JPS5910960B2 - Continuous pulling single crystal production method and equipment - Google Patents

Continuous pulling single crystal production method and equipment

Info

Publication number
JPS5910960B2
JPS5910960B2 JP3173578A JP3173578A JPS5910960B2 JP S5910960 B2 JPS5910960 B2 JP S5910960B2 JP 3173578 A JP3173578 A JP 3173578A JP 3173578 A JP3173578 A JP 3173578A JP S5910960 B2 JPS5910960 B2 JP S5910960B2
Authority
JP
Japan
Prior art keywords
single crystal
crystal material
crucible
rod
opening
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
Application number
JP3173578A
Other languages
Japanese (ja)
Other versions
JPS54124878A (en
Inventor
福彦 菅
憲治 冨沢
慎一郎 小林
忠昭 須川
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.)
Mitsubishi Metal Corp
Original Assignee
Mitsubishi Metal 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 Mitsubishi Metal Corp filed Critical Mitsubishi Metal Corp
Priority to JP3173578A priority Critical patent/JPS5910960B2/en
Publication of JPS54124878A publication Critical patent/JPS54124878A/en
Publication of JPS5910960B2 publication Critical patent/JPS5910960B2/en
Expired 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)

Description

【発明の詳細な説明】 本発明は引上法(こより半導体用単結晶を成長させる際
の新しい方法と装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a new method and apparatus for growing single crystals for semiconductors by pulling.

一般に電子工業用に使用される半導体単結晶は、シリコ
ンを例にとれば工業的には高純度シリコン多結晶を原料
としてチョクラルスキ一式引上法(以下CZ法と略称)
または帯溶融法(以下FZ法と略称)によって製造され
ている。
Semiconductor single crystals that are generally used in the electronics industry, taking silicon as an example, are industrially produced using the Czochralski set pulling method (hereinafter abbreviated as the CZ method) using high-purity silicon polycrystals as raw materials.
Alternatively, it is manufactured by a zone melting method (hereinafter abbreviated as FZ method).

近年、大規模集積回路製造技術の進歩により1個の電子
回路がますます微小化する一方、力日工基板となるシリ
コン単結晶ウエハーの面積を大きくして1回のプロセス
でウエハー中に形blされる回路数の増大をはかること
により、1つの回路当りのコストの低減がはかられてい
る。
In recent years, advances in large-scale integrated circuit manufacturing technology have resulted in the miniaturization of single electronic circuits, while increasing the area of single-crystal silicon wafers that serve as substrates, allowing the fabrication of BL into wafers in a single process. By increasing the number of circuits used, the cost per circuit is reduced.

そのため単結晶製造技術に対し、大直径化が絶えず要求
されているが、同時に単結晶製造時の時間当りの生産性
を高めるため一本の結晶の長さを長くする方向も追求さ
れている。
For this reason, there is a constant demand for larger diameters in single crystal manufacturing technology, but at the same time, efforts are also being made to increase the length of each crystal in order to increase productivity per unit of time during single crystal manufacturing.

単結晶の大直径化QこはCZ法が適し、すでに直径5〜
6インチの単結晶が得られているのみならず、自動直径
制御や原料多結晶のりチャージによる半連続化等の技術
改良が進んでコスト面でもFZ法をしのいでいる。
The CZ method is suitable for increasing the diameter of single crystals.
Not only has a 6-inch single crystal been obtained, but technological improvements such as automatic diameter control and semi-continuous processing using raw material polycrystalline glue charging have progressed, and the method surpasses the FZ method in terms of cost.

しかし従来のCZ法には下記(1)〜(3)の問題点が
存在し、なお未解決のままに残されていた。
However, the conventional CZ method has the following problems (1) to (3), which remain unsolved.

(1)電子デバイスの設計上最も重要な因子である抵抗
率は、単結晶中にドープされる不純物(ドーパント)濃
度できまるが、現行のCZ法Cこおいては引上方向のド
ーパント濃度の増大が避けられないため、所望の抵抗率
の単結晶を得るには引上長さに限界が生じた。
(1) Resistivity, which is the most important factor in the design of electronic devices, is determined by the impurity (dopant) concentration doped into the single crystal, but in the current CZ method, the dopant concentration in the pulling direction is Since the increase is unavoidable, there is a limit to the pulling length in order to obtain a single crystal with a desired resistivity.

