JPS6335600B2 - - Google Patents
Info
- Publication number
- JPS6335600B2 JPS6335600B2 JP58157625A JP15762583A JPS6335600B2 JP S6335600 B2 JPS6335600 B2 JP S6335600B2 JP 58157625 A JP58157625 A JP 58157625A JP 15762583 A JP15762583 A JP 15762583A JP S6335600 B2 JPS6335600 B2 JP S6335600B2
- Authority
- JP
- Japan
- Prior art keywords
- volatile component
- compound semiconductor
- melt
- vapor
- crucible
- 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
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C30—CRYSTAL GROWTH
- C30B—SINGLE-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
- C30B15/00—Single-crystal growth by pulling from a melt, e.g. Czochralski method
- C30B15/02—Single-crystal growth by pulling from a melt, e.g. Czochralski method adding crystallising materials or reactants forming it in situ to the melt
Landscapes
- 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
[発明の背景と目的]
本発明は化合物半導体の製造方法に係り、特に
不揮発性成分融液に揮発性成分蒸気を接触させて
合成した融液から化合物半導体の単結晶を引き上
げ成長させる製造方法に関するものである。
[従来の技術]
従来、リン化ガリウム(GaP)、リン化インジ
ウム(InP)、砒化ガリウム(GaAs)等の−
族化合物半導体の不揮発性成分と揮発性成分とを
含む化合物半導体の製造方法としては、別途製造
したこれらの多結晶をルツボ内で溶融して、この
融液から単結晶を引き上げることにより製造する
チヨクラルスキー法が主流となつている。
この多結晶を用いる引き上げ法とは異なり、不
揮発性成分融液に揮発性成分の蒸気を反応させて
目的の化合物の融液を生成し、この融液から直接
単結晶を引き上げる方法が提案されている。
例えば、不活性液体で覆つた不揮発性成分融液
を収納したルツボの下に揮発性成分を収納した低
温室容器を設け、ルツボと低温室容器の間に窒化
ボロン(BN)のような多孔質の材質または細孔
を持つ材質からなる隔壁を設け、低温室容器を加
熱して蒸気圧を制御しながら揮発性成分蒸気を隔
壁を通して不揮発性成分融液に供給して反応さ
せ、得られた融液から単結晶を引き上げることが
提案されている(特公昭52−12152号)。
しかし、たとえ高圧不活性ガス雰囲気下におい
ても、揮発性成分蒸気の蒸気圧を化学量論的に当
量となるように制御して不揮発性成分融液に供給
すると、揮発性成分の蒸気圧が高いため反応時に
未反応の揮発性成分がかなり蒸発する。また、結
晶の融点付近での反応のため、融液被覆材料とし
てのB2O3等の不活性液体成分との反応により、
ホウ素等の不純物の混入が多くなつてしまう。
そこで、揮発性成分の損失及び不純物の混入を
抑制するため、温度を結晶の融点よりも低く且つ
揮発性成分蒸気の蒸気圧を化学量論的に当量な蒸
気圧よりも低くした場合には、例えばInPの場合
では、InPはその比重がIn融液よりも小さいため
In融液の上方に浮き上がろうとするが、P蒸気の
噴出し口でInP融液ができ、これがさらに進む反
応の進行を遅らせるため、ルツボ内部まで均一に
反応が進むまでに時間がかかるという問題があ
る。
[発明の目的]
本発明は上記従来技術に鑑みてなされたもの
で、その目的とするところは、揮発性成分蒸気を
反応系外に逃がすことなく不揮発性成分と揮発性
成分との反応を良好に且つスムーズに行わせるこ
とができ、また、不純物の混入が少なく、良質の
結晶を成長させることのできる化合物半導体の製
造方法を提供することにある。
[発明の概要]
すなわち、本発明の要旨は、第1段階としてル
ツボ内の温度を化合物半導体の融点以下にし、揮
発性成分収納容器の温度を制御して揮発性成分蒸
気を化学量論的に当量となる蒸気圧よりも低い蒸
気圧で不揮発性成分融液と反応させ、この低い蒸
気圧での反応を行つた後に、第2段階として上記
ルツボ内の温度を上記化合物半導体の融点付近ま
で昇温し、上記揮発性成分収納容器の温度を昇温
して上記揮発性成分蒸気を化学量論的に当量とな
る蒸気圧で未反応で残つている上記不揮発性成分
融液と反応させ、該反応が完了した後に上記化合
物半導体の単結晶を引き上げ法により製造するこ
とにある。
[実施例]
以下本発明を第1図、第2図に示した実施例を
用いて詳細に説明する。
第1図は本発明を実施するための製造装置の一
例を示す模式的概略図である。第1図において、
1は耐熱、耐圧、機密性構造の反応容器で、反応
容器1の側壁には窒素、アルゴン等の不活性ガス
のガス導入口2、ガス排出口3を設けてあり、ま
た、上部には単結晶引き上げ棒4が上下移動自在
に装着してある。反応容器1内には、黒鉛製のル
ツボ5、揮発性成分収納容器6が設置してあり、
揮発性成分収納容器6には蒸気導入管7が着脱自
在に取り付けてあり、蒸気導入管7は図示のよう
にルツボ5の底部に伸びており、蒸気導入管7の
先端部の蒸気吐出口8は、第2図aまたはbに示
すように、先端を細くした細孔8aとするか、ま
たは、濾過板8bを取り付けた構成としてある。
9はルツボ5の加熱炉、10は不揮発性成分収
納容器6の加熱炉である。11はルツボ5内の不
揮発性成分融液、12は化合物半導体融液、13
は液体シール材を示し、14は揮発性成分収納容
器6内に入れてある揮発性成分である。
なお、蒸気導入管7を着脱自在にしたのは、結
晶成長のたび毎に取りはずしができるようにする
ためであり、蒸気導入管7の先端部の蒸気吐出口
8を第2図に示すようにしたのは、蒸気吐出圧力
の調整を容易にするためと、不揮発性成分融液1
1や化合物半導体融液12の逆流防止のためであ
る。
[Background and Objectives of the Invention] The present invention relates to a method for producing a compound semiconductor, and more particularly to a method for producing a single crystal of a compound semiconductor by pulling and growing a single crystal of a compound semiconductor from a melt synthesized by contacting a non-volatile component melt with volatile component vapor. It is something. [Conventional technology] Conventionally, gallium phosphide (GaP), indium phosphide (InP), gallium arsenide (GaAs), etc.
