JPH0477717B2 - - Google Patents
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- JPH0477717B2 JPH0477717B2 JP76488A JP76488A JPH0477717B2 JP H0477717 B2 JPH0477717 B2 JP H0477717B2 JP 76488 A JP76488 A JP 76488A JP 76488 A JP76488 A JP 76488A JP H0477717 B2 JPH0477717 B2 JP H0477717B2
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- temperature
- growth
- gaas
- melt
- crystal
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- Liquid Deposition Of Substances Of Which Semiconductor Devices Are Composed (AREA)
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明はGaAlAsの結晶成長に関し、特に溶質
を溶解したメルト内に一定の温度差を設け、高温
部より低温部に連続的に溶質を搬送して低温部で
結晶を成長させる温度差法によるGaAlAsの液相
エピタキシヤル結晶成長に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to crystal growth of GaAlAs, and in particular creates a certain temperature difference in a melt in which a solute is dissolved, and continuously transports the solute from a high temperature area to a low temperature area. This paper relates to liquid-phase epitaxial crystal growth of GaAlAs using a temperature difference method in which crystals are grown in a low-temperature region.
[従来の技術]
Ga1-xAlxAsは結晶中の組成x(AlAsの割合)
を変えることにより、そのバンドギヤンプエネル
ギを1.43eVから2.16eVまで変えることができる
混晶半導体である。そのためGa1-xAlxAsは赤外
光から可視光までの発光ダイオド(LED)の材
料として広く用いられている。例えば、波長
660nmの赤色LEDを得るには、発光層のP−
Ga1-xAlxAsのxを約0.35,波長780nmのLEDを
得るにはxを約0.15,波長850nmの赤外LEDを得
るにはxを約0.01とすればよい。したがつて、
GaAlAsのLEDにおいては、目的とする発光波長
に応じてp−Ga1-xAlxAsのxが決められる。n
−Ga1-xAlxAsのxも一定でなく、目的とする発
光波長に応じて決められる。n−Ga1-xAlxAsの
xは、p−Ga1-xAlxAs発光層に電子や正孔を閉
じ込めておくため、あるいは、p−Ga1-xAlxAs
層での発光を吸収せず有効に結晶外まで導くため
に必要な値が選ばれる。たとえば、p−Ga1-x
AlxAsのxが0.35の場合、n−Ga1-xAlxAsのxは
0.6−0.85に選ばれる。[Prior art] Ga 1-x Al x As is the composition x in the crystal (proportion of AlAs)
It is a mixed crystal semiconductor whose band gap energy can be changed from 1.43eV to 2.16eV by changing the . Therefore, Ga 1-x Al x As is widely used as a material for light emitting diodes (LEDs) that emit light from infrared to visible light. For example, the wavelength
To obtain a 660nm red LED, the P-
For Ga 1-x Al x As, x should be about 0.35, x should be about 0.15 to obtain an LED with a wavelength of 780 nm, and x should be about 0.01 to obtain an infrared LED with a wavelength of 850 nm. Therefore,
In a GaAlAs LED, x in p-Ga 1-x Al x As is determined depending on the target emission wavelength. n
-Ga 1-x Al x x in As is also not constant and is determined depending on the target emission wavelength. x in n-Ga 1-x Al x As is for confining electrons and holes in the p-Ga 1-x Al x As luminescent layer, or for p-Ga 1-x Al x As
A value is selected that is necessary to effectively guide light emitted from the layer to the outside of the crystal without absorbing it. For example, p-Ga 1-x
If x of Al x As is 0.35, then x of n-Ga 1-x Al x As is
It is chosen to be 0.6−0.85.
LEDの活性領域は通常基板結晶上にエピタキ
シヤル成長を行うことによつて作られる。基板結
晶としては、高価でなく大口径で結晶性の良いも
のが得られることが望ましい。Ga1-xAlxAs混晶
は組成xの全域にわたり、GaAs結晶との格子不
整合が少ない。そこで、大口径で良質の結晶が得
られるGaAsの基板上に良質のGa1-xAlxAsをエピ
タキシヤル成長することができる。これらの理由
によりGaAlAsは現在赤外光から赤色光まで高輝
度高出力の発光ダイオードとして多く用いられて
いる。このような発光デバイスとしてGa1-xAlx
Asを用いるとき、発光波長、外部発光効率等の
点から組成xを制御することは重要な課題であ
る。 The active region of an LED is usually produced by epitaxial growth on a substrate crystal. As the substrate crystal, it is desirable to obtain one that is not expensive, has a large diameter, and has good crystallinity. The Ga 1-x Al x As mixed crystal has little lattice mismatch with the GaAs crystal over the entire range of composition x. Therefore, it is possible to epitaxially grow high-quality Ga 1-x Al x As on a GaAs substrate, which provides a large diameter and high-quality crystal. For these reasons, GaAlAs is currently widely used as a light emitting diode with high brightness and high output from infrared light to red light. Ga 1-x Al x as such a light emitting device
When using As, it is an important issue to control the composition x in terms of emission wavelength, external emission efficiency, etc.
