JPH1129399A - Method and apparatus for producing GaAs single crystal - Google Patents

Method and apparatus for producing GaAs single crystal

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Publication number
JPH1129399A
JPH1129399A JP18116197A JP18116197A JPH1129399A JP H1129399 A JPH1129399 A JP H1129399A JP 18116197 A JP18116197 A JP 18116197A JP 18116197 A JP18116197 A JP 18116197A JP H1129399 A JPH1129399 A JP H1129399A
Authority
JP
Japan
Prior art keywords
gas
pressure vessel
single crystal
carbon monoxide
gaas single
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
JP18116197A
Other languages
Japanese (ja)
Inventor
Takashi Suzuki
隆 鈴木
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.)
Hitachi Cable Ltd
Original Assignee
Hitachi Cable 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 Hitachi Cable Ltd filed Critical Hitachi Cable Ltd
Priority to JP18116197A priority Critical patent/JPH1129399A/en
Publication of JPH1129399A publication Critical patent/JPH1129399A/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

(57)【要約】 【課題】COを含まないガスとCOを含むガスとをバル
ブの開閉により選択的に圧力容器内に導入する際に、バ
ルブを開いた時に生じるガスの高速突入に起因するヒー
タ発熱量の変動をなくし、GaAs単結晶中の炭素濃度
を成長方向で一定にする。 【解決手段】GaAs単結晶3を液体封止引上法によっ
て製造するに際し、圧力容器9内の雰囲気ガス中の一酸
化炭素濃度に応じて2つのガス導入系51、52に設け
たバルブ17、18を開閉制御し、第1のガスボンベ1
9からCOガスを含まないArガスを、第2のガスボン
ベ20からCOガスの混入したArガスを圧力容器9内
に選択的に導入する。このガスが導入される圧力容器9
のガス導入口9aに、多孔質のグラファイト製キャップ
25を嵌めて、ガスが圧力容器9内に導入される時、ガ
スを分散してその流速を低減し、高速突入を阻止する。
(57) Abstract: When selectively introducing a gas containing no CO and a gas containing CO into a pressure vessel by opening and closing a valve, the gas is caused by a high-speed rush of gas generated when the valve is opened. Variations in the calorific value of the heater are eliminated, and the carbon concentration in the GaAs single crystal is kept constant in the growth direction. When manufacturing a GaAs single crystal by a liquid sealing pulling method, valves provided in two gas introduction systems according to a concentration of carbon monoxide in an atmospheric gas in a pressure vessel are provided. 18 to control the opening and closing of the first gas cylinder 1
9, an Ar gas containing no CO gas is selectively introduced into the pressure vessel 9 from the second gas cylinder 20. Pressure vessel 9 into which this gas is introduced
When the gas is introduced into the pressure vessel 9, the gas is dispersed to reduce the flow velocity, thereby preventing high-speed intrusion.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、化合物半導体であ
るGaAs単結晶を液体封止引上げ法(以下LEC法と
略記する)により製造するGaAs単結晶の製造方法及
びその装置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 of manufacturing a GaAs single crystal, which is a compound semiconductor, by a liquid sealing and pulling method (hereinafter abbreviated as LEC method), and an apparatus therefor.

【0002】[0002]

【従来の技術】GaAs単結晶は、磁電変換素子、電界
効果トランジスタ(FET)、集積回路(IC)、大規
模集積回路(LSI)等の高速高周波素子の基板として
広い用途で使用されている。これらの素子に用いられる
基板材料の単結晶の製造方法の一つにLEC法がある。
2. Description of the Related Art GaAs single crystals are widely used as substrates for high-speed high-frequency devices such as magnetoelectric transducers, field-effect transistors (FETs), integrated circuits (ICs), and large-scale integrated circuits (LSIs). One of the methods for producing a single crystal of a substrate material used for these devices is the LEC method.

【0003】このLEC法によるGaAs単結晶の製造
では、不活性ガスとしてAr又はN2 ガスを用いて加圧
後に加熱して結晶成長を実施しているが、炭素がGaA
s結晶中に不純物として混入する。このGaAs結晶中
に混入した炭素は浅いアクセプタとなり、その濃度の高
低でGaAs単結晶の電気特性が大きく変化する。一
方、GaAsウェハに求められる電気特性は、GaAs
ウェハが基板として使われる素子の種類によって異な
る。このため、GaAs単結晶中に含まれる炭素濃度
は、結晶の先端から後端にかけて、希望する炭素濃度に
対してなるべくばらつきが少なく、均一であることが望
ましい。また、そのようなGaAs単結晶を再現性よく
成長する方法が必要とされている。
In the production of a GaAs single crystal by the LEC method, Ar or N 2 gas is used as an inert gas, and the crystal is grown by heating after pressurization.
It is mixed as an impurity into the s crystal. The carbon mixed into the GaAs crystal becomes a shallow acceptor, and the electrical characteristics of the GaAs single crystal greatly change depending on the concentration. On the other hand, the electrical characteristics required for a GaAs wafer are GaAs
The wafer varies depending on the type of device used as the substrate. For this reason, it is desirable that the concentration of carbon contained in the GaAs single crystal has as small a variation as possible with respect to a desired carbon concentration and is uniform from the front end to the rear end of the crystal. There is also a need for a method of growing such a GaAs single crystal with good reproducibility.

【0004】上記LEC法によるGaAs単結晶に混入
する炭素は、結晶成長中の雰囲気ガス中の一酸化炭素か
ら供給される。このため結晶成長中の炉内即ち圧力容器
34内の一酸化炭素濃度を所定の値に制御することで、
単結晶に含まれる炭素濃度を希望値にする方法が行われ
ている。
[0004] Carbon mixed into the GaAs single crystal by the LEC method is supplied from carbon monoxide in an atmosphere gas during the crystal growth. Therefore, by controlling the concentration of carbon monoxide in the furnace during crystal growth, that is, in the pressure vessel 34, to a predetermined value,
A method has been used in which the concentration of carbon contained in a single crystal is adjusted to a desired value.

