JPH0226887A - Liquid phase epitaxial growth method - Google Patents
Liquid phase epitaxial growth methodInfo
- Publication number
- JPH0226887A JPH0226887A JP17747988A JP17747988A JPH0226887A JP H0226887 A JPH0226887 A JP H0226887A JP 17747988 A JP17747988 A JP 17747988A JP 17747988 A JP17747988 A JP 17747988A JP H0226887 A JPH0226887 A JP H0226887A
- Authority
- JP
- Japan
- Prior art keywords
- heat treatment
- growth
- liquid phase
- epitaxial growth
- phase epitaxial
- 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
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- Crystals, And After-Treatments Of Crystals (AREA)
- Liquid Deposition Of Substances Of Which Semiconductor Devices Are Composed (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、化合物半導体結晶成長等に用いられる液相エ
ピタキシャル成長方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a liquid phase epitaxial growth method used for compound semiconductor crystal growth and the like.
液相エピタキシャル成長法は、特に化合物半導体のエピ
タキシャル結晶を成長させる方法の中で最も簡便な方法
であり、小面積ながら良質の結晶を得ることができる。The liquid phase epitaxial growth method is particularly the simplest method among methods for growing epitaxial crystals of compound semiconductors, and can obtain high-quality crystals in a small area.
この方法は、基本的にはIn、 Gaなどの低融点金属
の溶媒に溶質を所定の温度で溶解させかつほぼ飽和させ
一定時間保持した後、この融液を徐冷することによって
溶解度が低下し、その温度降下幅に相当する過剰溶質を
結晶としてInP XGaAs等の基板上に析出させ、
InP 、 InGaAsPなどのエピタキシャル結晶
を得るものである。This method basically involves dissolving a solute in a solvent of a low-melting point metal such as In or Ga at a predetermined temperature, reaching near saturation and holding for a certain period of time, and then slowly cooling this melt to reduce the solubility. , the excess solute corresponding to the width of the temperature drop is precipitated as crystals on a substrate such as InP XGaAs,
This method is used to obtain epitaxial crystals such as InP and InGaAsP.
この方法によって得られるエピタキシャル結晶の特性、
即ち不純物濃度、移動度等の電気的特性および結晶性は
、溶媒等の原料が高純度であることのみならずInP
、、 GaAsなどの溶質、成長に用いるボートなどに
吸着した酸素、水分等の不純物の存在に大きく依存する
ことが知られている。Properties of epitaxial crystals obtained by this method,
In other words, the impurity concentration, electrical properties such as mobility, and crystallinity are determined not only by the high purity of the raw materials such as the solvent but also by the high purity of InP.
,, It is known that it greatly depends on the presence of solutes such as GaAs and impurities such as oxygen and moisture adsorbed on the boat used for growth.
原料の高純度化のために、あるいはこれらの不純物の除
去のために、通常、溶質や成長融液を含んだ成長用ボー
ト等を極めて長時間の間アルゴン、窒素などの不活性ガ
スまたは水素ガス中で高温熱処理する必要がある。In order to highly purify raw materials or remove these impurities, growth boats containing solutes and growth melt are usually exposed to inert gas such as argon, nitrogen, or hydrogen gas for an extremely long period of time. It is necessary to perform high-temperature heat treatment inside.
例えば、InP基板上にInPを液相エピタキうノヤル
成長法によって結晶成長させる場合、その結晶のキャリ
ア濃度を5×10′6原子cm−’程度とするためには
、予めIn融液を700°Cで約10時間水素ガスを流
しなからベーキング熱処理をする(特公昭61−123
69号公報参照)。このベーキングが終了し、冷却した
後、原料を所定のボートに入れ装置中で再び昇温し、高
温である一定時間保持してからエピタキシャル成長を行
なわせる。For example, when growing an InP crystal on an InP substrate by liquid phase epitaxy, in order to make the carrier concentration of the crystal about 5 x 10'6 atoms cm-', the In melt is heated at 700° in advance. Baking heat treatment is performed at C for about 10 hours while flowing hydrogen gas (Special Publication No. 61-123)
(See Publication No. 69). After this baking is completed and cooled, the raw material is placed in a predetermined boat, heated again in the apparatus, and kept at high temperature for a certain period of time before epitaxial growth is performed.
以上のように従来の方法は、長時間にわたる高温熱処理
が必要なため生産性が悪く、大量の電力と高純度ガスを
消費するという欠点がある。As described above, the conventional method has disadvantages in that it requires high-temperature heat treatment over a long period of time, resulting in poor productivity and consuming a large amount of electricity and high-purity gas.
