合の
各測定曲線で、曲線23は3500ガウスの磁場印加
において結晶と容器2の内壁面との距離を69mmに
選定した場合である。曲線21と曲線22及び2
3とを比較して明らかなように容器2の回転数が
一定の状態では、磁場印加を行なつた場合、磁場
印加を行なわない場合に比して酸素濃度が低下す
るとともに結晶回転数の依存性が小となることが
わかる。また、曲線22と23とを比較すること
によつて明らかなように結晶10と容器2の内壁
面との距離が大となるほど結晶中の酸素濃度の結
晶回転数の変化による影響が小となることがわか
る。
Further, FIG. 3 shows the measurement of the oxygen concentration in the crystal 10 when the rotation speed of the crystal 10 was changed, and in this case, the rotation speed of the container 2 was set to 0.1 rpm. And curves 21 and 22 in Figure 3
are the distances between the crystal 10 and the inner wall of the container 2, respectively, 56
Curve 23 shows the distance between the crystal and the inner wall of container 2 of 69 mm when a magnetic field of 3500 Gauss is applied and when no magnetic field is applied and when a magnetic field of 3500 Gauss is applied. This is the case when selected. Curve 21 and curves 22 and 2
As is clear from comparison with 3, when the rotation speed of the container 2 is constant, when a magnetic field is applied, the oxygen concentration decreases compared to when no magnetic field is applied, and the dependence of the crystal rotation speed increases. It can be seen that the gender is small. Furthermore, as is clear from comparing curves 22 and 23, the larger the distance between the crystal 10 and the inner wall surface of the container 2, the less the effect of changes in the crystal rotation speed on the oxygen concentration in the crystal. I understand that.

また、第4図は容器2の回転数を0.1rpmに選
定した状態における結晶回転数の変化に対する結
晶の直径方向に関する酸素濃度の変化率、すなわ
ち最高濃度−最低濃度/最高濃度×100を示したもので
あ る。これより明らかなように結晶回転数が大にな
るほど結晶中の酸素濃度分布が一様化されること
がわかる。
In addition, Figure 4 shows the rate of change in oxygen concentration in the diametrical direction of the crystal with respect to the change in crystal rotation speed when the rotation speed of container 2 is selected to be 0.1 rpm, that is, maximum concentration - minimum concentration / maximum concentration x 100. It is something. As is clear from this, it can be seen that as the crystal rotation speed increases, the oxygen concentration distribution in the crystal becomes more uniform.

第5図は、引上げ結晶の回転数を50rpmとし、
容器2の回転数を20rpmとした状態で、結晶の引
上げをその各部A,B,Cで夫々印加磁場を3500
ガウス、0ガウス、3500ガウスと変化させたとき
の各部A,B,Cにおける酸素濃度を測定した結
果を示し、これより明らかなように育成される結
晶において磁場が印加されるかされないかによつ
て濃度の異る部分を形成し得ることがわかる。
In Figure 5, the rotation speed of the pulled crystal is 50 rpm,
With the rotation speed of the container 2 at 20 rpm, the magnetic field applied to each part A, B, and C of the crystal was 3500 rpm.
The results of measuring the oxygen concentration in each part A, B, and C when changing it to Gauss, 0 Gauss, and 3500 Gauss are shown, and it is clear from this that the concentration of oxygen depends on whether or not a magnetic field is applied to the growing crystal. It can be seen that portions with different concentrations can be formed.

更に、第6図は、容器2の回転数を変えたとき
の結晶10中の酸素濃度を測定したもので、第6
図中○印は、結晶10の回転数を50rpmとした場
合、△印は30rpmとした場合の各測定値を示す。
この場合、磁場の強さは3500ガウスとしたが、こ
の第6図より明らかなように、磁場が印加された
場合においても、容器2の回転数を大とすれば、
むしろ従前の磁場の印加がなされないCZ法にお
けるよりも高い濃度が得られることがわかる。そ
して、この容器2の回転数の選定により、結晶1
0中の酸素濃度は2.5×1018atoms/cm3にも及ぼす
ことができ、容器2の回転数0.1〜20rpmの範囲
で、結晶10中の酸素濃度を約1桁も変化させる
ことができることがわかる。
Furthermore, FIG. 6 shows the measurement of the oxygen concentration in the crystal 10 when the rotation speed of the container 2 was changed.
In the figure, the ○ mark indicates each measured value when the rotation speed of the crystal 10 was set to 50 rpm, and the △ mark indicates each measured value when the rotation speed was set to 30 rpm.
In this case, the strength of the magnetic field was 3500 Gauss, but as is clear from Fig. 6, even when a magnetic field is applied, if the rotation speed of the container 2 is increased,
In fact, it can be seen that a higher concentration can be obtained than in the conventional CZ method in which no magnetic field is applied. By selecting the rotation speed of this container 2, the crystal 1
The oxygen concentration in the crystal 10 can be as high as 2.5×10 18 atoms/cm 3 , and the oxygen concentration in the crystal 10 can be changed by about one order of magnitude within the range of the rotation speed of the container 2 from 0.1 to 20 rpm. Recognize.