なんとなれば融液中に添加されたドーパントはその個有
の偏析係数に従って単結晶中に取り込まれる割合が決ま
っているが、シリコンの場合、酸素を除くほとんどの不
純物が偏析係数1以下で融液中に残される割合が大きい
ため、引上げが進むに従って融液中のドーパント濃度が
高くなり、その結果単結晶中にとりこまれるドーパン十
の量も増し、ついには目標の抵抗率を低く外れる程の高
濃度に達してしまうのである3またたとカ万望の抵抗率
範囲内にあっても、切出されたウエハーの抵抗率が各ウ
エノ1−ごとに異なる値になることは避けられなかった
The proportion of dopants added to the melt that is incorporated into the single crystal is determined according to its unique segregation coefficient, but in the case of silicon, most impurities, except for oxygen, are incorporated into the melt with a segregation coefficient of less than 1. Because a large proportion of the dopant remains in the melt, as the pulling progresses, the dopant concentration in the melt increases, and as a result, the amount of dopant incorporated into the single crystal increases, and eventually the resistivity becomes so high that it deviates from the target resistivity. Even if the resistivity was within the desired range, it was inevitable that the resistivity of the cut wafers would be different for each wafer.

(2)従来、CZ法の半連続化の一手段として、所定の
大きさの単結晶を引き上げた後、不活性ガスの流通下に
炉を開き、新しいシリコン多結晶をるつぼ内に装填して
新たに引上げを行なういわゆるリチャージ方式が一般に
行なわれているが、この方法では多結晶リチャージの際
引上炉内部への酸素の侵入が避けられず、この酸素が炉
内のグラファイト部品をおかして一酸化炭素を生じ、つ
いには結晶中の炭素濃度を増加せしめるに至る。
(2) Conventionally, as a means of making the CZ method semi-continuous, after pulling a single crystal of a predetermined size, the furnace was opened under the flow of inert gas, and new silicon polycrystals were loaded into the crucible. Generally, a so-called recharge method is used in which a new pulling process is performed, but this method cannot avoid the intrusion of oxygen into the pulling furnace during polycrystalline recharging. Carbon oxide is produced, which ultimately leads to an increase in the carbon concentration in the crystal.

(3)一般に結晶欠陥の少ない良質の単結晶を得るため
には固液界面の形状が平坦であることが望まれるが、実
際にはCZ法においては結晶成長が進むにつれて融液面
が沈下するため、発熱体と溶融液体との位置関係が変化
して固液界而の形状を変化せしめる。
(3) Generally, in order to obtain a high-quality single crystal with few crystal defects, it is desirable that the shape of the solid-liquid interface be flat, but in reality, in the CZ method, the melt surface sinks as the crystal growth progresses. Therefore, the positional relationship between the heating element and the molten liquid changes, causing the shape of the solid-liquid interface to change.

このため相対位置か変化しないように融液面の沈下に応
じてるつぼを上昇させることが行われているが、今度は
るつぼ上端の熱しゃへい効来が変化して固液界面の温度
分布を変化させてしまう。
For this reason, the crucible is raised in response to the sinking of the melt surface so that the relative position does not change, but this time the heat shielding effect at the top of the crucible changes, changing the temperature distribution at the solid-liquid interface. I'll let you.

本発明は、これらの問題点を根本的に解決した新規なC
Z法の改良法を提供するものである。
The present invention is a new C
This provides an improved method of the Z method.

すなイつち、引上げるつぼに引上げ炉を開くことなく連
続的にシリコン溶融液およびドーパントを供給しつつ引
上げを行うことにより、引上げ方向のドーパントの分布
を均一ならしめ、かつ融液面のレベルが一定に保たれる
ことやりチャージの際に引上炉を開く必要がないことか
ら 結晶性の向]一をも達成し得るものである。
In other words, by continuously supplying the silicon melt and dopant to the pulling crucible without opening the pulling furnace, the dopant distribution in the pulling direction can be made uniform, and the level of the melt surface can be made uniform. Since it is not necessary to open the pulling furnace during charging, it is possible to achieve even better crystallinity.