A method for manufacturing compound semiconductors containing non-volatile components and volatile components of group compound semiconductors is to melt these separately manufactured polycrystals in a crucible and pull up single crystals from this melt. The Kralski method has become mainstream. Unlike this pulling method using polycrystals, a method has been proposed in which a melt of a non-volatile component is reacted with vapor of a volatile component to produce a melt of the target compound, and a single crystal is pulled directly from this melt. There is. For example, a cold room container containing volatile components is provided below a crucible containing a melt of nonvolatile components covered with an inert liquid, and a porous material such as boron nitride (BN) is placed between the crucible and the cold room container. A partition wall made of a material with pores or a material with pores is provided, and the volatile component vapor is supplied through the partition wall to the non-volatile component melt while controlling the vapor pressure by heating the cold room container and reacting with the non-volatile component melt. It has been proposed to pull a single crystal from a liquid (Special Publication No. 12152/1983). However, even under a high-pressure inert gas atmosphere, if the vapor pressure of the volatile component vapor is controlled to be stoichiometrically equivalent and then supplied to the nonvolatile component melt, the vapor pressure of the volatile component will be high. Therefore, a considerable amount of unreacted volatile components evaporate during the reaction. In addition, due to the reaction near the melting point of the crystal, due to the reaction with an inert liquid component such as B 2 O 3 as a melt coating material,
This increases the amount of impurities such as boron. Therefore, in order to suppress the loss of volatile components and the contamination of impurities, when the temperature is lower than the melting point of the crystal and the vapor pressure of the volatile component vapor is lower than the stoichiometrically equivalent vapor pressure, For example, in the case of InP, since the specific gravity of InP is smaller than that of In melt,
The InP melt tries to float above the melt, but the InP melt is formed at the P vapor outlet, which delays the further progress of the reaction, so it takes time for the reaction to proceed uniformly to the inside of the crucible. There's a problem. [Object of the Invention] The present invention has been made in view of the above-mentioned prior art, and its purpose is to improve the reaction between non-volatile components and volatile components without allowing volatile component vapor to escape outside the reaction system. It is an object of the present invention to provide a method for manufacturing a compound semiconductor, which can be performed smoothly and with less contamination of impurities, and can grow high-quality crystals. [Summary of the Invention] That is, the gist of the present invention is that, as a first step, the temperature inside the crucible is lowered to below the melting point of the compound semiconductor, and the temperature of the volatile component storage container is controlled to stoichiometrically control the volatile component vapor. After reacting with the nonvolatile component melt at a vapor pressure lower than the equivalent vapor pressure, and performing the reaction at this low vapor pressure, the temperature in the crucible is raised to around the melting point of the compound semiconductor as a second step. The temperature of the volatile component storage container is raised to cause the volatile component vapor to react with the unreacted non-volatile component melt at a vapor pressure that is stoichiometrically equivalent. After the reaction is completed, a single crystal of the compound semiconductor is manufactured by a pulling method. [Example] The present invention will be described in detail below using the example shown in FIGS. 1 and 2. FIG. 1 is a schematic diagram showing an example of a manufacturing apparatus for implementing the present invention. In Figure 1,
Reference numeral 1 denotes a reaction vessel having a heat-resistant, pressure-resistant, and airtight structure.The side wall of the reaction vessel 1 is provided with a gas inlet 2 for inert gas such as nitrogen or argon, and a gas outlet 3. A crystal pulling rod 4 is mounted so as to be vertically movable. Inside the reaction vessel 1, a crucible 5 made of graphite and a volatile component storage container 6 are installed.