また、原料のベーキング後これらの原料を用いてエピタ
キシャル成長させる場合、原料等を成長装置に入れる時
の取扱いなどによって成長用ボートや溶媒に吸着する酸
素、水分等の不純物の量が異るために、予め決めた一定
の時間の高温熱処理を施しても所望の不純物濃度の結晶
が得られなく、再現性が悪い場合がある。In addition, when performing epitaxial growth using these raw materials after baking the raw materials, the amount of impurities such as oxygen and moisture adsorbed to the growth boat or solvent varies depending on the handling when loading the raw materials into the growth equipment. Even if high-temperature heat treatment is performed for a predetermined period of time, crystals with the desired impurity concentration may not be obtained, and reproducibility may be poor.
これに加えて、成長用ボート等に吸着した酸素や水分な
どの不純物が十分に除去されないまま高温へ昇温を開始
すると、この昇温中にこれらの不純物が局所的に高濃度
となって集まり、これらの分子が成長融液に混入する。In addition to this, if the temperature starts to rise to a high temperature before the impurities such as oxygen and moisture adsorbed on the growth boat are sufficiently removed, these impurities will locally gather at a high concentration during this temperature rise. , these molecules mix into the growing melt.
このため成長融液が汚染され、これらの不純物分子の除
去のために更に長時間の熱処理が必要となるという欠点
がある。This has the disadvantage that the growth melt is contaminated and a longer heat treatment is required to remove these impurity molecules.
本発明は液相エピタキシャル成長方法における、上述の
ような課題を解決しようとするものである。The present invention aims to solve the above-mentioned problems in a liquid phase epitaxial growth method.
本発明は以上の課題を解決するために、融点が80℃以
上の金属を溶媒とする液相エピタキシャル成長方法にお
いて、前記成長工程に用いるボート、溶質、結晶基板お
よび溶媒金属を、不活性ガスまたは水素ガスの気流中で
80”C以上かつ前記溶媒金属の融点以下の温度で第1
の熱処理を行い、引き続いて、溶解もしくはベーキング
のために前記溶媒金属の融点以上の温度で第2の熱処理
を行う。In order to solve the above problems, the present invention provides a liquid phase epitaxial growth method using a metal with a melting point of 80° C. or higher as a solvent, in which the boat, solute, crystal substrate, and solvent metal used in the growth step are replaced with an inert gas or hydrogen gas. The first step is performed in a gas stream at a temperature of 80"C or higher and lower than the melting point of the solvent metal.
This is followed by a second heat treatment at a temperature equal to or higher than the melting point of the solvent metal for melting or baking.
この第1の熱処理は不純物ガス濃度が充分に低下するま
で行い、その不純物ガス濃度の低下を検知した後そのま
ま温度を上げて第2の熱処理を行うことが望ましい。ま
た、第1の熱処理温度の下限は、好ましくは水の沸点で
ある100’C以上であるとよい。It is desirable that this first heat treatment is performed until the impurity gas concentration is sufficiently reduced, and after detecting the decrease in the impurity gas concentration, the temperature is raised as it is and the second heat treatment is performed. Further, the lower limit of the first heat treatment temperature is preferably 100'C or higher, which is the boiling point of water.
ここで第2の熱処理とはベーキングのほが、液相エピタ
キシャル成長のために所定の温度にし徐冷を開始するま
で所定の時間保持することも含む。Here, the second heat treatment includes baking, but also includes setting the temperature to a predetermined temperature for liquid phase epitaxial growth and holding it for a predetermined time until slow cooling is started.
本発明による液相エピタキシャル成長方法によると、第
1の熱処理によって成長用ボートなどの成長系内に吸着
した酸素、水分等の不純物を十分に除去することができ
るので、引き続いて行う第2の熱処理による効果の再現
性がよくなり、また第2の熱処理の時間も短縮できる。According to the liquid phase epitaxial growth method according to the present invention, since impurities such as oxygen and moisture adsorbed in the growth system such as a growth boat can be sufficiently removed by the first heat treatment, the second heat treatment performed subsequently The reproducibility of the effect is improved, and the time for the second heat treatment can also be shortened.
本発明の実施例を第1図および第2図を参照しながら説
明する。An embodiment of the present invention will be described with reference to FIGS. 1 and 2.