液相結晶成長方法として徐冷法や温度差法等が
知られている。徐冷法は、メルトを徐々に冷却し
て結晶化させる方法である。 As a liquid phase crystal growth method, a slow cooling method, a temperature difference method, etc. are known. The slow cooling method is a method in which the melt is gradually cooled and crystallized.
温度差法は一定の温度差(ないし温度勾配)を
持つ高温部低温部を形成し、高温部から原料を供
給して低温部で結晶を析出させる方法であり、溶
液(メルト)内に温度差を設け、高温部で溶質を
溶解(供給)し、温度勾配と拡散によつて低温部
に輪送し、低温部で過飽和溶液から溶質を析出さ
せる方法をさす。すなわち、温度差法液相結晶成
長では、徐冷法のように温度を徐々に下げるので
はなく、一定温度で成長がおこなわれるため、温
度変化による結晶欠陥の発生や結晶組成や不純物
濃度の変動が少ない。また連続して多数枚成長で
きる。GaAlAs系結晶の場合、グラフアイトから
なるメルト槽にGa溶液からなるメルトを入れ、
800℃−1000℃、好ましくは850℃−950℃で10℃
−60℃の温度差を設けて結晶成長を行う。この方
法により、特性の優れた発光ダイオードやレーザ
ー等が製作されている。 The temperature difference method is a method in which a high temperature part and a low temperature part are formed with a certain temperature difference (or temperature gradient), and raw materials are supplied from the high temperature part and crystals are precipitated in the low temperature part. This refers to a method in which a solute is dissolved (supplied) in a high-temperature section, transported to a low-temperature section by temperature gradient and diffusion, and the solute is precipitated from a supersaturated solution in the low-temperature section. In other words, in the temperature difference method liquid phase crystal growth, growth is performed at a constant temperature rather than gradually lowering the temperature as in the slow cooling method, so there is less occurrence of crystal defects and fluctuations in crystal composition and impurity concentration due to temperature changes. . It can also grow in large numbers in succession. In the case of GaAlAs-based crystals, a melt made of Ga solution is placed in a melt bath made of graphite,
10℃ at 800℃-1000℃, preferably 850℃-950℃
Crystal growth is performed with a temperature difference of -60°C. Using this method, light emitting diodes, lasers, etc. with excellent characteristics are manufactured.
[発明が解決しようとする問題点]
メルトから混晶結晶を析出させる場合、メルト
の溶質の組成と成長結晶の組成xとは一般的に等
しくない。[Problems to be Solved by the Invention] When a mixed crystal is precipitated from a melt, the solute composition of the melt and the composition x of the growing crystal are generally not equal.
ところが、温度差法によるGa1-xAlxAsの液相
結晶成長においては、メルト組成と結晶組成との
間に明確な関係が見出だされておらず、希望する
結晶組成xをえようとすると多数の実験を繰り返
さなければならなかつた。 However, in the liquid phase crystal growth of Ga 1-x Al x As using the temperature difference method, no clear relationship has been found between the melt composition and the crystal composition, and it is difficult to obtain the desired crystal composition x. Therefore, many experiments had to be repeated.
本発明の目的は、希望する組成xのGa1-xAlx
As結晶が容易に得られる結晶成長技術を提供す
ることである。 The object of the present invention is to obtain Ga 1-x Al x with a desired composition x.
The object of the present invention is to provide a crystal growth technique that allows As crystals to be easily obtained.