本発明によれば、チョクラルスキ一式連続引上単結晶製
造法lこおいて、底部に円形開[]を有する単結晶用材
料融解容器を用い、該容器の温度分布を容器内部では融
浴を維持する温度に、該円形開口部では単結晶用材料が
凝固し始める温度であるように維持し、該円形開口から
、該円形開口の断面に一致する断面を有する棒状の単結
晶用材料を単結晶引上製造による浴の減少を補償する速
度で導入することを特徴とする方法が提供される。
According to the present invention, in the Czochralski continuous pulling single crystal production method, a single crystal material melting vessel having a circular opening at the bottom is used, and the temperature distribution of the vessel is controlled to maintain a molten bath inside the vessel. The circular opening is maintained at a temperature at which the single-crystal material starts to solidify, and a rod-shaped single-crystal material having a cross section that corresponds to the cross-section of the circular opening is fed into the single crystal through the circular opening. A method is provided which is characterized in that it is introduced at a rate that compensates for the loss of bath due to pull production.

本発明によれば、さらに単結晶用材料を融解するための
底部中央に円形の開口を有するるつぼであって該開口の
縁部が該るつぼの軸方向に下方に中空円筒状に延長して
いるもの:該円筒に固定されてそれが回転されることに
よって前記るつぼが回転される下端に前記るつぼの開口
から挿入されるべき棒状単結晶用材料を受け入れる開口
を有する回転シャフト、該回転シャフトを回転1駆動す
る千段;前記のるつぼをその杯状体部の温度を単結晶用
材料を融解する温度に、その底部開口部を該材料が凝固
し始める温度に保持するように温度分布を保つように加
熱する手段;前記の各部材を収納しその上部に前記るつ
ぼ内の単結晶用材料の融浴から種結晶をもって単結晶棒
を回転しながら引き上げる手段が出入できる開「1を有
し内部に気体を流通させることのできる炉体;該引き上
げ千段;およひ前記回転シャフトと前記るつぼの開口を
通じて棒状単結晶用材料を融浴内に挿入するための十ド
運動と回転運動できる単結晶用材料支持台を含む連続引
上式単結晶製造装置が提供される。
According to the present invention, there is further provided a crucible having a circular opening at the center of the bottom for melting the single crystal material, the edge of the opening extending downward in the axial direction of the crucible into a hollow cylindrical shape. A rotary shaft that is fixed to the cylinder and has an opening at the lower end of which the crucible is rotated by receiving the rod-shaped single crystal material to be inserted from the opening of the crucible, and rotates the rotary shaft. 1, driven by 1,000 stages; the temperature distribution is maintained so that the temperature of the cup-shaped body of the crucible is maintained at a temperature at which the single crystal material is melted, and the bottom opening is maintained at a temperature at which the material begins to solidify. means for storing each of the above-mentioned members and having an opening 1 in the upper part thereof through which a means for rotating and pulling up a single-crystal rod with a seed crystal from the molten bath of the single-crystal material in the crucible can be accessed and removed; a furnace body through which gas can flow; the lifting stage; and a single crystal capable of ten-dot movement and rotational movement for inserting the rod-shaped single crystal material into the molten bath through the rotating shaft and the opening of the crucible. A continuous pulling single crystal manufacturing apparatus is provided, including a material support for the invention.

本発明の方法と装置は半導体用材料一般の単結晶製造に
利川できるものであるが、以下の図面を参照した具体的
説明は代表的半導体材科であるシリコンについてなされ
る。
Although the method and apparatus of the present invention can be used to manufacture single crystals of semiconductor materials in general, the following detailed description with reference to the drawings will be made for silicon, which is a typical semiconductor material.

本発明の方法に使用される装置は第1図にその概念が示
される。
The concept of the apparatus used in the method of the present invention is shown in FIG.

本発明の装置の中心をなす底に開[1を有するるつぼ2
は通常石英で造られるが、他ζこシリコンナイトライド
、または石英、ボロンナイトライド、グラファイト等の
表面にシリコンナイトライド、またはシリコンオキシナ
イトライトのコーティングを施したものも使用し得る。
Crucible 2 with an opening [1] in the bottom forming the center of the device of the invention
is usually made of quartz, but other materials such as silicon nitride, quartz, boron nitride, graphite, etc. whose surfaces are coated with silicon nitride or silicon oxynitrite may also be used.

このるつほ通常グラファイト製のサセプタ−3によって
支持されるが、サセプター自身は必須ではない。
This support is usually supported by a susceptor 3 made of graphite, but the susceptor itself is not essential.