【0005】図4に、上述したLEC法を用いた従来の
GaAs単結晶製造装置の構成を示す。圧力容器34内
にpBN(熱分解窒化ホウ素)製のルツボ31をルツボ
支持軸32により回転自在に支持して設置し、このルツ
ボ31に原料のGa及びAsを収容しその上に液体封止
剤として原料元素と反応性の低いB2 3 を被せ、外部
に設けられた排気装置(図示せず)により排気ガス用ガ
ス配管46及びバルブ47を通して圧力容器34内を排
気する。排気後、圧力容器34内部に、第1のガスボン
ベ(Arガスボンベ)44からバルブ42、または第2
のガスボンベ(COガス混入Arガスボンベ)45から
バルブ43、及びガス導入配管41を通して不活性ガス
であるArガス、またはCOガスの混じったArガスを
所定の圧力で導入する。
FIG. 4 shows a configuration of a conventional GaAs single crystal manufacturing apparatus using the above-described LEC method. A crucible 31 made of pBN (pyrolytic boron nitride) is rotatably supported by a crucible support shaft 32 in a pressure vessel 34, and the raw material Ga and As are contained in the crucible 31, and a liquid sealant is placed thereon. Then, the inside of the pressure vessel 34 is evacuated through an exhaust gas pipe 46 and a valve 47 by an exhaust device (not shown) provided outside, with B 2 O 3 having low reactivity with the raw material element. After the evacuation, a first gas cylinder (Ar gas cylinder) 44 and a valve 42 or a second
Ar gas as an inert gas or Ar gas mixed with CO gas is introduced at a predetermined pressure from a gas cylinder (Ar gas cylinder mixed with CO gas) 45 through a valve 43 and a gas introduction pipe 41.

【0006】この後、ルツボ31の外周部に位置するヒ
ータ33で加熱して、GaAs融液30を作る。このと
きGaAs融液30は液体封止剤29である溶融B2
3 により被覆される。この後、結晶引上げ軸26の下端
に設けた種結晶27をGaAs融液30の液面に接触さ
せ、徐々に種結晶27を引き上げ、所定の径に制御しな
がら引き上げて行くことにより、炭素濃度の制御された
GaAsの単結晶28を得る。なお、35〜40は断熱
材である。
[0006] Thereafter, the GaAs melt 30 is produced by heating with a heater 33 located on the outer periphery of the crucible 31. At this time, the GaAs melt 30 is melted B 2 O
Coated with 3 . Thereafter, the seed crystal 27 provided at the lower end of the crystal pulling shaft 26 is brought into contact with the liquid surface of the GaAs melt 30, and the seed crystal 27 is gradually pulled up and pulled up while controlling to a predetermined diameter. GaAs single crystal 28 is obtained. In addition, 35 to 40 are heat insulating materials.

【0007】一酸化炭素濃度COのコントロールは次の
ようにして行われる。圧力容器34内の雰囲気ガスをガ
ス配管48を通して炉外のCO濃度測定装置49に導
き、このCO濃度測定装置49により圧力容器34内の
COガス濃度をモニターし、所定の値よりも圧力容器3
4内のCOガス濃度が高い場合には、COガスを含まな
い不活性ガス(Arガス)を、第1のガスボンベ44よ
りバルブ42、ガス導入配管41を通して圧力容器34
内に導入し、かつ圧力容器34内のガスを排気ガス用ガ
ス配管46及びバルブ47を通して排出することによ
り、圧力容器34内のCOガス濃度を下げる。また圧力
容器34内のCOガス濃度が所定の値よりも低い場合に
は、第2のガスボンベ(COガス混入Arガスボンベ)
45からバルブ43及びガス導入配管41を通して、C
Oガスの混じった不活性ガス(COガス混入Arガス)
を圧力容器34内に導入し、かつ圧力容器34内のガス
を排気ガス用ガス配管46及びバルブ47を通して排出
することにより、圧力容器34内のCOガス濃度を上げ
る。
The control of the carbon monoxide concentration CO is performed as follows. The atmosphere gas in the pressure vessel 34 is led to a CO concentration measuring device 49 outside the furnace through a gas pipe 48, and the CO gas concentration in the pressure vessel 34 is monitored by the CO concentration measuring device 49.
In the case where the CO gas concentration in the gas container 4 is high, an inert gas (Ar gas) containing no CO gas is supplied from the first gas cylinder 44 through the valve 42 and the gas introduction pipe 41 to the pressure vessel 34.
The gas concentration in the pressure vessel 34 is reduced by introducing the gas into the pressure vessel 34 and discharging the gas in the pressure vessel 34 through the exhaust gas pipe 46 and the valve 47. When the CO gas concentration in the pressure vessel 34 is lower than a predetermined value, a second gas cylinder (an Ar gas cylinder containing CO gas) is used.
45 through a valve 43 and a gas introduction pipe 41,
Inert gas mixed with O gas (Ar gas mixed with CO gas)
Is introduced into the pressure vessel 34, and the gas in the pressure vessel 34 is discharged through the exhaust gas pipe 46 and the valve 47 to increase the CO gas concentration in the pressure vessel 34.

【0008】[0008]

【発明が解決しようとする課題】従来の製造方法に用い
られる単結晶引上げ装置では、圧力容器34内にガスを
導入する場合、ガスボンベ44,45からのガス導入配
管41の終端開口を圧力容器34内に直接に開放し連通
させる構成を採っており、圧力容器内の一酸化炭素濃度
に応じて、それまで閉じていたバルブ42または43を
瞬時に開放して、ガスボンベ44または45からの高圧
ガスを圧力容器34内に高速で突入させるようになって
いた。
In the single crystal pulling apparatus used in the conventional manufacturing method, when gas is introduced into the pressure vessel 34, the terminal opening of the gas introduction pipe 41 from the gas cylinders 44 and 45 is connected to the pressure vessel 34. The valve 42 or 43, which had been closed until then, is instantaneously opened according to the concentration of carbon monoxide in the pressure vessel, and the high-pressure gas from the gas cylinder 44 or 45 is opened. At high speed into the pressure vessel 34.

【0009】しかし、ガスが高速で圧力容器内に突入す
ると、圧力容器内の雰囲気が乱されて、ヒータ33の発
熱量が大きく変化し、GaAs融液30の温度が大きく
変動してしまうことがあった。
However, when the gas enters the pressure vessel at a high speed, the atmosphere in the pressure vessel is disturbed, the calorific value of the heater 33 greatly changes, and the temperature of the GaAs melt 30 greatly fluctuates. there were.