[問題点を解決するために行つた検討]
一般に液相成長法によつて成長されるGa1-x
AlxAs結晶の組成xを決定するのは、溶液(メル
ト)中のAlの濃度である。液相エピタキシヤル
成長法としてひろく用いられている徐冷法では、
例えば
(1)1968 SYMPOSIUM on GaAs,paper 1
(2)Jap.J.Appl.Phys,Vol.18,no.8,1979,
p1509
に示されているように、溶液中のAlの濃度と成
長するGa1-xAlxAs結晶の組成xとの間に一定の
関係が存在することが知られている。この関係を
第2図,第3図に再現する。これらを用いて、成
長するGa1-xAlxAs結晶の組成xと成長温度に応
じて材料であるAlおよびGaAsと溶媒であるGa
の量が容易に決定できる。具体的には、以下のよ
うにすればよい。所望のGa1-xAlxAs結晶の組成
xとメルト低温部または基板の温度である成長温
度とを用いて第2図から溶媒GaにたいするAlの
重量比[Al]/[Ga]を得る。この[Al]/
[Ga]と成長温度とを用いてAl−Ga溶液に対す
るGaAsの飽和溶解度を示す第3図より溶解する
GaAsの量が溶媒Gaに対するGaAsの重量比
[GaAs]/[Ga]として求められる。この
[Al]/[Ga]と[GaAs]/[Ga]より各材料
の量を秤量し成長用メルトを形成する。[Study conducted to solve the problem] Ga 1-x, which is generally grown by liquid phase growth method
It is the concentration of Al in the solution (melt) that determines the composition x of the Al x As crystal. In the slow cooling method, which is widely used as a liquid phase epitaxial growth method,
For example, (1) 1968 SYMPOSIUM on GaAs, paper 1 (2) Jap.J.Appl.Phys, Vol. 18, no. 8, 1979,
As shown on page 1509, it is known that a certain relationship exists between the concentration of Al in the solution and the composition x of the growing Ga 1-x Al x As crystal. This relationship is reproduced in FIGS. 2 and 3. Using these, the materials Al and GaAs and the solvent Ga
The amount of can be easily determined. Specifically, it may be done as follows. The weight ratio [Al]/[Ga] of Al to the solvent Ga is obtained from FIG. 2 using the desired composition x of the Ga 1-x Al x As crystal and the growth temperature which is the temperature of the melt low temperature section or the substrate. This [Al]/
Figure 3 shows the saturation solubility of GaAs in Al-Ga solution using [Ga] and growth temperature.
The amount of GaAs is determined as the weight ratio of GaAs to solvent Ga: [GaAs]/[Ga]. The amount of each material from [Al]/[Ga] and [GaAs]/[Ga] is weighed to form a growth melt.
本発明者らはこの徐冷法で提案された方法で材
料を秤量し温度差法液相エピタキシヤル成長によ
り成長させた結晶の組成xをEPMAにより測定
した。第4図に測定結果を示す。実線は第2図か
ら再現した徐冷法の場合の成長温度900℃での
[Al]/[Ga]とxの関係である。データプロツ
トから明らかなように組成xとメルト中のAlと
Gaとの重量比[Al]/[Ga]との間には何ら関
連性が見出だせない。このように温度差法液相エ
ピタキシヤル成長においては、徐冷法におけるよ
うな重量比[Al]/[Ga]とxとの間の一定の
関係がなく、徐冷法と同様の方法では所望の組成
xをもつGa1-xAlxAs結晶を得ることができない
ことが判つた。 The present inventors weighed the material using the method proposed for this slow cooling method and measured the composition x of the crystal grown by temperature difference method liquid phase epitaxial growth using EPMA. Figure 4 shows the measurement results. The solid line is the relationship between [Al]/[Ga] and x at a growth temperature of 900° C. in the case of the slow cooling method reproduced from FIG. As is clear from the data plot, the composition x and Al in the melt
No relationship can be found between the weight ratio [Al]/[Ga] with respect to Ga. In this way, in liquid-phase epitaxial growth by temperature difference method, there is no fixed relationship between the weight ratio [Al]/[Ga] and x as in the slow cooling method, and in a method similar to the slow cooling method, it is difficult to obtain the desired composition x. It was found that it was not possible to obtain Ga 1-x Al x As crystals.
本発明者らはさらに多くの実験を行い、温度差
法液相エピタキシヤル結晶成長において、徐冷法
とは異なる一定の関係があることを見出だした。
この関係を利用することが温度差法による液相結
晶成長によりGaAlAs結晶を成長する際、非常に
有用であることを確認した。 The present inventors conducted many more experiments and found that there is a certain relationship in liquid phase epitaxial crystal growth using the temperature difference method, which is different from that in the slow cooling method.
We have confirmed that utilizing this relationship is extremely useful when growing GaAlAs crystals by liquid phase crystal growth using the temperature difference method.
[問題点を解決するための手段]
温度差法によるGa1-xAlxAsの液相結晶成長に
おいては、第1図に示されるような関係が成り立
ち、メルトに溶解するAlとGaAsの重量比
[Al]/[GaAs]=yと成長温度Tが、成長する
Ga1-xAlxAs結晶の組成xと一定の式で表される。
すなわち、
x=A・T+B・log(y)+C, (1)
A=0.00343,B=0.64,C=−1.82,
に従つてyとTを決めればよい。[Means for solving the problem] In the liquid phase crystal growth of Ga 1-x Al x As using the temperature difference method, the relationship shown in Figure 1 holds, and the weights of Al and GaAs dissolved in the melt are The ratio [Al]/[GaAs]=y and the growth temperature T are the growth
Ga 1-x Al x It is expressed by a certain formula with the composition x of the As crystal.
That is, y and T can be determined according to x=A・T+B・log(y)+C, (1) A=0.00343, B=0.64, C=−1.82.