A steam introduction pipe 7 is detachably attached to the volatile component storage container 6, and the steam introduction pipe 7 extends to the bottom of the crucible 5 as shown in the figure, and a steam discharge port 8 at the tip of the steam introduction pipe 7 As shown in FIGS. 2a or 2b, the pores 8a have tapered tips, or a filter plate 8b is attached. 9 is a heating furnace for the crucible 5, and 10 is a heating furnace for the nonvolatile component storage container 6. 11 is a non-volatile component melt in the crucible 5; 12 is a compound semiconductor melt; 13 is a compound semiconductor melt;
indicates a liquid sealing material, and 14 is a volatile component contained in the volatile component storage container 6. The reason why the steam introduction tube 7 is made detachable is to enable it to be removed each time crystal growth occurs. This was done in order to facilitate the adjustment of the steam discharge pressure and to increase the
This is to prevent backflow of the compound semiconductor melt 12 and the compound semiconductor melt 12.
【表】【table】
【表】
次に、InP単結晶を成長させる場合を例にとつ
て、具体的製造方法の一実施例について説明す
る。
InPの圧力−温度−組成の関は第1表に示す通
りであり、これは、例えば、インジウム(In)を
1057℃、リン(P)を585゜とすると、InPの融液
の組成は化学当量的に1:1であり、このときの
圧力は40気圧となることを示している。
成長方法としては、不揮発性成分(In)11と
シール材(B2O3)13とをルツボ5に入れ、ま
た、当量より過剰の揮発性成分(P)14を揮発
性成分収納容器6に入れる。そして、加熱炉9に
よりルツボ5の温度を昇温すると、156℃でIn1
1が融液になり、ルツボ5の底部に流れる。さら
に昇温して460℃になると、B2O313が融解し、
In11を覆う。そして、このまま約1000℃までル
ツボ5を昇温する。
これに合わせて揮発性成分収納容器6を加熱炉
10によつて加熱し、圧力バランスを保ちながら
420℃まで昇温する。この条件では、Pの蒸気圧
は第1表に示されているように化学量論的に当量
よりも低い1.1気圧であり、P蒸気は蒸気導入管
7、蒸気吐出口8を経て、Inの融液11に混入
し、Pの組成が約34%(比重約5.6)のInP化合物
半導体融液12ができ、比重7.3のIn11と比重
2.5のB2O313との間に層状に遊離する。
このように結晶の融点よりも低い温度で且つ化
学量論的に当量よりも低いP蒸気圧でIn融液と反
応させることにより、InP化合物半導体融液12
がIn11とB2O313との間に層状に遊離するこ
ともあつて、P蒸気がB2O313を通つて逃げる
ことはなくまたB2O313からの不純物の混入を
抑制することができる。
ルツボ5内のIn11の反応がほぼ完了したらガ
ス導入口2より不活性ガスを導入し、圧力バラン
スをとりながらルツボ5をInPの融点である1057
℃まで昇温し、揮発性成分収納容器6を585℃ま
で昇温してPの蒸気圧を化学量論的に当量の40気
圧にし、全体の反応が均一になるまでしばらく放
置する。そして、化学量論的に当量の特性の安定
したInP化合物半導体融液12ができたら、単結
晶引き上げ棒4を徐々に下げ、シーデングを行つ
てInP化合物半導体の単結晶を引き上げ成長させ
る。このようにして、化合物半導体を製造する。
上記した本発明の実施例によれば、始めに比較
的低温で、しかも、低い蒸気圧でInとPとを気相
−液層界面で直接反応させるようにしているの
で、Pが反応系外にほとんど逃げることがなく、
またホウ素の不純物濃度を従来の場合の1/10とす
ることができ、良質の結晶が得られる。
さらに、合成反応速度は、始めは反応によつて
生じたInP等の化合物半導体融液により若干遅い
ものの、その後P蒸気圧を上げることにより反応
が速くなり、極めてスムーズに合成反応が進むた
め量産的である。
[発明の効果]
以上説明したように、本発明によれば、揮発性
成分蒸気を反応系外に逃がすことなく不揮発性成
分と揮発性成分との反応を良好に且つスムーズに
行わせることができ、また、不純物の混入が少な
く良質の結晶を成長させることができるという効
果がある。[Table] Next, an example of a specific manufacturing method will be described using the case of growing an InP single crystal as an example. The pressure-temperature-composition relationship of InP is shown in Table 1, which indicates that, for example, indium (In)
Assuming that the temperature is 1057°C and phosphorus (P) is 585°, the composition of the InP melt is 1:1 in terms of chemical equivalence, and the pressure at this time is 40 atmospheres. As a growth method, a non-volatile component (In) 11 and a sealing material (B 2 O 3 ) 13 are placed in a crucible 5, and an excess of the volatile component (P) 14 is placed in a volatile component storage container 6. put in. Then, when the temperature of the crucible 5 is raised by the heating furnace 9, In1 reaches 156℃.