【0010】ヒータの発熱量の大きな変化が生じると、
GaAs単結晶の径の制御が乱れ、GaAs単結晶を再
現性よく成長することが難しくなる。また、GaAs融
液の温度が変動すると、雰囲気ガスから原料融液に混入
するCOガスの量が変化し、GaAs単結晶中の炭素濃
度を成長方向で一定にすることが困難となり、GaAs
ウェハの電気特性の不均一をもたらす。
When a large change in the calorific value of the heater occurs,
The control of the diameter of the GaAs single crystal is disturbed, and it becomes difficult to grow the GaAs single crystal with good reproducibility. Further, when the temperature of the GaAs melt fluctuates, the amount of CO gas mixed from the atmospheric gas into the raw material melt changes, making it difficult to keep the carbon concentration in the GaAs single crystal constant in the growth direction.
This leads to uneven electrical properties of the wafer.

【0011】なお、圧力容器内へのガスの高速突入をな
くすために、開閉バルブをオン/オフするのではなく、
流量制御弁の開度を変えてガスの導入量を制御すること
も考えられるが、即応性が悪くなるため、採用できな
い。
In order to prevent the gas from entering the pressure vessel at a high speed, the on-off valve is not turned on / off.
Although it is conceivable to control the gas introduction amount by changing the opening of the flow control valve, it cannot be adopted because the responsiveness is deteriorated.

【0012】そこで、本発明の目的は、上記課題を解決
し、ガス導入時におけるヒータ発熱量の大きな変動をな
くし、GaAs融液に大きな温度変動が生じないように
して、GaAs単結晶を再現性よく成長させ、GaAs
単結晶中の炭素濃度を成長方向で一定にすることが可能
なGaAs単結晶の製造方法及びその装置を提供するこ
とにある。
Therefore, an object of the present invention is to solve the above-mentioned problems, eliminate large fluctuations in the calorific value of the heater during gas introduction, and prevent large temperature fluctuations in the GaAs melt, thereby improving the reproducibility of the GaAs single crystal. Well grown, GaAs
An object of the present invention is to provide a method and an apparatus for manufacturing a GaAs single crystal capable of keeping the carbon concentration in the single crystal constant in the growth direction.

【0013】[0013]

【課題を解決するための手段】上記目的を達成するた
め、本発明はつぎのように構成されたものである。
Means for Solving the Problems In order to achieve the above object, the present invention is configured as follows.

【0014】本発明のGaAs単結晶の製造方法は、G
aAs単結晶を液体封止引上法によって製造するに際
し、圧力容器内の雰囲気ガス中の一酸化炭素濃度に応じ
て2つのガス導入系に設けたバルブを開閉制御し、2つ
のガス導入系から一酸化炭素ガスを含まない不活性ガス
と一酸化炭素ガスの混入した不活性ガスを圧力容器内に
選択的に導入することにより、GaAs単結晶に含まれ
る炭素濃度を制御するGaAs単結晶の製造方法におい
て、上記一酸化炭素ガスを含まない不活性ガス及び一酸
化炭素ガスの混入した不活性ガスを圧力容器内に導入す
る際に、ガスの流速を減速するようにしたものである。
The method for producing a GaAs single crystal of the present invention
In producing an aAs single crystal by the liquid sealing pulling method, the valves provided in the two gas introduction systems are controlled to open and close according to the concentration of carbon monoxide in the atmospheric gas in the pressure vessel, and the two gas introduction systems are used. Manufacture of a GaAs single crystal in which the concentration of carbon contained in a GaAs single crystal is controlled by selectively introducing an inert gas containing no carbon monoxide gas and an inert gas mixed with carbon monoxide gas into a pressure vessel. In the method, when the inert gas not containing the carbon monoxide gas and the inert gas mixed with the carbon monoxide gas are introduced into the pressure vessel, the flow rate of the gas is reduced.

【0015】また、本発明のGaAs単結晶の製造装置
は、不活性ガスで加圧した圧力容器内に、GaAs融液
と該融液の上面を覆う液体封止剤を収容しヒータにより
加熱されるルツボを設置し、GaAs単結晶の種結晶を
GaAs融液上面に接触させて回転させながら引き上げ
ることによりGaAs単結晶を製造する装置において、
圧力容器内の一酸化炭素濃度を測定する一酸化炭素濃度
測定手段と、一酸化炭素ガスを含まない不活性ガスと一
酸化炭素ガスの混入した不活性ガスとをそれぞれ導く2
つのガス導入系と、2つのガス導入系にそれぞれ設けら
れ、一酸化炭素ガスを含まない不活性ガスと一酸化炭素
ガスの混入した不活性ガスとを圧力容器内に選択的に導
入するために、一酸化炭素濃度測定手段の測定結果に応
じて開閉制御される開閉弁と、2つのガス導入系が接続
される圧力容器のガス導入口に設けられ、圧力容器内に
導入される一酸化炭素ガスを含まない不活性ガス及び一
酸化炭素ガスの混入した不活性ガスの流速を減速する減
速手段とを備えたものである。
Further, in the GaAs single crystal manufacturing apparatus of the present invention, a GaAs melt and a liquid sealant covering the upper surface of the melt are accommodated in a pressure vessel pressurized with an inert gas, and heated by a heater. An apparatus for manufacturing a GaAs single crystal by installing a crucible and bringing up a GaAs single crystal seed crystal while rotating the seed crystal while contacting the upper surface of the GaAs melt,
A carbon monoxide concentration measuring means for measuring the concentration of carbon monoxide in the pressure vessel; and introducing an inert gas containing no carbon monoxide gas and an inert gas containing carbon monoxide gas.
In order to selectively introduce into the pressure vessel an inert gas not containing carbon monoxide gas and an inert gas mixed with carbon monoxide gas, which are provided in two gas introduction systems and two gas introduction systems, respectively. An on-off valve that is controlled to open and close according to the measurement result of the carbon monoxide concentration measuring means, and a carbon monoxide gas that is provided at a gas inlet of a pressure vessel to which two gas introduction systems are connected and is introduced into the pressure vessel. A speed reducing means for reducing the flow rate of the inert gas containing no gas and the inert gas mixed with the carbon monoxide gas.