さらに、溶質の組成は成長温度に基づいて定
め、溶質の量は成長温度より40−70℃高い温度に
基づいて定めるのが好ましい。 Further, the composition of the solute is preferably determined based on the growth temperature, and the amount of solute is preferably determined based on a temperature 40-70° C. higher than the growth temperature.
[作用]
温度差法によるGa1-xAlxAsの液相成長におい
て見出だされた、(1)式で表される、徐冷法とは異
なる自然法則を利用してメルト組成y,成長温度
Tを決めるため、所望の組成xをもつGa1-xAlx
As結晶を成長できる。[Effect] Melt composition y and growth temperature are determined by utilizing the natural law, which is different from the slow cooling method, and is expressed by equation (1), which was found in the liquid phase growth of Ga 1-x Al x As by the temperature difference method. To determine T, Ga 1-x Al x with the desired composition x
Can grow As crystals.
さらに、成長温度より40−70℃高い温度におけ
るGaAsの飽和溶解度を求め、このGaAsの重量
に相当する上述の[Al]/[GaAs]=yに従う
Alの量を求め、メルトを準備すると連続成長に
適した溶質のソースを含むメルトが作れる。設定
するメルト高温部よりわずかに高温での飽和溶解
度に合わせれば、高温部において溶質が完全には
溶解せず、エピタキシヤル層の成長に伴つて順次
溶解する。 Furthermore, calculate the saturation solubility of GaAs at a temperature 40-70°C higher than the growth temperature, and follow the above-mentioned [Al]/[GaAs] = y, which corresponds to the weight of GaAs.
By determining the amount of Al and preparing the melt, a melt containing a solute source suitable for continuous growth can be created. If the solute is adjusted to the saturation solubility at a temperature slightly higher than the set high temperature part of the melt, the solute will not be completely dissolved in the high temperature part, but will gradually dissolve as the epitaxial layer grows.
[実施例]
第5図に温度差法液相成長装置の例を概略的に
示す。制御装置50はコンピユータを内蔵し、成
長装置全体の制御を行える。入口側予備室51内
には半導体基板を載せたスライダ53が収められ
ており、スライダ押上げ機構55により順次ゲー
トバルブ62を通つて押し上げられる。入口側予
備室51は予備加熱炉59で予熱されているのが
好ましい。押し上げられたスライダはスライダ駆
動機構61により成長室57内にゲートバルブ6
3を通つて送られる。成長室57内にはメルト槽
64が設けられ、主ヒータ67がメルト槽64を
加熱している。スライダ53上の基板69はメル
ト槽64下部でメルトと接触し結晶成長を行う。
結晶成長の終わつた基板を載せたスライダはゲー
トバルブ73を介して成長室57の外に送られ、
スライダ受取機構77によつてゲートバルブ74
を介して出口側予備室79に収められる。各駆動
機構55,61,77やヒータ59,67等は制
御装置50によつて制御できる。制御装置50は
さらに式(1)およびその変形式などを記憶してお
り、必要に応じて、各パラメータの算出、その結
果に基づく操作者への指示表示や自動制御などを
行うことができる。[Example] FIG. 5 schematically shows an example of a temperature difference method liquid phase growth apparatus. The control device 50 has a built-in computer and can control the entire growth apparatus. A slider 53 carrying a semiconductor substrate is housed in the entrance side preliminary chamber 51, and is successively pushed up through the gate valve 62 by the slider pushing up mechanism 55. Preferably, the inlet side preliminary chamber 51 is preheated in a preliminary heating furnace 59. The pushed-up slider is driven into the growth chamber 57 by the gate valve 6 by the slider drive mechanism 61.
Sent through 3. A melt tank 64 is provided in the growth chamber 57, and the main heater 67 heats the melt tank 64. The substrate 69 on the slider 53 comes into contact with the melt at the bottom of the melt tank 64 to cause crystal growth.
The slider carrying the substrate on which crystal growth has been completed is sent out of the growth chamber 57 via the gate valve 73.
Gate valve 74 by slider receiving mechanism 77
It is stored in the outlet side preliminary chamber 79 via the. The drive mechanisms 55, 61, 77, heaters 59, 67, etc. can be controlled by the control device 50. The control device 50 further stores Equation (1) and its modified forms, and can calculate each parameter, display instructions to the operator based on the results, perform automatic control, etc., as necessary.