るつぼ2は単結晶用材料すなわちシリコンを融解する杯
状部と底の円形開口の縁部より筒状に下方に延びる中空
円筒部2′を有する。
The crucible 2 has a cup-shaped part for melting the single crystal material, ie, silicon, and a hollow cylindrical part 2' extending downward in a cylindrical shape from the edge of the circular opening at the bottom.

この中空円筒部には円筒状の回転シャフト7が固定され
ている。
A cylindrical rotating shaft 7 is fixed to this hollow cylindrical portion.

この回転シャフト7には底部に開[」11が設けられて
おり、ここより棒状単結晶用材料(多結晶シリコン棒)
20が挿入され、さらに中空円筒2′を介して、るつぼ
2の底部開1夕]に挿入されるようになっている。
This rotary shaft 7 is provided with an opening 11 at the bottom, from which a rod-shaped single crystal material (polycrystalline silicon rod) is inserted.
20 is inserted into the bottom opening of the crucible 2 via the hollow cylinder 2'.

シリコン棒と回転シャフト7の底部開[」11の間はシ
リコンゴム、テフロン等の通常のシール材料でシールさ
れる。
The space between the silicon rod and the bottom opening 11 of the rotating shaft 7 is sealed with a common sealing material such as silicone rubber or Teflon.

るつぼ2(およびサセプタ−3)の外側には主ヒーター
4と補助ヒーター5が配置され、るつぼ内の温度分布が
シリコンの場合第3図に示されるようになるように調整
される。
A main heater 4 and an auxiliary heater 5 are arranged outside the crucible 2 (and susceptor 3), and the temperature distribution inside the crucible is adjusted as shown in FIG. 3 in the case of silicon.

ヒーターは通常電気抵抗加熱または高周波加熱方式であ
るが、これに限定されるものではない。
The heater is usually of an electric resistance heating type or a high frequency heating type, but is not limited thereto.

以上説明した部材は回転ノヤフト7の下部を残して炉体
1内に収納さイtる。
The members described above are stored in the furnace body 1, leaving the lower part of the rotary shaft 7 intact.

炉は通常ステンレス鋼製で、前記部材の収納取外し修理
調整に便利であるように適当に分割して構造され、回転
シャフトの挿入部の底部開口12にはンヤフトとの間は
シリコンゴムやテフロンのようなシール材料でシールさ
れる。
The furnace is usually made of stainless steel, and is divided into sections for convenient storage, removal, repair, and adjustment of the above-mentioned parts.The bottom opening 12 of the insertion part of the rotating shaft is made of silicone rubber or Teflon between the shaft and the shaft. sealed with a sealing material such as

炉体1の上方には、単結晶引上用シャフト9が通過する
上部開[厘121があり、これはスライドバルブ13で
開閉される。
Above the furnace body 1, there is an upper opening 121 through which the single crystal pulling shaft 9 passes, and this is opened and closed by a slide valve 13.

引上げられる単結晶18を保護するためのベロウ(通常
ステンレス製)22を設けてもよい。
A bellows (usually made of stainless steel) 22 may be provided to protect the single crystal 18 being pulled.

炉にはまたのぞき窓16を設けてもよい。The furnace may also be provided with a viewing window 16.

また炉体には熱しゃへい体6を設けてもよい。Further, a heat shielding body 6 may be provided in the furnace body.

通常不活性ガスを導入するための弁を備えた供給管15
が設けられる。
Supply pipe 15, usually equipped with a valve for introducing inert gas
is provided.

不活性ガスは通常上部の開[−1へ吹き抜けとなる。Inert gas usually blows through the upper opening [-1.

炉体1の下方には、そこに突き出した回転シャフト7を
回転させる回転駆動手段10、多結晶シリコン棒20を
上昇させるための回転上下運動する棒状単結晶用材料支
持台8、多結晶シリコン棒20を保持する支持アーム1
4などが設けられる。
Below the furnace body 1, there are a rotary drive means 10 for rotating a rotary shaft 7 protruding therefrom, a rod-shaped single crystal material support 8 that rotates and moves up and down to raise the polycrystalline silicon rod 20, and a polycrystalline silicon rod. Support arm 1 holding 20
4 etc. are provided.

これらの装置は当業者は上記の情報をもとにして容易に
製造することができる。
These devices can be easily manufactured by those skilled in the art based on the above information.