【0016】成長したGaAs単結晶中のAs格子点に
置換した炭素原子数で表す炭素濃度を、例えば1×10
15〜5×1016/cm3 の範囲に抑えると、比抵抗が10
17Ω−cm以上の半絶縁性が確保されることが分かってい
る。そこで、前提となる圧力容器内の雰囲気ガス中の一
酸化炭素濃度の制御は、成長したGaAs単結晶中の炭
素濃度が、この範囲中の希望値として得られるように制
御される。例えば、GaAs単結晶中の炭素濃度の希望
値として2×1015/cm3 を得たい場合、圧力容器内の
雰囲気ガス中の一酸化炭素濃度は、所定値の500ppm
になるように制御される。
The carbon concentration represented by the number of carbon atoms substituted for As lattice points in the grown GaAs single crystal is, for example, 1 × 10
When the resistivity is suppressed to the range of 15 to 5 × 10 16 / cm 3 , the specific resistance becomes 10
It is known that a semi-insulating property of 17 Ω-cm or more is secured. Therefore, the control of the concentration of carbon monoxide in the atmospheric gas in the pressure vessel is controlled such that the carbon concentration in the grown GaAs single crystal is obtained as a desired value in this range. For example, when it is desired to obtain 2 × 10 15 / cm 3 as a desired value of the carbon concentration in the GaAs single crystal, the concentration of carbon monoxide in the atmosphere gas in the pressure vessel is set to a predetermined value of 500 ppm.
Is controlled so that

【0017】上記のような炭素濃度の希望値に対し、L
EC法で成長したGaAs単結晶の先端から後端にかけ
て炭素濃度のばらつきの小さいGaAs単結晶を再現性
よく成長すべく、圧力容器内の雰囲気ガス中の一酸化炭
素濃度に応じて2つのガス導入系に設けたバルブを開閉
制御し、2つのガス導入系から一酸化炭素ガスを含まな
い不活性ガスと一酸化炭素ガスの混入した不活性ガスを
圧力容器内に選択的に導入する。
With respect to the desired value of the carbon concentration as described above, L
In order to reproducibly grow a GaAs single crystal having a small carbon concentration variation from the front end to the rear end of the GaAs single crystal grown by the EC method, two gases are introduced according to the concentration of carbon monoxide in the atmosphere gas in the pressure vessel. A valve provided in the system is controlled to open and close, and an inert gas containing no carbon monoxide gas and an inert gas mixed with carbon monoxide gas are selectively introduced into the pressure vessel from the two gas introduction systems.

【0018】この圧力容器内への不活性ガスの導入はバ
ルブの開閉制御、すなわちオン/オフ制御により行って
いるため、バルブを開いたとき、圧力容器内にガスが高
速で突入することになる。ガスが高速で圧力容器内に突
入すると、圧力容器内の雰囲気が乱されてヒータの発熱
量が大きく変化し、GaAs融液に大きな温度変動が生
じる。
Since the introduction of the inert gas into the pressure vessel is performed by opening and closing control of the valve, that is, on / off control, when the valve is opened, the gas enters the pressure vessel at a high speed. . When the gas enters the pressure vessel at a high speed, the atmosphere in the pressure vessel is disturbed, the calorific value of the heater changes greatly, and a large temperature fluctuation occurs in the GaAs melt.

【0019】本発明は、このようなヒータ発熱量の変化
やGaAs融液の温度変動をなくすために、圧力容器内
に導入するガスの流速を低減して、圧力容器内の雰囲気
が乱されるのを抑制するものである。
The present invention reduces the flow rate of the gas introduced into the pressure vessel and disturbs the atmosphere in the pressure vessel in order to eliminate such a change in the calorific value of the heater and the fluctuation in the temperature of the GaAs melt. It is to suppress.

【0020】このガスの流速を低減する減速手段は、例
えば、圧力容器内のガス導入口にグラファイトのような
多孔質の物質から成るキャップを嵌めて、その多孔質物
質の細孔を通し分散させる構成とすることで達成でき
る。
The deceleration means for reducing the gas flow velocity is, for example, fitting a cap made of a porous substance such as graphite into a gas inlet in a pressure vessel and dispersing the gas through the pores of the porous substance. This can be achieved by adopting a configuration.

【0021】このようにグラファイト製キャップ等の減
速手段を通すことにより圧力容器内に導入するガスの流
速をガス導入口にて低減すると、ガスの突入が緩和され
るので、圧力容器内の雰囲気が乱されるのが抑制され、
ヒータの発熱量が大きく変化する現象がなくなり、Ga
As融液に大きな温度変動が生じなくなる。従って、G
aAs単結晶を再現性よく成長させ、GaAs単結晶中
の炭素濃度を希望する値にて成長方向で一定にすること
ができる。
When the flow rate of the gas introduced into the pressure vessel is reduced at the gas introduction port by passing through a speed reducing means such as a graphite cap as described above, gas intrusion is reduced, and the atmosphere in the pressure vessel is reduced. It is suppressed from being disturbed,
The phenomenon that the heating value of the heater greatly changes is eliminated, and Ga
No large temperature fluctuation occurs in the As melt. Therefore, G
An aAs single crystal can be grown with good reproducibility, and the carbon concentration in the GaAs single crystal can be kept constant at a desired value in the growth direction.

【0022】[0022]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0023】本発明を実施するために用いた結晶成長炉
たる単結晶引上げ装置の構成を図1に示す。
FIG. 1 shows a structure of a single crystal pulling apparatus as a crystal growth furnace used for carrying out the present invention.

【0024】図1に示すように、圧力容器9内にpBN
製のルツボ6がルツボ支持軸7により回転自在に支持さ
れて設置され、ルツボ6の外周囲にはヒータ8が配置さ
れ、その更に外周囲には断熱材10〜12が配置され、
圧力容器9の底部との間にも断熱材13〜15が配置さ
れている。
As shown in FIG. 1, pBN is
The crucible 6 is rotatably supported and installed by a crucible support shaft 7, a heater 8 is arranged around the crucible 6, and further, heat insulating materials 10 to 12 are arranged around the outside.
Insulating materials 13 to 15 are also arranged between the pressure vessel 9 and the bottom.

【0025】圧力容器9の内部は、排気ガス用ガス配管
21及びバルブ22を通して外部に設けられた排気装置
(図示せず)に接続される。また、ガス導入配管16及
びバルブ17を通してArガスボンベである第1のガス
ボンベ19に接続されていると共に、ガス導入配管16
及びバルブ18を通してCOガス混入Arガスボンベで
ある第2のガスボンベ20に接続されている。この第2
のガスボンベ20には、アルゴンガスにCOガスを5%
混入した混合ガスが入っている。そして、圧力容器9の
内部は、ガス配管23を通して炉外のCO濃度測定装置
24に接続されている。
The interior of the pressure vessel 9 is connected to an exhaust device (not shown) provided outside through an exhaust gas pipe 21 and a valve 22. Further, it is connected to a first gas cylinder 19 which is an Ar gas cylinder through a gas introduction pipe 16 and a valve 17, and is connected to a gas introduction pipe 16.
And a valve 18 connected to a second gas cylinder 20 which is an Ar gas cylinder containing CO gas. This second
5% CO gas in argon gas
Contains mixed gas. The inside of the pressure vessel 9 is connected to a CO concentration measuring device 24 outside the furnace through a gas pipe 23.