1 becomes a melt and flows to the bottom of the crucible 5. When the temperature further increases to 460℃, B 2 O 3 13 melts,
Cover In11. Then, the temperature of the crucible 5 is raised to about 1000°C. At the same time, the volatile component storage container 6 is heated by the heating furnace 10, while maintaining the pressure balance.
Raise the temperature to 420℃. Under these conditions, the vapor pressure of P is 1.1 atm, which is stoichiometrically lower than the equivalent amount, as shown in Table 1, and the P vapor passes through the steam inlet pipe 7 and the steam outlet 8, and the P vapor passes through the steam inlet pipe 7 and the steam outlet 8. Mixed into the melt 11, an InP compound semiconductor melt 12 with a P composition of about 34% (specific gravity of about 5.6) is formed, and the InP compound semiconductor melt 12 has a specific gravity of about 7.3.
It is liberated in a layer between 2.5 and 13 B 2 O 3 . In this way, by reacting with the In melt at a temperature lower than the melting point of the crystal and at a P vapor pressure lower than the stoichiometrically equivalent amount, the InP compound semiconductor melt 12
may be liberated between In11 and B2O313 in a layered manner, so P vapor does not escape through B2O313 , and contamination of impurities from B2O313 is suppressed . be able to. When the reaction of In11 in the crucible 5 is almost completed, inert gas is introduced from the gas inlet 2, and while maintaining pressure balance, the crucible 5 is heated to the melting point of InP, 1057.
The temperature of the volatile component storage container 6 is raised to 585°C to bring the vapor pressure of P to 40 atmospheres, which is the stoichiometric equivalent, and the mixture is left for a while until the entire reaction becomes uniform. Once the InP compound semiconductor melt 12 with stable stoichiometric properties is produced, the single crystal pulling rod 4 is gradually lowered to perform seeding and pull and grow the InP compound semiconductor single crystal. In this way, a compound semiconductor is manufactured. According to the embodiment of the present invention described above, since In and P are first reacted directly at the gas phase-liquid layer interface at a relatively low temperature and low vapor pressure, P is removed from the reaction system. There is almost no escape from
In addition, the boron impurity concentration can be reduced to 1/10 of the conventional method, resulting in high quality crystals. Furthermore, although the synthesis reaction rate is initially a little slow due to the compound semiconductor melt such as InP generated by the reaction, the reaction speeds up by increasing the P vapor pressure, and the synthesis reaction proceeds extremely smoothly, making it suitable for mass production. It is. [Effects of the Invention] As explained above, according to the present invention, the reaction between the non-volatile components and the volatile components can be carried out favorably and smoothly without escaping the volatile component vapor to the outside of the reaction system. In addition, there is an effect that high-quality crystals can be grown with less contamination of impurities.
第1図は本発明の化合物半導体の製造方法を実
施するための製造装置の一例を示す模式的概略
図、第2図は第1図の蒸気導入管の蒸気吐出口の
一実施例を示す構造説明図である。
1:反応容器、2:ガス導入口、3:ガス排出
口、4:単結晶引き上げ棒、5:ルツボ、6:揮
発性成分収納容器、7:蒸気導入管、8:蒸気吐
出口、9,10:加熱炉、11:不揮発性成分融
液、12:化合物半導体融液、13:シール材、
14:揮発性成分。
FIG. 1 is a schematic diagram showing an example of a manufacturing apparatus for carrying out the compound semiconductor manufacturing method of the present invention, and FIG. 2 is a structure showing an example of the steam outlet of the steam introduction pipe in FIG. 1. It is an explanatory diagram. 1: Reaction container, 2: Gas inlet, 3: Gas outlet, 4: Single crystal pulling rod, 5: Crucible, 6: Volatile component storage container, 7: Steam inlet pipe, 8: Steam outlet, 9, 10: heating furnace, 11: non-volatile component melt, 12: compound semiconductor melt, 13: sealing material,
14: Volatile component.