この装置を用いて、シリコン単結晶を製造するにはまず
回転シャフト7の底部開口11から単結晶用材料支持台
8に保持させた所定の即ちるつぼの開口のそれに等しい
直径の円筒に研削したシリコン多結晶棒20を、該支持
台8の図中に示されていない上昇機構を作動させて挿入
し、石英中空円筒2lを貫通して石英るつぼ2の底部開
[1に寸で至らしめる。
To manufacture a silicon single crystal using this device, first, silicon is ground from the bottom opening 11 of the rotating shaft 7 into a cylinder with a diameter equal to that of the opening of a predetermined crucible held on the single crystal material support 8. The polycrystalline rod 20 is inserted by activating the lifting mechanism (not shown in the figure) of the support base 8, passes through the quartz hollow cylinder 2l, and reaches the bottom opening [1] of the quartz crucible 2.

このとき多結晶供給口11は回転シャフト7のシールド
部12と共にシール材を用いて十分な気密シールがほど
こされている。
At this time, the polycrystal supply port 11 and the shield portion 12 of the rotating shaft 7 are sufficiently airtightly sealed using a sealing material.

次いで炉上部を開いて所定量のシリコン多結晶をるつぼ
中に装填した後、従来法と同様の操作で炉内に不活性ガ
スを満たし、抵抗加熱方式または高周波加熱方式による
主ヒーター4と補助ヒーター5を稼動させ、るつぼに装
填したシリコン多結晶を溶融せしめる。
Next, the upper part of the furnace is opened and a predetermined amount of polycrystalline silicon is loaded into the crucible, and then the inside of the furnace is filled with inert gas in the same manner as in the conventional method, and the main heater 4 and auxiliary heater are heated using resistance heating or high frequency heating. 5 is operated to melt the silicon polycrystals loaded in the crucible.

この際、石英るつぼ2と石英中空円筒2′の内部が第2
図に示す温度分布となるように制御することにより、多
結晶シリコンは第2図のイ,口の間の部分では溶融体と
して存在し、口,ハの間の部分では凝固して融液が下部
へこぼれ落ちることがないのみならず、多結晶支持台8
の運動に伴うシリコン多結晶棒20の上昇や回転を妨げ
ない。
At this time, the inside of the quartz crucible 2 and the quartz hollow cylinder 2' is
By controlling the temperature distribution as shown in the figure, polycrystalline silicon exists as a molten body in the area between the openings and openings in Figure 2, and solidifies in the area between the openings and c. Not only will it not spill to the bottom, but the polycrystalline support 8
The rise and rotation of the silicon polycrystalline rod 20 accompanying the movement of the silicon polycrystalline rod 20 is not hindered.

このような状態で、回転シャフト7を回転させて石英る
つほ2に回転を伝えると共に、種結晶17を装着した引
−ヒげシャフト9を下降せしめ従来法とまったく同様に
して単結晶18の引上げを開始する。
In this state, the rotary shaft 7 is rotated to transmit rotation to the quartz crystal 2, and the pull shaft 9 on which the seed crystal 17 is attached is lowered, and the single crystal 18 is grown in exactly the same manner as in the conventional method. Start lifting.

一方同時に、引上げられた単結晶の量に等しい融液19
を補給してやるため、単結晶用材料支持台8を上昇させ
てシリコン多結晶20を第2図イ,口の溶融ゾーンに移
動させれば、融液19の表面レベルを常に一定に保つこ
とが可能となり、引上装置の引上1駆動距離の続く限り
同一条件で引上げを行なうことができるのみならず、原
料中に含まれる不純物に関してはFZ法の場合とまった
く同様に溶融した際に常に一定濃度の融液を生ずるため
、づ1上げられる単結晶の全長にわたって均一な不純物
濃度が達成され、その結果均一な抵抗率分布をもった単
結晶がもたらされるに至る。
At the same time, melt 19 equal to the amount of the single crystal pulled up
In order to replenish the melt, the surface level of the melt 19 can be kept constant by raising the single crystal material support 8 and moving the silicon polycrystal 20 to the melting zone shown in Figure 2A. Therefore, not only can pulling be carried out under the same conditions as long as the pulling distance of the pulling device continues, but the concentration of impurities contained in the raw material will always be constant when melted, just as in the case of the FZ method. As a result, a uniform impurity concentration is achieved over the entire length of the raised single crystal, resulting in a single crystal with a uniform resistivity distribution.