【0026】上記ガス導入配管16から第1のガスボン
ベ19に至る配管が第1のガス導入系51を構成し、上
記ガス導入配管16から第2のガスボンベ20に至る配
管が第2のガス導入系52を構成する。
A pipe from the gas introduction pipe 16 to the first gas cylinder 19 constitutes a first gas introduction system 51, and a pipe from the gas introduction pipe 16 to the second gas cylinder 20 is a second gas introduction system. 52.

【0027】ここで、ガスボンベ19,20からのガス
導入配管16の終端開口を圧力容器9内に直接に開放し
連通させる従来の構成では、ガスボンベ19,20から
のArガス又は混合ガスが圧力容器9内に直接に導入さ
れ、そのガスの導入に起因してガスの導入時にヒータ8
の発熱量が大きく変化し、GaAs融液5の温度が大き
く変動する現象が生じる。
Here, in the conventional configuration in which the terminal opening of the gas introduction pipe 16 from the gas cylinders 19 and 20 is directly opened and communicated with the pressure vessel 9, Ar gas or mixed gas from the gas cylinders 19 and 20 is supplied to the pressure vessel. 9 is introduced directly into the heater 8 when the gas is introduced due to the introduction of the gas.
Of the GaAs melt 5 greatly fluctuates and the temperature of the GaAs melt 5 fluctuates greatly.

【0028】かかる不都合を回避するため、図1の単結
晶引上げ装置では、図示するように、ガス導入配管16
と圧力容器9の接続部のガスが導入してくる入口、つま
り圧力容器9内のガス導入口9aに、グラファイト製の
キャップ25を取り付けてある。この実施形態の場合、
ガス導入口9aは圧力容器9の外周部の下部に設けられ
ており、グラファイト製のキャップ25は、このガス導
入口9aを圧力容器9の内側から被う形で、圧力容器9
の内側面と断熱材13との間に設けられている。グラフ
ァイトは多孔質の物質であり、通気性がある。グラファ
イト製キャップ25をガス導入の入口に取り付けること
で、圧力容器9内に導入するガスの流速は、低減され
る。
In order to avoid such inconvenience, the single crystal pulling apparatus shown in FIG.
A graphite cap 25 is attached to an inlet through which a gas is introduced at a connection portion between the pressure vessel 9 and the gas introduction port 9 a in the pressure vessel 9. In this embodiment,
The gas inlet 9a is provided at the lower part of the outer peripheral portion of the pressure vessel 9. A cap 25 made of graphite covers the gas inlet 9a from the inside of the pressure vessel 9 so as to cover the pressure vessel 9.
Is provided between the inner side surface of the heat sink and the heat insulating material 13. Graphite is a porous substance and has air permeability. By attaching the graphite cap 25 to the gas introduction inlet, the flow rate of the gas introduced into the pressure vessel 9 is reduced.

【0029】(実施例)上記構成の単結晶引上げ装置を
用い、次のようにして、GaAs単結晶を10本成長し
た。
(Example) Ten GaAs single crystals were grown in the following manner using the single crystal pulling apparatus having the above structure.

【0030】ルツボ6に原料のGa及びAsを収容しそ
の上に液体封止剤として原料元素と反応性の低いB2
3 を被せ、外部に設けられた排気装置により排気ガス用
ガス配管21及びバルブ22を通して圧力容器9内を排
気した後、圧力容器9内部に、第1のガスボンベ19か
らバルブ17及びガス導入配管16を通して不活性ガス
であるArガスを所定の圧力20kg/cm2 で導入する。
この後、ルツボ6の外周部に位置するヒータ8で加熱し
て、GaAs融液5を作る。このときGaAs融液5は
液体封止剤4である溶融B2 3 により被覆される。
The raw material Ga and As are accommodated in the crucible 6 and B 2 O having low reactivity with the raw material element is formed thereon as a liquid sealant.
3 covered with, after evacuating the pressure vessel 9 via the exhaust gas gas pipe 21 and the valve 22 by the exhaust apparatus provided outside, inside the pressure vessel 9, the first from the gas cylinder 19 valve 17 and the gas introduction pipe 16 Ar gas, which is an inert gas, is introduced at a predetermined pressure of 20 kg / cm 2 .
Thereafter, the GaAs melt 5 is produced by heating with a heater 8 located at the outer peripheral portion of the crucible 6. At this time, the GaAs melt 5 is covered with molten B 2 O 3 as the liquid sealant 4.

【0031】このように20kg/cm2 の圧力下で、ルツ
ボ6にAsが過剰組成となるようなGaAs融液5を2
0kg作成した後、バルブ17、18の開閉により、結晶
が引き上げられる空間のCOガス濃度が所定の値の50
0ppm になるようにした。即ち、圧力容器9内の雰囲気
ガスをガス配管23を通して炉外のCO濃度測定装置2
4に導き、このCO濃度測定装置24により圧力容器9
内のCOガス濃度をモニターし、所定の値の500ppm
よりも圧力容器9内のCOガス濃度が高い場合には、C
Oガスを含まない不活性ガス(Arガス)を、第1のガ
スボンベ19よりバルブ17、ガス導入配管16を通し
て圧力容器9内に導入し、かつ圧力容器9内のガスを排
気ガス用ガス配管21及びバルブ22を通して排出する
ことにより、圧力容器9内のCOガス濃度を下げた。
As described above, under a pressure of 20 kg / cm 2 , the crucible 6 is filled with the GaAs melt 5 having an excess composition of As.
After producing 0 kg, the CO gas concentration in the space where the crystal is pulled up is set to a predetermined value of 50 by opening and closing the valves 17 and 18.
It was adjusted to 0 ppm. That is, the atmospheric gas in the pressure vessel 9 is passed through the gas pipe 23 and the CO concentration
4 and the pressure vessel 9 is measured by the CO concentration measuring device 24.
Monitor the concentration of CO gas in
If the CO gas concentration in the pressure vessel 9 is higher than
An inert gas (Ar gas) containing no O gas is introduced from the first gas cylinder 19 into the pressure vessel 9 through the valve 17 and the gas introduction pipe 16, and the gas in the pressure vessel 9 is discharged into the exhaust gas pipe 21. And, by discharging through the valve 22, the CO gas concentration in the pressure vessel 9 was reduced.