上述したところから明らかなように、容器2の
回転によつて、結晶10中の酸素濃度を低濃度か
ら高濃度にまで変化させることができるものであ
り、この場合に、第2図で説明したところから明
らかなように、印加磁場を1500ガウス以上に選定
すれば、磁場の変動による酸素濃度への影響を回
避でき、また第3図で説明したように、結晶10
と容器2の内壁面との距離を十分大に、例えば69
mmに選定するときは、結晶10の回転速度が結晶
10中の酸素濃度に与える影響を回避できるの
で、容器2の回転数の制御のみで結晶10中の例
えば酸素濃度を制御できるのでこの濃度の設定を
正確に行うことができる。そして、この濃度の選
定範囲は、1×1017〜2.5×1018atoms/cm3という
広範囲のものである。そして、上述したように結
晶10と容器2の内壁面との距離を大に選定する
ことによつて結晶10の回転数を任意に選ぶこと
ができるので、この結晶回転数を、第4図で示さ
れるように、結晶中の半径方向に関して均一な濃
度分布を得ることのできる回転数の約30rpm以上
に選定することができる。
As is clear from the above, by rotating the container 2, the oxygen concentration in the crystal 10 can be changed from a low concentration to a high concentration. As is clear from the above, if the applied magnetic field is selected to be 1500 Gauss or higher, it is possible to avoid the influence of magnetic field fluctuations on the oxygen concentration, and as explained in Figure 3, the crystal 10
Make the distance between the inner wall of container 2 sufficiently large, for example 69
mm, it is possible to avoid the influence of the rotational speed of the crystal 10 on the oxygen concentration in the crystal 10, and therefore the oxygen concentration in the crystal 10 can be controlled only by controlling the rotational speed of the container 2. Settings can be made accurately. The selected concentration range is a wide range of 1×10 17 to 2.5×10 18 atoms/cm 3 . As mentioned above, by selecting a large distance between the crystal 10 and the inner wall surface of the container 2, the rotation speed of the crystal 10 can be arbitrarily selected. As shown, the rotation speed can be selected to be about 30 rpm or more, which is the speed at which a uniform concentration distribution in the radial direction in the crystal can be obtained.

上述したように、本発明によれば、酸素濃度を
結晶10の半径方向、すなわち横断面に関して各
部均一にすることができ、しかもその濃度を、広
範囲に亘つて制御することができるので、冒頭に
述べたように、イントリンシツク・ゲツタリング
効果を得る程度の濃度に選定するとか、サーマル
ドナー効果を得る濃度にするとか、或いはこれら
の効果が生じないような濃度にするとかの選定が
でき、目的に応じた酸素濃度の選定ができるので
実用上の利益は極めて大である。
As described above, according to the present invention, the oxygen concentration can be made uniform in each part in the radial direction, that is, in the cross section of the crystal 10, and the concentration can be controlled over a wide range. As mentioned above, it is possible to select a concentration that produces an intrinsic gettering effect, a concentration that produces a thermal donor effect, or a concentration that does not produce any of these effects, depending on the purpose. Since the oxygen concentration can be selected according to the situation, the practical benefits are extremely large.