さらにシリコン多結晶20の供給は支持台8が上昇して
シリコン多結晶供給「111に近づいたとき、伸縮自在
の支持アーム14でシリコン多結晶を保持しつつ支持台
8を下降させて新しい多結晶棒を継ぎたしでやることが
可能なため、必要なだけいくらでも供給してやることが
できる。
Further, the supply of the silicon polycrystal 20 is carried out when the support stand 8 rises and approaches the silicon polycrystal supply 111, the support stand 8 is lowered while holding the silicon polycrystal with the extendable support arm 14, and a new polycrystal is supplied. Since it can be done by splicing sticks together, you can supply as much or as little as you need.

しかもこの操作には炉を開閉したり加熱を止めたりする
必要がないため、外部からの望ましくない不純物による
汚染もなく、かつ従来のりチャージ法に比へて著るしく
操作時間が短縮された。
Moreover, since this operation does not require opening and closing the furnace or stopping heating, there is no contamination by undesirable external impurities, and the operating time is significantly reduced compared to the conventional glue charging method.

ドーピング法に関しては、先に述べたあらかじめドーピ
ングした原料を使用する方法だけでなく、ドーパントを
細線状にして棒状単結晶用材料にそえて(棒状材料にそ
のための縦溝を設けてもよい少導入してもよく、また比
較的短い棒状材料を用いて、その継ぎたしと同様にして
ドーパントを添加してやる方法も町能なため、抵抗率の
分布の幅をきわめてせまい範囲に限定することができる
Regarding the doping method, there is not only the method of using pre-doped raw materials mentioned above, but also the method of making the dopant into a thin wire and placing it on the rod-shaped single crystal material (a vertical groove for this purpose may be provided in the rod-shaped material). It is also possible to add dopants using relatively short rod-shaped materials in the same way as when splicing them together, so the width of the resistivity distribution can be limited to an extremely narrow range. .

一方、所定の長さの単結晶が引上げられた後、第1図の
13で示したスライドバルブの上部に単結晶を移動させ
、バルブ13を閉じて炉内を密閉した」二、図には示さ
れていない結晶取出口を開いて単結晶を取り出し新しい
種結晶につけ換えて次のプロセスを繰りかえすことがで
きるので、高温の溶融体を収容した炉体内には、単結晶
のとり出しにおいても原料多結晶の供給においても外部
からの不純物汚染がなく、かつ操作を中断する必要もな
く、理想的な連続化が可能となる。
On the other hand, after the single crystal of a predetermined length was pulled, the single crystal was moved to the upper part of the slide valve shown by 13 in Figure 1, and the valve 13 was closed to seal the inside of the furnace. By opening the crystal extraction port (not shown), the single crystal can be taken out, replaced with a new seed crystal, and the next process can be repeated. Even in the supply of polycrystals, there is no external impurity contamination, and there is no need to interrupt the operation, making it possible to ideally continue supplying the polycrystal.

上述の装置に関する説明および図面中では省略されてい
るが、この方法及び装置は通常自動制御されている。
Although omitted from the description and drawings of the above-mentioned apparatus, the method and apparatus are typically automatically controlled.

生成する、即ち、引き上げしれる単結晶の重量が常に検
知されていて、その情報を単結晶用材料支持台の上昇機
構にフィードバックして単結晶用材料の融解浴への供給
速度が丁度浴の減少を補償するように制御される。
The weight of the single crystal to be produced, that is, to be pulled, is constantly detected, and this information is fed back to the lifting mechanism of the single crystal material support to ensure that the supply rate of the single crystal material to the melting bath is just that of the bath. controlled to compensate for the decrease.

このような電子回路は当業者が容易に構成し製作できる
ものであるから特に詳細に記す必要はない。
Such electronic circuits do not need to be described in detail since they can be easily constructed and manufactured by those skilled in the art.

融浴減少の検知は浴の液面の変動の監視によってもよい
Detection of molten bath loss may also be by monitoring changes in the bath level.

この場合は光学的もしくは電気的検出手段によって融液
の液面レベルが監視される。
In this case, the level of the melt is monitored by optical or electrical detection means.