【0032】また、圧力容器9内のCOガス濃度が所定
の値の500ppm よりも低い場合には、第2のガスボン
ベ20からバルブ18及びガス導入配管16を通して、
COガスの混じった不活性ガス(COガスを5%混入し
たArガス)を圧力容器9内に導入し、かつ圧力容器9
内のガスを排気ガス用ガス配管21及びバルブ22を通
して排出することにより、圧力容器9内のCOガス濃度
を上げた。
When the CO gas concentration in the pressure vessel 9 is lower than a predetermined value of 500 ppm, the second gas cylinder 20 passes through the valve 18 and the gas introduction pipe 16
An inert gas mixed with CO gas (Ar gas mixed with 5% of CO gas) is introduced into the pressure vessel 9 and the pressure vessel 9
The CO gas concentration in the pressure vessel 9 was increased by discharging the gas inside through the exhaust gas pipe 21 and the valve 22.

【0033】上記のように圧力容器9内のCOガス濃度
を制御しつつ、結晶引上げ軸1の下端に設けた種結晶2
をGaAs融液5に液面に接触させ、徐々に種結晶2を
引き上げ、所定の径に制御しながら引き上げて行くこと
によりGaAsの単結晶3を得た。
While controlling the CO gas concentration in the pressure vessel 9 as described above, the seed crystal 2 provided at the lower end of the crystal pulling shaft 1 is controlled.
Was brought into contact with the GaAs melt 5 and the seed crystal 2 was gradually pulled up and pulled up while controlling to a predetermined diameter to obtain a GaAs single crystal 3.

【0034】その際、GaAs単結晶が引き上げられる
空間及びヒータ8が設置される加熱空間の圧力をぞれぞ
れ20kg/cm2 にし、GaAs結晶中の炭素濃度を希望
値の2.0×1015/cm3 とすることを狙い、種結晶2
をGaAs融液5につけて、直径110mm、長さ350
mmのGaAs単結晶3を成長した。このようにしてGa
As単結晶3を10本引き上げた。
At this time, the pressure in the space in which the GaAs single crystal is pulled up and the pressure in the heating space in which the heater 8 is installed are set to 20 kg / cm 2 , respectively, and the carbon concentration in the GaAs crystal is set to a desired value of 2.0 × 10 2. Seed crystal 2 aiming at 15 / cm 3
Was applied to the GaAs melt 5 and the diameter was 110 mm and the length was 350
A GaAs single crystal 3 of mm was grown. Thus, Ga
Ten As single crystals 3 were pulled up.

【0035】表1に、この実施例1の方法により引き上
げた計10本のGaAs単結晶の成長結果を示す。実施
例1の方法による場合、全て単結晶の成長となり、多結
晶の発生は認められなかった。
Table 1 shows the results of the growth of a total of ten GaAs single crystals pulled up by the method of Example 1. In the case of the method of Example 1, single crystals were all grown, and generation of polycrystals was not observed.

【0036】[0036]

【表1】 [Table 1]

【0037】(比較例)図4に示す従来の減速手段を設
けていない単結晶引上げ装置を用いてGaAs単結晶を
成長した。
Comparative Example A GaAs single crystal was grown using a conventional single crystal pulling apparatus shown in FIG.

【0038】第2のガスボンベ45には、ArガスにC
Oガスが5%混入したガスが入っている。20kg/cm2
の圧力下で、pBN製のルツボ31にAsが過剰組成と
なるようなGaAs融液30を20kg作成した後、バル
ブ42、43の開閉により、圧力容器34内に、第1の
ガスボンベ44からの単体のArガスと、第2のガスボ
ンベ45からの一酸化炭素ガスを含んだArガスを選択
的に導入して、圧力容器34内の一酸化炭素ガス濃度が
所定値の500ppm になるようにした。
In the second gas cylinder 45, C is added to Ar gas.
A gas containing 5% of O gas is contained. 20kg / cm 2
After preparing 20 kg of the GaAs melt 30 such that the As composition becomes excessive in the crucible 31 made of pBN under the above pressure, the valves 42 and 43 are opened and closed, and the first gas cylinder 44 from the first gas cylinder 44 is placed in the pressure vessel 34. A single Ar gas and an Ar gas containing a carbon monoxide gas from the second gas cylinder 45 are selectively introduced so that the concentration of the carbon monoxide gas in the pressure vessel 34 becomes a predetermined value of 500 ppm. .

【0039】この後、実施例1と同様に、GaAs単結
晶の引き上げられる空間及びヒータ33が設置される加
熱空間の圧力をそれぞれ20kg/cm2 にし、GaAs単
結晶の炭素濃度を希望値の2.0×1015/cm3 とする
ことを狙い、種結晶27をGaAs融液30につけて、
直径110mm、長さ350mmのGaAs単結晶28を成
長した。このようにしてGaAs単結晶28を10本引
き上げた。
Thereafter, as in the first embodiment, the pressure in the space in which the GaAs single crystal is pulled up and the pressure in the heating space in which the heater 33 is installed are each set to 20 kg / cm 2 , and the carbon concentration of the GaAs single crystal is set to the desired value of 2 kg / cm 2. Aiming at 0.010 15 / cm 3 , the seed crystal 27 was applied to the GaAs melt 30,
A GaAs single crystal 28 having a diameter of 110 mm and a length of 350 mm was grown. Thus, ten GaAs single crystals 28 were pulled up.

【0040】表2に、上記比較例の方法により引き上げ
た計10本の単結晶の成長結果を示す。
Table 2 shows the results of the growth of a total of 10 single crystals pulled up by the method of the comparative example.

【0041】[0041]

【表2】 [Table 2]

【0042】(実施例と比較例との比較)比較例の製造
方法によった場合、表2に示す如く、10本中の5本だ
けが単結晶で、他の5本は多結晶となった。その多結晶
の発生位置は一定しておらず、結晶の形状に乱れが認め
られた。
(Comparison between Example and Comparative Example) According to the manufacturing method of the comparative example, as shown in Table 2, only 5 out of 10 lines are single crystals and the other 5 lines are polycrystals. Was. The position where the polycrystal was generated was not constant, and the shape of the crystal was disturbed.