また、本発明方法によるときは、結晶10の横
断面における濃度分布は一様にし、引上げ方向に
関する濃度を、その結晶10の引上げ育成位置に
応じて容器2の回転数を変化させることによつて
酸素濃度の異る層を形成することができるので、
例えば第7図に示すように、結晶10の引上げ方
向に関して、酸素濃度が、例えば2×
1017atoms/cm3程度に低い層31と、その濃度が
例えば2.5×1018atoms/cm3程度に高い層32とを
順次形成し、この結晶10からウエフアを切り出
すことによつて、例えば第8図に示すように、半
導体装置の活性領域となる部分を低濃度層31に
よつて形成し、その裏面を高濃度層32によつて
構成し、熱処理することによつて、層32の高濃
度に存在する酸素によつて生ずる欠陥を活性領域
の裏面に形成し、これにより活性領域に存在する
有害不純物、欠陥発生核のゲツタリングを行うよ
うにすることができる。
Further, when using the method of the present invention, the concentration distribution in the cross section of the crystal 10 is made uniform, and the concentration in the pulling direction is changed by changing the rotation speed of the container 2 depending on the pulling and growing position of the crystal 10. Since layers with different oxygen concentrations can be formed,
For example, as shown in FIG. 7, with respect to the pulling direction of the crystal 10, the oxygen concentration is, for example, 2
For example, by sequentially forming a layer 31 with a low concentration of about 10 17 atoms/cm 3 and a layer 32 with a high concentration of about 2.5×10 18 atoms/cm 3 and cutting a wafer from this crystal 10, As shown in FIG. 8, the part that will become the active region of the semiconductor device is formed of a low concentration layer 31, the back surface of which is formed of a high concentration layer 32, and heat treatment is performed to increase the high concentration of the layer 32. Defects caused by the concentration of oxygen can be formed on the back surface of the active region, thereby gettering harmful impurities and defect generation nuclei present in the active region.

また、或いは結晶10自体にその引上げに際し
p型不純物のドーピングを行つておき、引上げ位
置に応じて、容器2の回転数を変化させて結晶1
0の引上げ方向に関して酸素濃度の高い層と、低
い層とが繰返えし積層された結晶を形成し、その
後の熱処理によつて、サーマルドナーを発生させ
て酸素濃度の高い部分をn型化し、酸素濃度の低
い部分によるp型層との繰返えし積層によつてス
タツキングダイオードを得ることもできる。
Alternatively, the crystal 10 itself may be doped with a p-type impurity when the crystal 10 is pulled, and the rotation speed of the container 2 may be changed depending on the pulling position.
A layer with high oxygen concentration and a layer with low oxygen concentration are repeatedly stacked to form a crystal in the pulling direction of zero, and through subsequent heat treatment, a thermal donor is generated and the portion with high oxygen concentration becomes n-type. A stacking diode can also be obtained by repeatedly stacking a p-type layer with a portion having a low oxygen concentration.

上述したように本発明によれば、結晶中の例え
ば酸素濃度の選定を広範囲に亘つて行うことがで
きることによつて各種の特性の良い半導体装置を
廉価に製造でき、その工業的利益は甚大である。
As described above, according to the present invention, for example, the oxygen concentration in the crystal can be selected over a wide range, so that semiconductor devices with various good characteristics can be manufactured at low cost, and the industrial benefits thereof are enormous. be.

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

第1図は本発明による結晶成長法を実施する装
置の一例の構成図、第2図ないし第6図は本発明
の説明に供する測定曲線図、第7図は本発明によ
る結晶成長法によつて得る結晶の一例断面図、第
8図はこれより得たウエフアの拡大断面図であ
る。 1は結晶成長装置、2は結晶材料液3の収容容
器、4は加熱手段、5はそのヒーター、7は磁場
発生手段、8は単結晶シード、10は育成された
結晶である。
FIG. 1 is a block diagram of an example of an apparatus for carrying out the crystal growth method according to the present invention, FIGS. 2 to 6 are measurement curve diagrams used to explain the present invention, and FIG. FIG. 8 is an enlarged cross-sectional view of a wafer obtained from this. Reference numeral 1 designates a crystal growth apparatus, 2 a storage container for a crystal material liquid 3, 4 a heating means, 5 a heater thereof, 7 a magnetic field generating means, 8 a single crystal seed, and 10 a grown crystal.

Claims (1)

【特許請求の範囲】[Claims] 1 電気伝導性を有する結晶成長用液体が収容さ
れた容器と、上記液体から結晶を回転させながら
引き上げる手段と、上記液体に所定方向の静磁場
を印加する手段と、上記容器を回転させる手段と
を設け、上記結晶と上記容器の内壁面との距離
を、該結晶中の容器構成成分の含有濃度が上記結
晶の回転数に依存しない距離とし、上記容器の回
転数を変化させて上記結晶中の容器構成成分の含
有濃度を制御することを特徴とする結晶成長方
法。
1. A container containing an electrically conductive crystal growth liquid, means for rotating and pulling up a crystal from the liquid, means for applying a static magnetic field in a predetermined direction to the liquid, and means for rotating the container. The distance between the crystal and the inner wall surface of the container is such that the concentration of the container constituent components in the crystal does not depend on the rotation speed of the crystal, and the rotation speed of the container is changed to A crystal growth method characterized by controlling the concentration of constituent components of a container.
JP17120581A 1981-10-26 1981-10-26 KETSUSHOSEICHOHOHO Expired - Lifetime JPH0244799B2 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
JP17120581A JPH0244799B2 (en) 1981-10-26 1981-10-26 KETSUSHOSEICHOHOHO
CA000414053A CA1223798A (en) 1981-10-26 1982-10-22 Process for solidification of materials
GB08230370A GB2109267B (en) 1981-10-26 1982-10-25 Processes for solidifying liquid materials
FR8217924A FR2515216B1 (en) 1981-10-26 1982-10-26 METHOD FOR SOLIDIFYING MATERIALS SUCH AS SEMICONDUCTORS, DIELECTRICS OR MAGNETIC MATERIALS
NL8204133A NL8204133A (en) 1981-10-26 1982-10-26 METHOD FOR MAKING CRYSTALS
DE19823239570 DE3239570C2 (en) 1981-10-26 1982-10-26 Process for controlling the oxygen concentration of silicon single crystals