第6図はメルト槽64部分の1例の拡大説明図
である。溶媒であるGaの中に溶質のAl,GaAs
が溶解されて、pメルト槽65とnメルト槽66
に収容されている。さらに不純物としてpメルト
槽65にはZnがnメルト槽66にはTeが溶解さ
れている。後から成長するn型領域のバンドギヤ
ツプをp型領域のバンドギヤツプより大きくする
ためnメルト槽66のAlの量はpメルト槽65
のAlの量より大きくするのがよい。例えば、赤
色発光のGa1-xAlxAs発光ダイオードをえるには、
AlAsの組成割合xをp型領域で約0.35、n型領
域で約0.6−0.85となるようにAlとGaAsの量を決
める。両メルト槽65,66内には図中右に示す
ような垂直方向の温度差が設定される。たとえ
ば、850℃−950℃の温度で温度差を10℃−60℃設
ける。溶質を連続的に供給するには高温部である
メルト上部に溶質を浮かせておくか溶質収容部を
作つてメルトと接触させてもよい。溶質は高温部
で飽和溶解度まで溶解し、温度勾配と拡散で低温
部に輪送される。通常溶解度は温度と共に増加す
るので、低温部では過飽和溶液となつて析出でき
る状態となる。このようなメルト低温部へ基板を
順次接触させる。たとえば、成長時間約60分で50
−60μmの成長層がえられる。第7図は温度と時
間との関係を示す。図から判るように温度分布は
一定に保たれる。初め1番目の基板がpメルトの
下に接し、p型層を成長させる。次にスライダを
移動させて1番目の基板がnメルトの下に接し、
2番目の基板がpメルトの下に接するようにす
る。そこで、それぞれの成長層を形成する。これ
で1番目の基板上には下にp型層、上にn型層が
成長され、ダイオードが形成される。この様な操
作を繰り返して多数枚の基板上にエピタキシヤル
成長を行う。成長結晶層の組成を光励起スペクト
ル等により、成長システムから基板を出すことな
く、モニタし、結果を制御装置50を介してフイ
ードバツクしてもよい。 FIG. 6 is an enlarged explanatory view of one example of the melt tank 64 portion. Solutes Al and GaAs in the solvent Ga
is melted, and the p melt tank 65 and the n melt tank 66
is housed in. Furthermore, as impurities, Zn is dissolved in the P melt tank 65 and Te is dissolved in the N melt tank 66. In order to make the bandgap of the n-type region that will grow later larger than that of the p-type region, the amount of Al in the n-melt tank 66 is set to be equal to that of the p-melt tank 65.
It is better to make the amount of Al larger than the amount of Al. For example, to obtain a red-emitting Ga 1-x Al x As light-emitting diode,
The amounts of Al and GaAs are determined so that the AlAs composition ratio x is about 0.35 in the p-type region and about 0.6-0.85 in the n-type region. A vertical temperature difference is set in both melt tanks 65 and 66 as shown on the right side of the figure. For example, a temperature difference of 10°C to 60°C is set between 850°C and 950°C. In order to continuously supply the solute, the solute may be floated above the melt, which is a high temperature section, or a solute containing section may be created and brought into contact with the melt. The solute dissolves to saturation solubility in the high temperature zone and is transported to the low temperature zone due to the temperature gradient and diffusion. Since the solubility usually increases with temperature, it becomes a supersaturated solution in a low temperature region and is in a state where it can precipitate. The substrates are sequentially brought into contact with such melt low temperature parts. For example, 50 with a growth time of about 60 minutes
A growth layer of −60 μm is obtained. FIG. 7 shows the relationship between temperature and time. As can be seen from the figure, the temperature distribution remains constant. Initially, the first substrate contacts the bottom of the p-melt and grows a p-type layer. Next, move the slider so that the first board touches the bottom of the n-melt,
The second substrate touches the bottom of the p-melt. Therefore, respective growth layers are formed. In this way, a p-type layer is grown on the bottom and an n-type layer is grown on the top of the first substrate, thereby forming a diode. Such operations are repeated to perform epitaxial growth on a large number of substrates. The composition of the grown crystal layer may be monitored by optical excitation spectra or the like without taking the substrate out of the growth system, and the results may be fed back via the control device 50.
次に、p側n側にそれぞれ電極をつけ、分離裁
断して高輝度Ga1-xAlxAs発光ダイオード(LED)
を得る。 Next, electrodes are attached to the p side and the n side, and separated and cut to create a high brightness Ga 1-x Al x As light emitting diode (LED).
get.
pメルト、nメルトの準備について以下に説明
する。 The preparation of p-melt and n-melt will be explained below.
