JPH0551296A - Method for producing compound semiconductor single crystal - Google Patents

Method for producing compound semiconductor single crystal

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Publication number
JPH0551296A
JPH0551296A JP23113791A JP23113791A JPH0551296A JP H0551296 A JPH0551296 A JP H0551296A JP 23113791 A JP23113791 A JP 23113791A JP 23113791 A JP23113791 A JP 23113791A JP H0551296 A JPH0551296 A JP H0551296A
Authority
JP
Japan
Prior art keywords
concentration
single crystal
compound semiconductor
furnace
gas
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
JP23113791A
Other languages
Japanese (ja)
Inventor
Manabu Kano
学 加納
Yoshinobu Sasaki
慶悦 佐々木
Takanori Tanaka
孝憲 田仲
Soichiro Otani
聡一郎 大谷
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.)
Eneos Corp
Original Assignee
Nikko Kyodo Co 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 Nikko Kyodo Co Ltd filed Critical Nikko Kyodo Co Ltd
Priority to JP23113791A priority Critical patent/JPH0551296A/en
Publication of JPH0551296A publication Critical patent/JPH0551296A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】 (修正有) 【構成】LEC法により化合物半導体単結晶を育成する
方法において、水分量100ppmw以下のB23を使
用し、化合物半導体多結晶を溶融後の炉内雰囲気ガス中
のCO濃度を一定の濃度に制御して所定時間以上放置し
た後、炉内雰囲気ガス中のCO濃度を引き続き同じく一
定の濃度に制御しながら単結晶を育成する。 【効果】炉内雰囲気ガス中のCO濃度のみによって、単
結晶中の炭素濃度を任意の値にテ−ルまで均一に育成す
ることができる。
(57) [Summary] (Modified) [Constitution] In the method for growing a compound semiconductor single crystal by the LEC method, B 2 O 3 having a water content of 100 ppmw or less is used, and the atmosphere in the furnace after melting the compound semiconductor polycrystal is used. After the CO concentration in the gas is controlled to a constant concentration and left for a predetermined time or longer, the single crystal is grown while the CO concentration in the furnace atmosphere gas is continuously controlled to the same concentration. [Effect] The carbon concentration in the single crystal can be uniformly grown to an arbitrary value up to the tail only by the CO concentration in the furnace atmosphere gas.

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LEC法による化合物半
導体単結晶の製造方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a compound semiconductor single crystal by the LEC method.

【0002】[0002]

【従来の技術】GaAs単結晶中の炭素は浅いアクセプ
ターとして作用し、結晶の電気特性やデバイスを作製し
た際にその特性に大きな影響を与える。このため、特に
IC基板用結晶としては、炭素濃度の均一性に優れた単
結晶が望まれている。
2. Description of the Related Art Carbon in a GaAs single crystal acts as a shallow acceptor and greatly affects the electrical characteristics of the crystal and its characteristics when a device is manufactured. For this reason, in particular, as a crystal for an IC substrate, a single crystal excellent in uniformity of carbon concentration is desired.

【0003】化合物半導体単結晶の製造方法として工業
的に用いられているLEC法では、原料融液の炭素濃
度、ひいては結晶の炭素濃度を制御するには、炉内ガス
中のCO濃度を制御する方法が有効であることが知られ
ている。従来ガス中のCO濃度等を制御して化合物半導
体単結晶の炭素濃度を制御する方法としては、特開昭
62−30700、特開平1−242488、特開
平1−239089、特開平1−313398などが
報告されている。,の方法は、COまたはCO2
度を、あるレベル以下にすることで、結晶の炭素濃度を
低減するのが目的で、結晶内の均一性に関しては考慮さ
れていない。の方法はCO濃度を一定に保つことによ
って炭素濃度を制御する方法であるが後述するように、
この場合も均一性の良い結晶は得られない。の方法
は、炭素濃度を制御することで、結晶内の炭素濃度が頭
部で2×1015cm-3〜20×1015cm-3、尾部で頭部濃
度の1/3以上ということで均一性は良くない。これら
従来の方法では、ある程度炭素濃度は制御できるもの
の、IC基板用として充分満足のできる均一性の優れた
結晶は得られない。
In the LEC method, which is industrially used as a method for producing a compound semiconductor single crystal, the CO concentration in the furnace gas is controlled in order to control the carbon concentration in the raw material melt, and thus the carbon concentration in the crystal. The method is known to be effective. Conventional methods for controlling the carbon concentration of a compound semiconductor single crystal by controlling the CO concentration in a gas and the like include JP-A-62-30700, JP-A-1-242488, JP-A-1-239089 and JP-A-1-313398. Has been reported. The method of (1) aims to reduce the carbon concentration of the crystal by making the CO or CO 2 concentration below a certain level, and does not consider the uniformity within the crystal. The method of is a method of controlling the carbon concentration by keeping the CO concentration constant, but as described later,
Also in this case, crystals with good uniformity cannot be obtained. The method is that the carbon concentration in the crystal is 2 × 10 15 cm −3 to 20 × 10 15 cm −3 in the head and 1/3 or more of the head concentration in the tail by controlling the carbon concentration. The uniformity is not good. Although these conventional methods can control the carbon concentration to some extent, they cannot provide sufficiently satisfactory crystals having excellent uniformity for IC substrates.