【0043】これに対し上記実施例の製造方法の場合、
成長した計10本の結晶は、既に上記表1の所で触れた
如く10本とも全て単結晶であった。よって、実施例の
製造方法は、この比較例の製造方法に比べ、結晶形状に
乱れのない単結晶を安定して成長できる優れたGaAs
単結晶の製造方法であることがわかる。
On the other hand, in the case of the manufacturing method of the above embodiment,
As already mentioned in Table 1 above, all the ten grown crystals were all single crystals. Therefore, the manufacturing method of the example is superior to the manufacturing method of the comparative example in that it is an excellent GaAs that can stably grow a single crystal having no disorder in crystal shape.
It can be seen that this is a method for producing a single crystal.

【0044】次に、成長したGaAs単結晶中の炭素濃
度分布を測定するため、上記実施例の製造方法及び上記
比較例の製造方法によって成長したGaAs単結晶から
無作為に結晶を1本づつ選び、それぞれの結晶の先端
(シード)から後端(テール)までの20mmおきの各位
置から5mmの厚さの試料を採取し、各試料の両面を研磨
して鏡面にした。この後、赤外線吸収法により、それぞ
れの試料のGaAs単結晶中の炭素濃度を測定し、Ga
As単結晶中の炭素濃度の分布を調べた。
Next, in order to measure the carbon concentration distribution in the grown GaAs single crystal, crystals were randomly selected one by one from the GaAs single crystals grown by the manufacturing method of the above embodiment and the comparative example. A sample having a thickness of 5 mm was taken from each position of every 20 mm from the front end (seed) to the rear end (tail) of each crystal, and both surfaces of each sample were polished to a mirror surface. Thereafter, the carbon concentration in the GaAs single crystal of each sample was measured by an infrared absorption method.
The distribution of the carbon concentration in the As single crystal was examined.

【0045】その結果を図2及び図3に示す。比較例の
方法により成長したGaAs単結晶(図3)では、ガス
が突入するたびに、その影響が炭素濃度の大きな変動と
して現れているに比べて、実施例の方法により成長した
GaAs単結晶(図2)の場合は、ガスの突入が緩和さ
れているため、GaAs単結晶中の炭素濃度の希望値
(2×1015/cm3 )からのずれが小さい。
The results are shown in FIG. 2 and FIG. In the GaAs single crystal grown by the method of the comparative example (FIG. 3), each time gas enters, the effect appears as a large change in the carbon concentration, whereas the GaAs single crystal grown by the method of the example ( In the case of FIG. 2), since the gas intrusion is reduced, the deviation of the carbon concentration in the GaAs single crystal from the desired value (2 × 10 15 / cm 3 ) is small.

【0046】[0046]

【発明の効果】本発明方法によれば、バルブの開放によ
り圧力容器内に導入されるガスの流速を減速して圧力容
器内の雰囲気を乱さないようにしたので、ヒータ発熱量
の変動を抑えることができ、GaAs融液に大きな温度
変動が生じなくなる。したがって、導入時のガス流速を
減速していない従来の方法に比べて、結晶形状に乱れの
ない単結晶を安定して、かつ所望する炭素濃度に対して
ばらつきの少ない炭素濃度の結晶を安定して製造でき
る。その結果、電気特性のより均一なGaAs単結晶を
より安価に生産することができ、これらを基板として使
用する素子の製造コストを下げることができる。
According to the method of the present invention, the flow rate of the gas introduced into the pressure vessel is reduced by opening the valve so that the atmosphere in the pressure vessel is not disturbed. Therefore, a large temperature fluctuation does not occur in the GaAs melt. Therefore, compared to the conventional method in which the gas flow rate at the time of introduction is not reduced, a single crystal having no disorder in the crystal shape is stabilized, and a crystal having a small carbon concentration with respect to a desired carbon concentration is stabilized. Can be manufactured. As a result, GaAs single crystals having more uniform electric characteristics can be produced at lower cost, and the manufacturing cost of an element using these as a substrate can be reduced.

【0047】本発明装置によれば、圧力容器のガス導入
口にガスの流速を減速する減速手段を設けるという構造
によって、上記効果を適切に得ることができる。
According to the apparatus of the present invention, the above-mentioned effect can be appropriately obtained by the structure in which the gas introduction port of the pressure vessel is provided with the speed reducing means for reducing the gas flow rate.

【0048】特に減速手段を多孔質の物質からなるキャ
ップで構成した場合には、多孔質キャップを圧力容器の
ガス導入口に嵌めるという簡単な構成で実現できる。
In particular, when the speed-reducing means is constituted by a cap made of a porous substance, it can be realized by a simple structure in which the porous cap is fitted to the gas inlet of the pressure vessel.

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

【図1】実施形態の製造方法で用いた単結晶引上げ装置
の構成を示す図である。
FIG. 1 is a diagram showing a configuration of a single crystal pulling apparatus used in a manufacturing method of an embodiment.

【図2】炭素濃度2.0×1015/cm3 の結晶を得るべ
く、実施形態の製造方法により成長したGaAs単結晶
の成長方向の炭素濃度分布を示した図である。
FIG. 2 is a view showing a carbon concentration distribution in a growth direction of a GaAs single crystal grown by a manufacturing method of an embodiment to obtain a crystal having a carbon concentration of 2.0 × 10 15 / cm 3 .

【図3】炭素濃度2.0×1015/cm3 の結晶を得るべ
く、従来の製造方法によって成長したGaAs単結晶の
成長方向の炭素濃度分布を示した図である。
FIG. 3 is a diagram showing a carbon concentration distribution in a growth direction of a GaAs single crystal grown by a conventional manufacturing method to obtain a crystal having a carbon concentration of 2.0 × 10 15 / cm 3 .

【図4】比較例の製造方法で用いた単結晶引上げ装置の
構成を示す図である。
FIG. 4 is a diagram showing a configuration of a single crystal pulling apparatus used in a manufacturing method of a comparative example.