成長すべきGa1-xAlxAsエピタキシヤル層につ
いて所望の組成xが決まつているものとしてGa
溶媒に溶解するAlとGaAsの重量比[Al]/
[GaAs]=yまたは成長温度T℃(基板結晶の温
度あるいはメルトの低温側の温度)を以下の式か
ら決定する。 Assuming that the desired composition x of the Ga 1-x Al x As epitaxial layer to be grown is determined,
Weight ratio of Al and GaAs dissolved in solvent [Al]/
[GaAs]=y or the growth temperature T° C. (temperature of the substrate crystal or temperature on the low temperature side of the melt) is determined from the following equation.
x=A・T+Blog(y)+C (1)
A=0.00343,B=0.64,C=−1.82
これにより成長温度Tと溶質の重量比yとが定
められる。たとえば、成長温度T=900(℃)の場
合は、
x=0.00343×900+0.64log(y)−1.82
∴y=0.011exp(3.6x)
に従つて、溶質の重量比yを求めればよい。 x=A·T+Blog(y)+C (1) A=0.00343, B=0.64, C=−1.82 This determines the growth temperature T and the solute weight ratio y. For example, when the growth temperature T=900 (° C.), the weight ratio y of the solute can be determined according to x=0.00343×900+0.64log(y)−1.82 ∴y=0.011exp(3.6x).
次ぎに成長温度より40−70℃高い温度、たとえ
ば成長温度より約60℃高い温度におけるAl−Ga
溶液に対するGaAsの溶解度と上に求めた
[Al]/[GaAs]とから[GaAs]/[Ga],
[Al]/[Ga]を決定できる。なお、Ga溶媒に
溶解するAlとGaAsの重量比[Al]/[GaAs]=
yは0.015−0.3が好ましい。 Next, Al-Ga at a temperature 40-70℃ higher than the growth temperature, for example, about 60℃ higher than the growth temperature.
From the solubility of GaAs in the solution and [Al]/[GaAs] obtained above, [GaAs]/[Ga],
[Al]/[Ga] can be determined. In addition, the weight ratio of Al and GaAs dissolved in Ga solvent [Al]/[GaAs] =
y is preferably 0.015-0.3.
一旦作成したメルトから成長させる結晶の組成
xを変更調整する場合は制御装置50を介して成
長温度Tを制御すればよい。 When changing and adjusting the composition x of the crystal grown from the melt once created, the growth temperature T may be controlled via the control device 50.
この結晶成長法の基礎をなすデータを以下に説
明する。第1図がまとめたデータを示す。以下要
素を分けて説明する。 The data underlying this crystal growth method are explained below. Figure 1 shows the compiled data. The following elements will be explained separately.
第8図はメルトに溶解するAlとGaAsとの重量
比[Al]/[GaAs]=yと温度差法液相エピタ
キシヤル成長により成長温度900℃で得られた
Ga1-xAlxAs結晶の組成xとの関係の例を示す実
験データのプロツトである。この関係は次の式に
より近似できる。 Figure 8 shows the weight ratio of Al and GaAs dissolved in the melt [Al]/[GaAs] = y, obtained by temperature difference method liquid phase epitaxial growth at a growth temperature of 900°C.
1 is a plot of experimental data showing an example of the relationship between Ga 1-x Al x As crystal composition x; This relationship can be approximated by the following equation.
x=α・log(y)+β±10% (2)
α=0.64,β=1.27,
0≦x<0.1及び0.85<x≦1.0の範囲では、破
線のようにこの式の関係から外れてくる。しかし
この範囲内であつても,希望する組成xの結晶を
得るのに必要な溶質の重量比[Al]/[GaAs]
=yを予想することは比較的容易である。 x=α・log(y)+β±10% (2) α=0.64, β=1.27, In the range of 0≦x<0.1 and 0.85<x≦1.0, the relationship of this equation deviates as shown by the broken line. . However, even within this range, the solute weight ratio [Al]/[GaAs] necessary to obtain a crystal with the desired composition x
=y is relatively easy to predict.
第9図は第8図の結晶中の組成xを求めるため
に測定されたEPMAのデータで、成長厚み方向
のxの分布を示している。 FIG. 9 shows EPMA data measured to determine the composition x in the crystal shown in FIG. 8, and shows the distribution of x in the growth thickness direction.
第10図はEPMAにより測定したGa1-xAlxAs
結晶の組成xと成長温度T℃(基板結晶の温度あ
るいはメルトの低温部の温度)との関係を示す実
験データプロツトであり、メルトに溶解するAl
とGaAsの重量比[Al]/[GaAs]=yをパラメ
ータとして示したものである。AlとGaAsの重量
比[Al]/[GaAs]=yの各値においてxの成
長温度依存性はほぼ一定であり、これらの関係は
次の式で近似できる。 Figure 10 shows Ga 1-x Al x As measured by EPMA.
This is an experimental data plot showing the relationship between the crystal composition
The weight ratio of GaAs and [Al]/[GaAs]=y is shown as a parameter. The growth temperature dependence of x is almost constant at each value of the weight ratio of Al and GaAs [Al]/[GaAs]=y, and these relationships can be approximated by the following equation.
x=γ・T+δ
γ=0.00343 δ=−2.6〜−2.9
第8図および第10図をまとめて、組成x
(AlAsの割合)をz軸に、成長温度T(℃)をx
軸に、溶質の重量比[Al]/[GaAs]=y軸に
表したのが第1図である。 x=γ・T+δ γ=0.00343 δ=−2.6 to −2.9 Combining Figures 8 and 10, the composition x
(AlAs ratio) is the z-axis, and the growth temperature T (℃) is x
In FIG. 1, the solute weight ratio [Al]/[GaAs] is expressed on the y-axis.