【0004】[0004]

【発明が解決しようとする問題点】本発明は上記の欠点
を解決したもので、目的は、所定の炭素濃度でかつ、均
一性の優れた化合物半導体単結晶の製造技術を提供する
ことにある。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned drawbacks, and an object thereof is to provide a technique for producing a compound semiconductor single crystal having a predetermined carbon concentration and excellent uniformity. ..

【0005】[0005]

【問題点を解決するための手段及び作用】本発明者らは
先ず、CO濃度一定の条件でGaAs単結晶を育成した
場合に、結晶内で炭素濃度がどのように変化するかを調
べた。
[Means and Actions for Solving Problems] First, the present inventors investigated how the carbon concentration changes in a crystal when a GaAs single crystal is grown under the condition that the CO concentration is constant.

【0006】LEC法で化合物半導体単結晶を製造する
方法において、高圧引上げ炉に接続されたガス導入管の
途中に圧力調節弁を設け、排気管の途中にはバルブを設
けるとともに、上記排気管もしくは引上げ炉にはCOガ
ス検出器を取り付け、この検出器の信号に基づいて、上
記引上げ炉内のCO濃度が350ppm±10ppmの範囲で
一定となるように制御しながら結晶の引上げを行なっ
た。液体封止剤B23は水分濃度200ppmwと300pp
mwのものを用いた。
In the method for producing a compound semiconductor single crystal by the LEC method, a pressure control valve is provided in the middle of a gas introduction pipe connected to a high-pressure pulling furnace, and a valve is provided in the middle of the exhaust pipe. A CO gas detector was attached to the pulling furnace, and the crystal was pulled up while controlling the CO concentration in the pulling furnace to be constant within the range of 350 ppm ± 10 ppm based on the signal from the detector. Liquid sealant B 2 O 3 has a water concentration of 200 ppmw and 300 pp
The mw one was used.

【0007】その結果、GaAs単結晶中の炭素濃度は
図1に示すようになった。図1より、何れも結晶テール
側で高くなり均一性は悪かった。
As a result, the carbon concentration in the GaAs single crystal became as shown in FIG. As shown in FIG. 1, in all cases, the crystal tail was high and the uniformity was poor.

【0008】本発明者らは、CO濃度一定にも関わら
ず、炭素濃度が一定にならない原因はB23の水分濃度
の変化にあると考えた。
The present inventors have considered that the cause of the inconsistent carbon concentration despite the constant CO concentration is the change in the water concentration of B 2 O 3 .

【0009】LEC法において、液体封止剤B23中の
水分濃度が結晶の炭素濃度に影響を及ぼすことは従来か
ら判っており、チャージ時のB23水分濃度と結晶の炭
素濃度の関係については、A.T.Hunter(Apply Phys Let.
44(1),1984)の報告等がある。一般的に、低
水分濃度のB23を用いると、炭素濃度が高くなるた
め、従来は、水分濃度100ppmw以上のB23が使用さ
れてきた。
In the LEC method, it has been previously known that the water concentration in the liquid sealant B 2 O 3 affects the carbon concentration of the crystal, and the B 2 O 3 water concentration at the time of charging and the carbon concentration of the crystal. For the relationship between ATHunter (Apply Phys Let.
44 (1), 1984). Generally, when B 2 O 3 having a low water concentration is used, the carbon concentration becomes high. Therefore, conventionally, B 2 O 3 having a water concentration of 100 ppmw or more has been used.