本実施例ではInPO液相エピタキシャル成長の場合を
例とし、成長溶媒としてIn、溶質としてlnP %お
よび結晶基板としてInP基板をそれぞれ第1図に示す
成長用グラファイトボート1の所定の位置に入れ、この
ボート1を石英製反応管2の中に配置する。次に、この
管の中を排気し1O−5Pa以下とし、その後水素を置
換し、26/分の速度で水素を流す。Inの融点は約1
55℃であるので、第1図に示す加熱炉3によって成長
用グラファイトボート1を、第2図に示す温度プログラ
ムのように、第1の熱処理として130°Cにして後述
する酸素濃度がo、o5ppm以下となるまで約1時間
保持する。しかる後に、第2の熱処理として685°C
まで昇温し1〜2時間保つ。この後、0.45℃/分の
冷却速度で徐冷を開始し、所定の温度範囲で結晶基板に
InPをエピタキシャル成長させる。In this example, InPO liquid phase epitaxial growth is taken as an example, and In as a growth solvent, InP as a solute, and an InP substrate as a crystal substrate are placed in predetermined positions in a graphite boat for growth 1 shown in FIG. 1 is placed in a quartz reaction tube 2. Next, the inside of this tube is evacuated to a pressure of 10-5 Pa or less, and then hydrogen is replaced and hydrogen is caused to flow at a rate of 26/min. The melting point of In is approximately 1
Since the temperature is 55°C, the graphite boat 1 for growth is heated to 130°C as the first heat treatment as shown in the temperature program shown in Fig. 2 using the heating furnace 3 shown in Fig. 1, and the oxygen concentration as described below is o. Hold for about 1 hour until o5ppm or less. After that, a second heat treatment at 685°C
Raise the temperature to 1-2 hours. Thereafter, slow cooling is started at a cooling rate of 0.45° C./min, and InP is epitaxially grown on the crystal substrate within a predetermined temperature range.
不純物の中で、特に酸素は、反応管の中を流れこれから
出てくる水素ガス中の酸素濃度をモニターすることによ
って成長系から除去されたかを知ることができる。この
モニターの結果によると、低温(130°C)で1時間
の第1の熱処理を施した後、更に温度を上げても水素ガ
ス中の酸素濃度は上昇しないので、この第1の熱処理に
よって成長用ボード等の成長系から酸素を十分に除去で
きたことがわかった。Among the impurities, it is possible to know whether oxygen in particular has been removed from the growth system by monitoring the oxygen concentration in the hydrogen gas flowing through the reaction tube and coming out. According to the results of this monitor, the oxygen concentration in the hydrogen gas does not increase even if the temperature is further increased after the first heat treatment is performed at a low temperature (130°C) for one hour. It was found that oxygen could be sufficiently removed from the growth system such as commercial boards.
本発明による第1の熱処理の効果を確認するために、こ
の第1の熱処理を行なわずそれ以外は第2図に示す温度
プログラムと同じ条件で液相エピタキシャル成長させた
場合、および第2図の温度プログラムに従って第1の熱
処理を行い液相エピタキシャル成長させた場合に得られ
たそれぞれのInP結晶について、キャリア移動度を絶
対温度300°にで測定した。その結果によると、前者
の場合は約3000 c+a/Volt・秒であったが
、後者の本発明による方法の場合は約4500 cd/
Volt・秒であった。これによって、不純物濃度がか
なり低くなっていることがわかったので、本発明におけ
る第1の熱処理は極めて大きな効果があるという結論を
得た。In order to confirm the effect of the first heat treatment according to the present invention, a case where liquid phase epitaxial growth was performed without performing this first heat treatment under the same conditions as the temperature program shown in FIG. 2, and a case where the temperature program shown in FIG. The carrier mobility was measured at an absolute temperature of 300° for each InP crystal obtained when the first heat treatment was performed according to the program and liquid phase epitaxial growth was performed. According to the results, the former case was approximately 3000 c+a/Volt·sec, while the latter method according to the present invention was approximately 4500 cd/sec.
It was Volt/second. As a result, it was found that the impurity concentration was considerably reduced, and it was concluded that the first heat treatment in the present invention has an extremely large effect.
なお、本実施例おいては液相エピタキシャル成長を行う
場合に低温での第1の熱処理を行い、上述のような効果
を得ているが、成長用の原料を精製するためのベーキン
グ直前に同様の低温での熱処理を行えば、同様の不純物
除去の効果が得られ、高温でのベーキング時間の短縮を
はかれる。In this example, when performing liquid phase epitaxial growth, the first heat treatment was performed at a low temperature and the above-mentioned effect was obtained. If heat treatment is performed at a low temperature, a similar effect of removing impurities can be obtained, and the baking time at a high temperature can be shortened.