温度差法によるGa1-xAlxAsの液相結晶成長で
は、第1図に示したように、成長結晶の組成xが
成長温度T(℃)と溶質の重量比y=[Al]/
[GaAs]とで決定され、この関係を用いて成長
条件を決めることができる。第1図の関係は、次
式で表すことができる。 In the liquid phase crystal growth of Ga 1-x Al x As by the temperature difference method, as shown in Figure 1, the composition x of the growing crystal is determined by the growth temperature T (°C) and the solute weight ratio y = [Al]/
[GaAs], and growth conditions can be determined using this relationship. The relationship shown in FIG. 1 can be expressed by the following equation.
x=A・T+B・log(y)+C (1)
A=0.00343,B=0.64,C=−1.82
従つて成長温度T(℃)とメルトに溶解される
AlとGaAsの重量比[Al]/[GaAs]=yは希望
するGa1-xAlxAlの組成x(1)とから求めることが
できる。 x=A・T+B・log(y)+C (1) A=0.00343, B=0.64, C=-1.82 Therefore, the growth temperature T (℃) and melting
The weight ratio of Al to GaAs [Al]/[GaAs]=y can be determined from the desired composition x(1) of Ga 1-x Al x Al.
以上、メルトの低温部で行われる結晶成長につ
いて検討した。温度差法によるメルト内には温度
分布が存在する。素材であるAl,GaAsは高温部
で溶解する。 The above discussion has been about crystal growth that takes place in the low-temperature part of the melt. There is a temperature distribution within the melt measured by the temperature difference method. The materials Al and GaAs melt in high temperature areas.
温度差法においては、多数枚の基板上への連続
成長が可能であるから、成長中のメルトは成長素
材(Al,GaAs)が完全に溶解した状態ではな
く、メルトを飽和溶液の状態に保つのに必要な量
に加えて、必要枚数成長させられるだけの量の成
長素材(完全には溶解していない)を含むことが
望ましい。しかしこの余分の成長素材が多すぎる
と、メルトの全体にわたり成長素材が微結晶とし
て存在し、一度溶解した成長素材が微結晶を核と
してその上に析出し、必要な基板上への析出、成
長を妨げることが起こる。このようなことから成
長温度より40−70℃高い温度における溶解度から
溶質の量を定めるのが好ましい。 In the temperature difference method, continuous growth is possible on multiple substrates, so the melt during growth is not in a state in which the growth materials (Al, GaAs) are completely dissolved, but in a saturated solution state. In addition to the amount necessary for this purpose, it is desirable to include a sufficient amount of growth material (not completely dissolved) to grow the required number of sheets. However, if there is too much of this extra growth material, the growth material will exist as microcrystals throughout the melt, and once melted, the growth material will precipitate on the microcrystals as nuclei, causing precipitation and growth on the necessary substrate. It happens that it interferes with. For this reason, it is preferable to determine the amount of solute based on its solubility at a temperature 40-70°C higher than the growth temperature.
たとえば基板の温度が約900℃でありメルトに
10−50℃の温度差がつけられているとして、高温
部分よりわずかに高い温度たとえば、約960℃で
完全に溶解し、これ以下では完全には溶解しない
状態におく、すなわち、成長温度が900℃である
として、メルトに溶解するAlとGaAsの重量比y
=[Al]/[Ga]を希望するGa1-xAlxAs結晶の
組成x(好ましくは0.1≦x≦0.85)と成長温度T
から式(1)を用いて計算にて決定する。次に第3図
において等[Al]/[GaAs]線(破線)と960
℃での[GaAs]/[Ga]対[Al]/[Ga]線
(実線)との交点のy値より[GaAs]/[Ga]
を求める。この[GaAs]/[Ga]と[Al]/
[Ga]およびGaの総量より、溶媒Gaに対する各
材料の量を算出する。このように求めた溶質の量
は、960℃で完全に溶ける。つまり基板の温度が
960℃でメルトに10−50℃の温度差をつけている
から、基板温度(900℃+温度差(50℃)+αの温
度(960℃)では完全に溶解するが、これ以下で
は完全には溶解しない。これによつて溶質のソー
スが確保される。 For example, the temperature of the board is about 900℃, and it melts.