【0010】しかし、結晶育成中のB23水分濃度の変
化に関しては調べられておらず、筆者らが育成終了後の
23水分濃度を調べた結果、図2に示すように、チャ
ージ時の水分濃度に比べ、大きく低下していることがわ
かり、このためにテール側で炭素濃度が高くなると考え
た。
However, the change in the B 2 O 3 water concentration during crystal growth has not been investigated, and the authors investigated the B 2 O 3 water concentration after the growth, and as a result, as shown in FIG. It was found that the water content was much lower than the water content at the time of charging, and we thought that the carbon content would be higher on the tail side because of this.

【0011】そこで、図2からわかるように、B23
分濃度は約100ppmw以下で安定するので、炭素濃度の
均一性を改善する手段として、最初から100ppmw以下
の低水分濃度のB23を使用することとした。このこと
によって、結晶育成中にB23の水分濃度は変化せず、
従って、結晶の炭素濃度を炉内ガス中のCO濃度だけで
制御できる。
As can be seen from FIG. 2, the B 2 O 3 water concentration is stable at about 100 ppmw or less. Therefore, as a means for improving the uniformity of the carbon concentration, B 2 O having a low water concentration of 100 ppmw or less from the beginning. I decided to use 3 . As a result, the water concentration of B 2 O 3 does not change during crystal growth,
Therefore, the carbon concentration of the crystal can be controlled only by the CO concentration in the furnace gas.

【0012】また、低水分濃度のB23を用いると炭素
濃度が高くなるという問題は、多結晶を溶融した後、一
定CO濃度の炉内雰囲気下に所定時間以上、具体的には
GaAsの場合10時間以上、好ましくは15時間以上
放置してから単結晶引き上げを行うことにより、炭素濃
度を高すぎない所定の値とすることができた。
Further, the problem that the carbon concentration becomes high when B 2 O 3 having a low water content is used is that after melting the polycrystal, it is kept in a furnace atmosphere having a constant CO concentration for a predetermined time or more, specifically, GaAs. In this case, the carbon concentration could be set to a predetermined value which was not too high by allowing the single crystal to be pulled after standing for 10 hours or longer, preferably 15 hours or longer.

【0013】すなわち、本発明は、LEC法により化合
物半導体単結晶を育成する方法において、水分量100
ppmw以下の低水分量のB23を使用し、化合物半導体多
結晶を溶融後の炉内雰囲気ガス中のCO濃度を一定の濃
度に制御して所定時間以上放置した後、炉内雰囲気ガス
中のCO濃度を同じく一定の濃度に制御しながら化合物
半導体単結晶を育成することを特徴とする化合物半導体
単結晶の製造方法を提供するものである。
That is, the present invention provides a method for growing a compound semiconductor single crystal by the LEC method, wherein the water content is 100%.
Using B 2 O 3 with a low water content of ppmw or less, controlling the CO concentration in the furnace atmosphere gas after melting the compound semiconductor polycrystal to a certain concentration and leaving it for a predetermined time or more, and then the furnace atmosphere gas A method for producing a compound semiconductor single crystal, which comprises growing a compound semiconductor single crystal while controlling the CO concentration therein to a constant concentration.

【0014】[0014]