かくして現行CZ法のすべての問題点を解決し、連続し
て多数の均一不純物濃度の単結晶引上げを可能ならしめ
た点、本発明の工業的価値は大きい。
The present invention has great industrial value in that it solves all the problems of the current CZ method and makes it possible to continuously pull a large number of single crystals with uniform impurity concentrations.

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

第1図は本発明になる引上単結晶製造装置の断面図であ
る。 図中、1・・・・・・ 、2・・・・・・るつぼ、2′
・・・・・・中空円筒、3・・・・・・グラファイ1・
サセプクー、4・・・・・・主ヒーター、5・・・・・
・補助ヒーター、6・・・・・・熱しゃへい体、7・・
・・・・回転シャフト、8・・・・・・棒状単結晶材料
支持台、9・・・・・・引上げシャフト、10・・・・
・・回転シャフ1ヘ1駆動輪、11・・・・・・気密シ
ール式多結晶供給口、12・・・・・・回転シャフト下
部開1」、13・・・・・・スライドパルフ、14・・
・・・・支持アーム、15・・・・・・不活性ガス供給
口、16・・・・・・のぞき窓、17・・・・・・種結
晶、18・・・・・・引−北単結晶、19・・・・・・
単結晶用材料融液、20・・・・・・棒状単結晶用材料
、21・・・・・・炉体上部開口、22・・・・・・ベ
ロウ。 第2図は第1図の装置の該尚する番号の部分を抜き出し
たものに、その位置に対応する部分の温度分布を示すグ
ラフを対置l−たものである。
FIG. 1 is a sectional view of a pulled single crystal manufacturing apparatus according to the present invention. In the figure, 1..., 2...crucible, 2'
...Hollow cylinder, 3...Graphite 1.
Sasepuku, 4... Main heater, 5...
・Auxiliary heater, 6...Heat shielding body, 7...
... Rotating shaft, 8 ... Rod-shaped single crystal material support stand, 9 ... Pulling shaft, 10 ...
...Rotating shaft 1 to 1 drive wheel, 11...Airtight seal type polycrystalline supply port, 12...Rotating shaft bottom open 1'', 13...Slide palf, 14...
...Support arm, 15...Inert gas supply port, 16...Peephole, 17...Seed crystal, 18...Pull-north Single crystal, 19...
Melt of material for single crystal, 20... Material for rod-shaped single crystal, 21... Upper opening of furnace body, 22... Bellows. FIG. 2 shows a diagram showing the temperature distribution of the portion corresponding to the extracted portion of the apparatus shown in FIG. 1 with the corresponding number.

Claims (1)