【符号の説明】[Explanation of symbols]

1 結晶引上げ軸 2 種結晶 3 GaAs単結晶 4 液体封止剤 5 GaAs融液 6 pBN製のルツボ 8 ヒータ 9 圧力容器 9a ガス導入口 16 ガス導入配管 17,18 バルブ 19 第1のガスボンベ(Arガスボンベ) 20 第2のガスボンベ(COガス混入Arガスボン
ベ) 24 CO濃度測定装置
Reference Signs List 1 crystal pulling shaft 2 seed crystal 3 GaAs single crystal 4 liquid sealant 5 GaAs melt 6 crucible made of pBN 8 heater 9 pressure vessel 9a gas inlet 16 gas introduction pipe 17, 18 valve 19 first gas cylinder (Ar gas cylinder) ) 20 second gas cylinder (Ar gas cylinder mixed with CO gas) 24 CO concentration measuring device

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】GaAs単結晶を液体封止引上法によって
製造するに際し、圧力容器内の雰囲気ガス中の一酸化炭
素濃度に応じて2つのガス導入系に設けたバルブを開閉
制御し、2つのガス導入系から一酸化炭素ガスを含まな
い不活性ガスと一酸化炭素ガスの混入した不活性ガスを
圧力容器内に選択的に導入することにより、GaAs単
結晶に含まれる炭素濃度を制御するGaAs単結晶の製
造方法において、上記一酸化炭素ガスを含まない不活性
ガス及び一酸化炭素ガスの混入した不活性ガスを圧力容
器内に導入する際に、ガスの流速を減速するようにした
ことを特徴とするGaAs単結晶の製造方法。
In producing a GaAs single crystal by a liquid sealing pulling method, valves provided in two gas introduction systems are controlled to open and close according to the concentration of carbon monoxide in an atmospheric gas in a pressure vessel. By selectively introducing an inert gas containing no carbon monoxide gas and an inert gas containing carbon monoxide gas into the pressure vessel from two gas introduction systems, the carbon concentration contained in the GaAs single crystal is controlled. In the method for producing a GaAs single crystal, when introducing the inert gas containing no carbon monoxide gas and the inert gas mixed with carbon monoxide gas into the pressure vessel, the flow rate of the gas is reduced. A method for producing a GaAs single crystal, comprising:
【請求項2】不活性ガスで加圧した圧力容器内に、Ga
As融液と該融液の上面を覆う液体封止剤を収容しヒー
タにより加熱されるルツボを設置し、GaAs単結晶の
種結晶をGaAs融液上面に接触させて回転させながら
引き上げることによりGaAs単結晶を製造する装置に
おいて、圧力容器内の一酸化炭素濃度を測定する一酸化
炭素濃度測定手段と、一酸化炭素ガスを含まない不活性
ガスと一酸化炭素ガスの混入した不活性ガスとをそれぞ
れ導く2つのガス導入系と、2つのガス導入系にそれぞ
れ設けられ、一酸化炭素ガスを含まない不活性ガスと一
酸化炭素ガスの混入した不活性ガスとを圧力容器内に選
択的に導入するために、一酸化炭素濃度測定手段の測定
結果に応じて開閉制御される開閉弁と、2つのガス導入
系が接続される圧力容器のガス導入口に設けられ、圧力
容器内に導入される一酸化炭素ガスを含まない不活性ガ
ス及び一酸化炭素ガスの混入した不活性ガスの流速を減
速する減速手段とを備えたGaAs単結晶の製造装置。
2. A pressure vessel pressurized with an inert gas contains Ga.
A crucible containing the As melt and a liquid sealant covering the upper surface of the melt is placed by heating with a heater, and the GaAs single crystal is brought into contact with the upper surface of the GaAs melt and pulled up while rotating. In an apparatus for producing a single crystal, a carbon monoxide concentration measuring means for measuring a carbon monoxide concentration in a pressure vessel, and an inert gas containing no carbon monoxide gas and an inert gas mixed with carbon monoxide gas are used. Two gas introduction systems for guiding each gas, and an inert gas containing no carbon monoxide gas and an inert gas mixed with carbon monoxide gas, which are provided in each of the two gas introduction systems, are selectively introduced into the pressure vessel. In order to achieve this, an opening / closing valve that is controlled to open and close according to the measurement result of the carbon monoxide concentration measuring means, and a gas introduction port of a pressure vessel to which two gas introduction systems are connected, are introduced into the pressure vessel. Apparatus for producing a GaAs single crystal and a decelerating means for decelerating the flow rate of the entrained inert gas of the inert gas and carbon monoxide gas containing no carbon monoxide gas.
【請求項3】上記減速手段が、圧力容器のガス導入口に
嵌められた多孔質の物質からなるキャップで構成されて
いる請求項2に記載のGaAs単結晶の製造装置。
3. The apparatus for producing a GaAs single crystal according to claim 2, wherein said deceleration means is constituted by a cap made of a porous substance fitted to a gas inlet of a pressure vessel.
JP18116197A 1997-07-07 1997-07-07 Method and apparatus for producing GaAs single crystal Pending JPH1129399A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18116197A JPH1129399A (en) 1997-07-07 1997-07-07 Method and apparatus for producing GaAs single crystal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18116197A JPH1129399A (en) 1997-07-07 1997-07-07 Method and apparatus for producing GaAs single crystal

Publications (1)

Publication Number Publication Date
JPH1129399A true JPH1129399A (en) 1999-02-02

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP18116197A Pending JPH1129399A (en) 1997-07-07 1997-07-07 Method and apparatus for producing GaAs single crystal

Country Status (1)

Country Link
JP (1) JPH1129399A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008056562A (en) * 2007-09-14 2008-03-13 Dowa Holdings Co Ltd GaAs SINGLE CRYSTAL, AND METHOD AND APPARATUS FOR PRODUCING THE SAME
WO2020129330A1 (en) * 2018-12-19 2020-06-25 株式会社Sumco Method for manufacturing single crystal silicon ingot and silicon single crystal pulling device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008056562A (en) * 2007-09-14 2008-03-13 Dowa Holdings Co Ltd GaAs SINGLE CRYSTAL, AND METHOD AND APPARATUS FOR PRODUCING THE SAME
WO2020129330A1 (en) * 2018-12-19 2020-06-25 株式会社Sumco Method for manufacturing single crystal silicon ingot and silicon single crystal pulling device
JP2020100516A (en) * 2018-12-19 2020-07-02 株式会社Sumco Method for producing single crystal silicon ingot and silicon single crystal pulling apparatus
CN113302346A (en) * 2018-12-19 2021-08-24 胜高股份有限公司 Method for manufacturing silicon single crystal ingot and silicon single crystal pulling apparatus
CN113302346B (en) * 2018-12-19 2023-11-03 胜高股份有限公司 Manufacturing method of single crystal silicon ingot and single crystal silicon pulling device

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