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17120581A JPH0244799B2 (en) 1981-10-26 1981-10-26 KETSUSHOSEICHOHOHO

Publications (2)

Publication Number Publication Date
JPS5874594A JPS5874594A (en) 1983-05-06
JPH0244799B2 true JPH0244799B2 (en) 1990-10-05

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Country Link
JP (1) JPH0244799B2 (en)
CA (1) CA1223798A (en)
DE (1) DE3239570C2 (en)
FR (1) FR2515216B1 (en)
GB (1) GB2109267B (en)
NL (1) NL8204133A (en)

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US4565671A (en) * 1983-08-05 1986-01-21 Kabushiki Kaisha Toshiba Single crystal manufacturing apparatus
JPS60137892A (en) * 1983-12-26 1985-07-22 Toshiba Ceramics Co Ltd Quartz glass crucible
JPS6153187A (en) * 1984-08-24 1986-03-17 Sony Corp Device for growing single crystal
EP0173764B1 (en) * 1984-08-31 1989-12-13 Gakei Electric Works Co., Ltd. Single crystal growing method and apparatus
JPS62105998A (en) * 1985-10-31 1987-05-16 Sony Corp Production of silicon substrate
US4836788A (en) * 1985-11-12 1989-06-06 Sony Corporation Production of solid-state image pick-up device with uniform distribution of dopants
JPS62202528A (en) * 1986-03-03 1987-09-07 Toshiba Corp Manufacture of semiconductor substrate
US4659423A (en) * 1986-04-28 1987-04-21 International Business Machines Corporation Semiconductor crystal growth via variable melt rotation
JP2561072B2 (en) * 1986-04-30 1996-12-04 東芝セラミツクス株式会社 Single crystal growth method and apparatus
JP2556966B2 (en) * 1986-04-30 1996-11-27 東芝セラミツクス株式会社 Single crystal growing equipment
JPS645992A (en) * 1987-06-29 1989-01-10 Sony Corp Method for growing crystal
JP2651481B2 (en) * 1987-09-21 1997-09-10 株式会社 半導体エネルギー研究所 How to make superconducting materials
JPH01282185A (en) * 1988-05-09 1989-11-14 Nippon Telegr & Teleph Corp <Ntt> Method for growing crystal
JPH0431386A (en) * 1990-05-25 1992-02-03 Shin Etsu Handotai Co Ltd Pulling up semiconductor single crystal
JPH0442894A (en) * 1990-06-07 1992-02-13 Shin Etsu Handotai Co Ltd Growth of silicon single crystal
JP2767074B2 (en) * 1990-07-13 1998-06-18 信越半導体 株式会社 Silicon single crystal pulling method
US5196085A (en) * 1990-12-28 1993-03-23 Massachusetts Institute Of Technology Active magnetic flow control in Czochralski systems
JP2734445B2 (en) * 1996-04-16 1998-03-30 ソニー株式会社 Crystal growth method
JP4463957B2 (en) 2000-09-20 2010-05-19 信越半導体株式会社 Silicon wafer manufacturing method and silicon wafer
JP6680108B2 (en) 2016-06-28 2020-04-15 株式会社Sumco Method for producing silicon single crystal

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Also Published As

Publication number Publication date
CA1223798A (en) 1987-07-07
DE3239570A1 (en) 1983-05-05
NL8204133A (en) 1983-05-16
GB2109267A (en) 1983-06-02
GB2109267B (en) 1984-12-05
JPS5874594A (en) 1983-05-06
FR2515216A1 (en) 1983-04-29
DE3239570C2 (en) 1993-11-18
FR2515216B1 (en) 1985-09-13

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