【特許請求の範囲】 1 チョクラルスキ一式連続引上単結晶製造法において
、底部に円形開口を有する単結晶用材料融解容器を用い
、該容器の温度分布を容器内部では融浴を維持する温度
に、該円形開口部では単結晶用材料が凝固し始める温度
であるように維持し、該円形開口から、該円形開[」の
断面に一致する断面を有する棒状の単結晶用材料を単結
晶引上製造による浴の減少を補償する速度で導入するこ
とを特徴とする方法。 2 特許請求の範囲第1項記載の方法であって、連続的
に製造される単結晶の重量を検出して、その変動に応じ
て棒状単結晶用材料の導入を加減するように自動制御す
ることを特徴とする方法。 3 特許請求の範囲第1項記載の方法であって、単結晶
用材料の融浴の液面の変動を検出して、その変動に応じ
て棒状単結晶用材料の導入を加減するように自動制御す
ることを特徴とする方法。 4 単結晶用材料を融解するための底部中央に円形の開
[」を有するるつぼであって該開口の縁部が該るつぼの
軸方向に下方に中空円筒状に延長しているもの;該円筒
に固定されてそれが回転されることによって前記るつぼ
が回転される下端に前記るつぼの開[」から挿入される
べき棒状単結晶用材料を受け入れる開口を有する回転シ
ャフト、該回転シャフトを回転駆動する手段;前記のる
つぼをその杯状体部の温度を単結晶用材料を融解する温
度に、その底部開口部を該材料が凝固し始める温度に保
持するように温度分布を保つように加熱する千段;前記
の各部材を収納しその上部に前記るつぼ内の単結晶用材
料の融浴から種結晶をもって単結晶棒を回転しながら引
き上げる手段が出入できる開口を有し内部に気体を流通
させることのできる炉体;該引き上げ千段;および前記
回転シャフトと前記るつぼの開口を通じて棒状単結晶用
材料を融浴内に挿入するための上下運動と回転運動でき
る単結晶用材料支持台を含む連続引上式単結晶製造装置
。 5 特許請求の範囲第4項記載の装置であって、連続的
に製造される単結晶の重量を検出して、その変動に応じ
て棒状単結晶用材料の導入を加減する自動制御機穫を備
えたことを特徴とする装置。 6 特許請求の範囲第5項記載の装置であって、単結晶
用材料の融浴の液面の変動を検出して、その変動に応じ
て棒状単結晶用材料の導入を加減する自動制御機構を備
えたことを特徴とする装置。
[Claims] 1. In the Czochralski continuous pulling single crystal production method, a single crystal material melting vessel having a circular opening at the bottom is used, and the temperature distribution of the vessel is adjusted to a temperature that maintains a molten bath inside the vessel. The temperature in the circular opening is maintained at a temperature at which the single crystal material begins to solidify, and a rod-shaped single crystal material having a cross section matching the cross section of the circular opening is pulled from the circular opening. A method characterized in that the introduction is carried out at a rate that compensates for the loss of bath due to production. 2. The method according to claim 1, which detects the weight of the continuously produced single crystal and automatically controls the introduction of rod-shaped single crystal material in accordance with the fluctuation thereof. A method characterized by: 3. The method according to claim 1, which detects fluctuations in the liquid level of the melt bath of the single crystal material and automatically adjusts the introduction of the rod-shaped single crystal material according to the fluctuation. A method characterized by controlling. 4 A crucible that has a circular opening in the center of the bottom for melting single crystal material, and the edge of the opening extends downward in the axial direction of the crucible into a hollow cylindrical shape; a rotary shaft having an opening at its lower end for receiving rod-shaped single crystal material to be inserted from the opening of the crucible, on which the crucible is rotated by being fixed to the crucible; Means: Heating the crucible so as to maintain a temperature distribution such that the temperature of the cup-shaped body is maintained at a temperature at which the single crystal material is melted, and the bottom opening is maintained at a temperature at which the material begins to solidify. Stage; storing each of the above-mentioned members and having an opening in the upper part through which a means for rotating and pulling up a single-crystal rod with a seed crystal from the molten bath of the single-crystal material in the crucible can enter and exit, and gas can be circulated inside. a continuous puller comprising a furnace body capable of vertical movement and rotational movement for inserting the rod-shaped single crystal material into the molten bath through the rotating shaft and the opening of the crucible; The above type single crystal manufacturing equipment. 5. The device according to claim 4, which includes an automatic control device that detects the weight of the continuously produced single crystal and adjusts or reduces the introduction of rod-shaped single crystal material in accordance with the fluctuation thereof. A device characterized by: 6. The device according to claim 5, which is an automatic control mechanism that detects fluctuations in the liquid level of the molten bath of single crystal material and adjusts or reduces the introduction of the rod-shaped single crystal material in accordance with the fluctuations. A device characterized by comprising:
JP3173578A 1978-03-22 1978-03-22 Continuous pulling single crystal production method and equipment Expired JPS5910960B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3173578A JPS5910960B2 (en) 1978-03-22 1978-03-22 Continuous pulling single crystal production method and equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3173578A JPS5910960B2 (en) 1978-03-22 1978-03-22 Continuous pulling single crystal production method and equipment

Publications (2)

Publication Number Publication Date
JPS54124878A JPS54124878A (en) 1979-09-28
JPS5910960B2 true JPS5910960B2 (en) 1984-03-12

Family

ID=12339285

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3173578A Expired JPS5910960B2 (en) 1978-03-22 1978-03-22 Continuous pulling single crystal production method and equipment

Country Status (1)

Country Link
JP (1) JPS5910960B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0335480Y2 (en) * 1986-12-15 1991-07-26

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0095384A3 (en) * 1982-05-26 1984-12-27 Konica Corporation Vacuum deposition apparatus
KR101265154B1 (en) 2011-05-12 2013-05-27 한국에너지기술연구원 Manufacturing apparatus of single crystal silicon ingot having dual crucible for silicon melting which can recycle

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0335480Y2 (en) * 1986-12-15 1991-07-26

Also Published As

Publication number Publication date
JPS54124878A (en) 1979-09-28

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