【実施例】図4には本発明方法に使用した単結晶成長装
置の一例を示す。この実施例の結晶成長装置は、密閉型
の高圧引上げ炉1内にるつぼ2が支持軸3により回転可
能に支持され、るつぼ2の周囲にカーボン製ヒーター4
が配置されている。そして、ヒーター4の外側には同じ
くカーボン製の熱遮蔽体5が配置されているとともに、
るつぼ2の上方からは下端に種結晶を有する引上げ軸6
が垂下されている。さらに、引上げ炉1の側壁には、不
活性ガス等を導入するためのガス導入管11と、炉内ガ
スを排気するための排気管12が接続され、ガス導入管
11の途中には炉内圧力調整弁13が、また排気管12
の途中にはバルブ14が設けられている。
EXAMPLE FIG. 4 shows an example of a single crystal growth apparatus used in the method of the present invention. In the crystal growth apparatus of this embodiment, a crucible 2 is rotatably supported by a support shaft 3 in a closed high-pressure pulling furnace 1, and a carbon heater 4 is provided around the crucible 2.
Are arranged. A heat shield 5 also made of carbon is arranged outside the heater 4, and
A pulling shaft 6 having a seed crystal at the lower end from above the crucible 2
Is hanging. Further, a gas introduction pipe 11 for introducing an inert gas and the like and an exhaust pipe 12 for exhausting the gas in the furnace are connected to the side wall of the pulling furnace 1, and the inside of the furnace is provided in the middle of the gas introduction pipe 11. The pressure regulating valve 13 and the exhaust pipe 12
A valve 14 is provided midway.

【0015】また、排気管12にはCOガス濃度検出器
16が接続され、この検出器16の出力信号に基づいて
制御装置17が上記バルブ14を制御するように構成さ
れている。ガス導入管11の始端には、不活性ガスボン
ベ及びCOまたはCO2 または酸素ボンベが接続されて
おり、切り換え可能となっている。
A CO gas concentration detector 16 is connected to the exhaust pipe 12, and a control device 17 controls the valve 14 based on an output signal of the detector 16. An inert gas cylinder and a CO or CO 2 or oxygen cylinder are connected to the starting end of the gas introduction pipe 11 and are switchable.

【0016】まず、GaAsの原料として、7N(9
9.99999%)の高純度Gaと同じく7N(99.
99999%)の高純度Asとを直径6インチのpBN
製るつぼに入れ、その上に封止剤となるB23をのせ、
高圧引上げ炉内にセットした。B23は水分濃度50pp
mwのものを用いた。高圧引上げ炉内をArガスで置換し
てから、30kg/cm2の圧力を加え、約500℃に昇温
し、B23を溶融した後、600〜700℃まで昇温し
てGaAs多結晶を合成した。そのまま炉内を1400
℃までさらに昇温してGaAs多結晶を溶融させてか
ら、ガス導入管11の炉内圧力調整弁13の2次側圧力
を20kg/cm2に設定し、排気管12のバルブ14を開
いて高圧引上げ炉内の圧力を20kg/cm2まで徐々に減
圧するとともに、バルブ15を開いて検出器16により
COガス濃度を測定しながらCOガス濃度を一定に制御
し、20時間放置した後、COガス濃度を同じく一定に
制御したままるつぼ内の融液に種結晶をつけてGaAs
単結晶を引上げた。
First, 7N (9
7N (99.
99999%) high purity As and 6 inch diameter pBN
Put it in a crucible, put B 2 O 3 as a sealant on it,
It was set in the high-pressure pulling furnace. B 2 O 3 has a water concentration of 50 pp
The mw one was used. After the inside of the high-pressure pulling furnace was replaced with Ar gas, a pressure of 30 kg / cm 2 was applied, the temperature was raised to about 500 ° C., B 2 O 3 was melted, and the temperature was raised to 600-700 ° C. Crystals were synthesized. 1400 in the furnace as it is
After further raising the temperature to 0 ° C. to melt the GaAs polycrystal, set the secondary pressure of the furnace pressure control valve 13 of the gas introduction pipe 11 to 20 kg / cm 2 , and open the valve 14 of the exhaust pipe 12. The pressure inside the high-pressure pulling furnace is gradually reduced to 20 kg / cm 2 , the valve 15 is opened, the CO gas concentration is measured by the detector 16, and the CO gas concentration is controlled to a constant value. A seed crystal was added to the melt in the crucible while keeping the gas concentration constant and GaAs was added.
Single crystal pulled up.