Claims (1)
剤を収容し、前記ルツボの外側に揮発性成分を収
納した揮発性成分収納容器を設け、該揮発性成分
収納容器に連結した蒸気導入管の先端を前記不揮
発性成分融液の底部にまで差し込み、該蒸気導入
管の先端から揮発性成分蒸気を供給して合成反応
させ、該合成反応により得られた融液から化合物
半導体を製造する方法において、 第1段階として前記ルツボ内温度を前記化合物
半導体の融点以下にし、前記揮発性成分収納容器
の温度を制御して前記揮発性成分蒸気を化学量論
的に当量となる蒸気圧よりも低い蒸気圧で前記不
揮発性成分融液と反応させ、この低い蒸気圧での
反応を行つた後に、 第2段階として前記ルツボ内温度を前記化合物
半導体の融点付近にまで昇温し、前記揮発性成分
収納容器の温度を昇温して前記揮発性成分蒸気を
化学量論的に当量となる蒸気圧で未反応で残つて
いる前記不揮発性成分融液と反応させ、 該反応が完了した後に前記化合物半導体の単結
晶を引き上げ法により製造することを特徴とする
化合物半導体の製造方法。 2 前記揮発性成分を含む化合物半導体がリン化
インジウム、砒化ガリウムまたはリン化ガリウム
化合物半導体である特許請求の範囲第1項記載の
化合物半導体の製造方法。[Claims] 1. A non-volatile component melt and a liquid sealant are stored in a crucible, and a volatile component storage container storing volatile components is provided outside the crucible, and connected to the volatile component storage container. Insert the tip of the vapor introduction tube to the bottom of the nonvolatile component melt, supply volatile component vapor from the tip of the vapor introduction tube to cause a synthesis reaction, and form a compound semiconductor from the melt obtained by the synthesis reaction. In the method for manufacturing, as a first step, the temperature inside the crucible is made equal to or lower than the melting point of the compound semiconductor, and the temperature of the volatile component storage container is controlled so that the volatile component vapor becomes stoichiometrically equivalent. After performing the reaction at this low vapor pressure, the temperature inside the crucible is raised to around the melting point of the compound semiconductor as a second step, The temperature of the volatile component storage container is raised to cause the volatile component vapor to react with the unreacted non-volatile component melt at a stoichiometrically equivalent vapor pressure, and the reaction is completed. A method for manufacturing a compound semiconductor, comprising: manufacturing a single crystal of the compound semiconductor by a pulling method. 2. The method for manufacturing a compound semiconductor according to claim 1, wherein the compound semiconductor containing a volatile component is indium phosphide, gallium arsenide, or a gallium phosphide compound semiconductor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15762583A JPS6051697A (en) | 1983-08-29 | 1983-08-29 | Compound semiconductor manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15762583A JPS6051697A (en) | 1983-08-29 | 1983-08-29 | Compound semiconductor manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6051697A JPS6051697A (en) | 1985-03-23 |
| JPS6335600B2 true JPS6335600B2 (en) | 1988-07-15 |
Family
ID=15653816
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15762583A Granted JPS6051697A (en) | 1983-08-29 | 1983-08-29 | Compound semiconductor manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6051697A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61227985A (en) * | 1985-04-02 | 1986-10-11 | Hitachi Cable Ltd | Method for manufacturing compound semiconductor single crystal |
| JPS6230689A (en) * | 1985-08-02 | 1987-02-09 | Mitsubishi Metal Corp | Growth of iii-v semiconductor crystal and apparatus therefor |
| CN102628180A (en) * | 2012-04-23 | 2012-08-08 | 南京金美镓业有限公司 | Preparation method of high-purity indium phosphide polycrystalline rod |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5212152A (en) * | 1975-07-18 | 1977-01-29 | Idemitsu Kosan Co Ltd | Process for alkylation of adamantanes |
| JPS606920B2 (en) * | 1982-11-12 | 1985-02-21 | 工業技術院長 | Gallium arsenide single crystal production equipment |
-
1983
- 1983-08-29 JP JP15762583A patent/JPS6051697A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6051697A (en) | 1985-03-23 |
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