本発明は上述のような構成としているので、液相エピタ
キシャル成長法における成長融液の純化あるいは成長用
原料の精製を、低温での第1の熱処理を施すことによっ
て一定の短時間で行うことができ、その得られるエピタ
キシャル結晶は一定の優れた特性を有する。Since the present invention has the above-described configuration, purification of the growth melt or the growth raw material in the liquid phase epitaxial growth method can be performed in a certain short time by performing the first heat treatment at a low temperature. , the resulting epitaxial crystal has certain excellent properties.
短時間でエピタキシャル成長が可能となり、結晶基板を
長い間高温にさらすことがなくなるので、結晶基板への
悪影響を少なくすることができる。Since epitaxial growth can be performed in a short time and the crystal substrate is not exposed to high temperatures for a long period of time, adverse effects on the crystal substrate can be reduced.
高純度エピタキシャル結晶を得るための液相エピタキシ
ャル成長工程に要する時間を大きく短縮でき生産性が向
上する。また、消費する電力、高純度ガスも少なくなる
ので経済的にも有利である。The time required for the liquid phase epitaxial growth process for obtaining high-purity epitaxial crystals can be greatly shortened and productivity can be improved. In addition, it is economically advantageous because it consumes less electricity and less high-purity gas.
第1図は本実施例の液相エピタキシャル成長に用いた装
置の概略図、第2図は本実施例における液相エピタキシ
ャル成長工程の温度プログラム図である。
なお図面に用いた符号において、
1−・=−−−−一一一−−−−成長用グラファイトポ
ート2−・−−−−一・−−−一−−−−−−石英製反
応管3−−一一一−−−−−−−−加熱炉
である。FIG. 1 is a schematic diagram of an apparatus used for liquid phase epitaxial growth in this example, and FIG. 2 is a temperature program diagram for the liquid phase epitaxial growth process in this example. In addition, in the symbols used in the drawings, 1-・=-----111-----Growth graphite port 2--・-----1・----1--------Quartz reaction tube 3--111-----Heating furnace.
Claims (1)
ル成長方法において、 前記成長工程に用いるボート、溶質、結晶基板および溶
媒金属を、不活性ガスまたは水素ガスの気流中で80℃
以上かつ前記溶媒金属の融点以下の温度で第1の熱処理
を行い、 引き続いて、溶解もしくはベーキングのために前記溶媒
金属の融点以上の温度で第2の熱処理を行うことを特徴
とする液相エピタキシャル成長方法。[Claims] In a liquid phase epitaxial growth method using a metal with a melting point of 80° C. or higher as a solvent, a boat, a solute, a crystal substrate, and a solvent metal used in the growth step are grown in an inert gas or hydrogen gas stream for 80° C. ℃
Liquid phase epitaxial growth characterized by performing a first heat treatment at a temperature above and below the melting point of the solvent metal, and subsequently performing a second heat treatment at a temperature above the melting point of the solvent metal for melting or baking. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17747988A JPH0226887A (en) | 1988-07-16 | 1988-07-16 | Liquid phase epitaxial growth method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17747988A JPH0226887A (en) | 1988-07-16 | 1988-07-16 | Liquid phase epitaxial growth method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0226887A true JPH0226887A (en) | 1990-01-29 |
Family
ID=16031633
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17747988A Pending JPH0226887A (en) | 1988-07-16 | 1988-07-16 | Liquid phase epitaxial growth method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0226887A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6439898B1 (en) * | 2017-07-04 | 2018-12-19 | 住友電気工業株式会社 | Indium phosphide single crystal and indium phosphide single crystal substrate |
-
1988
- 1988-07-16 JP JP17747988A patent/JPH0226887A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6439898B1 (en) * | 2017-07-04 | 2018-12-19 | 住友電気工業株式会社 | Indium phosphide single crystal and indium phosphide single crystal substrate |
| WO2019009306A1 (en) * | 2017-07-04 | 2019-01-10 | 住友電気工業株式会社 | Indium phosphide single crystal and indium phosphide single crystal substrate |
| WO2019008662A1 (en) * | 2017-07-04 | 2019-01-10 | 住友電気工業株式会社 | Indium phosphide single crystal and indium phosphide single crystal substrate |
| JPWO2019009306A1 (en) * | 2017-07-04 | 2019-07-04 | 住友電気工業株式会社 | Indium phosphide single crystal and indium phosphide single crystal substrate |
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