【0017】CO濃度を各々100ppm,300ppm,6
00ppmの一定に制御した場合の結晶の炭素濃度を図3
に示す。図3に示すようにCO濃度に応じて任意の炭素
濃度でテ−ルまで一定の単結晶を得ることができた。な
お、炭素濃度はIR吸収法により分析したが、その換算
係数は9.2×1015cm-1を用いた。
CO concentrations of 100 ppm, 300 ppm, and 6 respectively
Fig. 3 shows the carbon concentration of the crystal when controlled to be constant at 00 ppm.
Shown in. As shown in FIG. 3, it was possible to obtain a constant single crystal up to the tail at an arbitrary carbon concentration depending on the CO concentration. The carbon concentration was analyzed by the IR absorption method, and the conversion factor was 9.2 × 10 15 cm −1 .

【0018】[0018]

【発明の効果】以上説明したように、LEC法により化
合物半導体単結晶を製造する方法において、100ppmw
以下の低水分濃度のB23を使用し、化合物半導体多結
晶を溶融後の炉内雰囲気ガス中のCO濃度を一定の濃度
に制御して所定時間以上放置した後、炉内雰囲気ガス中
のCO濃度を同じく一定の濃度に制御しながら化合物半
導体単結晶を育成することによって、B23の水分濃度
変化の影響がなく、ガス中のCO濃度のみにより結晶の
炭素濃度を制御することができた。
As described above, in the method for producing a compound semiconductor single crystal by the LEC method, 100 ppmw
The following low B 2 O 3 concentration was used to control the CO concentration in the furnace atmosphere gas after melting the compound semiconductor polycrystal to a constant concentration and leave it for a predetermined time or longer, and then in the furnace atmosphere gas By growing a compound semiconductor single crystal while controlling the CO concentration in the same manner to a constant concentration, the carbon concentration of the crystal is controlled only by the CO concentration in the gas without being affected by the change in the water concentration of B 2 O 3. I was able to.

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

【図1】従来法で育成したGaAs単結晶の成長軸方向
の炭素濃度のばらつき。
FIG. 1 shows variations in carbon concentration in the growth axis direction of a GaAs single crystal grown by a conventional method.

【図2】結晶育成中のB23水分濃度の変化。FIG. 2 shows changes in water concentration of B 2 O 3 during crystal growth.

【図3】本発明法で育成したGaAs単結晶の成長軸方
向の炭素濃度のばらつき。
FIG. 3 shows variations in carbon concentration in the growth axis direction of a GaAs single crystal grown by the method of the present invention.

【図4】本発明法を適用する単結晶引上げ装置。FIG. 4 is a single crystal pulling apparatus to which the method of the present invention is applied.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 大谷 聡一郎 埼玉県戸田市新曽南三丁目17番35号 日本 鉱業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Soichiro Otani 3-17-35, Niizonan, Toda City, Saitama Prefecture Japan Mining Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 LEC法により化合物半導体単結晶を育
成する方法において、水分量100ppmw以下の低水分量
のB23を使用し、化合物半導体多結晶を溶融後の炉内
雰囲気ガス中のCO濃度を一定の濃度に制御して所定時
間以上放置した後、炉内雰囲気ガス中のCO濃度を同じ
く一定の濃度に制御しながら化合物半導体単結晶を育成
することを特徴とする化合物半導体単結晶の製造方法。
1. A method for growing a compound semiconductor single crystal by the LEC method, wherein B 2 O 3 having a low water content of 100 ppmw or less is used, and CO in the atmosphere gas in the furnace after melting the compound semiconductor polycrystal is used. A compound semiconductor single crystal characterized by growing a compound semiconductor single crystal while controlling the CO concentration in a furnace atmosphere gas to a constant concentration after controlling the concentration to be a constant concentration for a predetermined time or more. Production method.
JP23113791A 1991-08-20 1991-08-20 Method for producing compound semiconductor single crystal Pending JPH0551296A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23113791A JPH0551296A (en) 1991-08-20 1991-08-20 Method for producing compound semiconductor single crystal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23113791A JPH0551296A (en) 1991-08-20 1991-08-20 Method for producing compound semiconductor single crystal

Publications (1)

Publication Number Publication Date
JPH0551296A true JPH0551296A (en) 1993-03-02

Family

ID=16918865

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23113791A Pending JPH0551296A (en) 1991-08-20 1991-08-20 Method for producing compound semiconductor single crystal

Country Status (1)

Country Link
JP (1) JPH0551296A (en)

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