Assuming a temperature difference of 10-50°C, the temperature slightly higher than the high temperature part will completely melt at about 960°C, for example, and it will not completely melt below this temperature, that is, the growth temperature will be 900°C. ℃, weight ratio y of Al and GaAs dissolved in the melt
= [Al]/[Ga] desired Ga 1-x Al x As crystal composition x (preferably 0.1≦x≦0.85) and growth temperature T
It is determined by calculation using formula (1). Next, in Figure 3, the equal [Al]/[GaAs] line (dashed line) and the 960
[GaAs]/[Ga] from the y value of the intersection of [GaAs]/[Ga] vs. [Al]/[Ga] line (solid line) at °C
seek. This [GaAs]/[Ga] and [Al]/
The amount of each material relative to the solvent Ga is calculated from [Ga] and the total amount of Ga. The amount of solute determined in this way will completely dissolve at 960°C. In other words, the temperature of the board is
Since we set a temperature difference of 10-50℃ for the melt at 960℃, it will completely melt at the substrate temperature (900℃ + temperature difference (50℃) + α (960℃), but it will not completely melt below this temperature. Does not dissolve.This ensures a source of solutes.
この方法で得られた各材料(GaAs,Ga,Al)
を含むメルトを用いて約900℃で温度差10−50℃
で結晶成長させると、希望するxから,±約10%
以内の組成xをもつGa1-xAlxAs結晶が得られる。 Materials obtained using this method (GaAs, Ga, Al)
Temperature difference of 10-50℃ at about 900℃ using melt containing
If you grow a crystal with
A Ga 1-x Al x As crystal having a composition x within the following range is obtained.
同一メルトを用いて成長結晶の組成xを修正し
たい場合、制御装置50に現在の組成xと修正後
の組成xとを入力し、修正すべき成長温度の変化
を求め、ヒータを自動調整することもできる。 When it is desired to correct the composition x of the grown crystal using the same melt, the current composition x and the corrected composition x are input to the control device 50, the change in the growth temperature to be corrected is determined, and the heater is automatically adjusted. You can also do it.
[発明の効果]
温度差法においては、成長中の基板付近のメル
トの温度を正確に測定することは容易ではなく、
また温度差をつけるため局部ヒータや冷却気体を
用いるため炉体の温度のみからも成長温度を正確
に求めることは困難である。また成長システムご
とにもバラツキがあり、従つて正確に希望する組
成xに合わせるには、繰り返し[GaAs]/
[Ga]や[Al/GaAs]等を調節しなければなら
なかつた。本発明の方法では±約10%以内で正確
な組成xをもつGa1-xAlxAs結晶が得られる。多
くの時間と労力や高価な材料を節約することがで
き、非常に有用である。[Effect of the invention] In the temperature difference method, it is not easy to accurately measure the temperature of the melt near the growing substrate;
Furthermore, since local heaters and cooling gas are used to create temperature differences, it is difficult to accurately determine the growth temperature from only the temperature of the furnace body. Furthermore, there are variations in each growth system, so to precisely match the desired composition x, it is necessary to repeatedly [GaAs]/
[Ga], [Al/GaAs], etc. had to be adjusted. The method of the present invention yields Ga 1-x Al x As crystals with a precise composition x within ±about 10%. It can save a lot of time and effort and expensive materials, which is very useful.
第1図は本発明による温度差法液相結晶成長で
の各パラメータ間の関係を示すグラフ、第2図は
徐冷法による結晶組成x対メルト中の溶質Al対
Gaの重量比[Al]/[Ga]の関係を示すグラ
フ、第3図はGa−Al溶液におけるGaAsの飽和
溶解度を示すグラフ、第4図は結晶中の組成x対
メルト中のAlとGaの重量比[Al][Ga]の関係
において徐冷法と温度差法とを対比するグラフ、
第5図は温度差法による液相結晶成長装置の概略
図、第6図は第5図の部分拡大図、第7図は成長
操作を説明する温度対時間のグラフ、第8図は温
度差法における組成x対メルト中の[Al]/
[GaAs]重量比のグラフ、第9図はEPMAの測
定データ、第10図は[Al]/[GaAs]重量比
をパラメータとした組成x対成長温度Tの関係を
示すグラフである。
符号の説明、50……コンピユータ内蔵の制御
装置、64,65,66……メルト槽、53……
スライダ、69……基板、1P……1枚目基板上
のp型層、1N……1枚目基板上のn型層、2P
……2枚目基板上のp型層、2N……2枚目基板
上のn型層。
Figure 1 is a graph showing the relationship between each parameter in the temperature difference method liquid phase crystal growth according to the present invention, and Figure 2 is a graph showing the relationship between the crystal composition x and the solute Al in the melt in the slow cooling method.
A graph showing the relationship between the Ga weight ratio [Al]/[Ga]. Figure 3 is a graph showing the saturation solubility of GaAs in a Ga-Al solution. Figure 4 is a graph showing the composition x in the crystal versus Al and Ga in the melt. A graph comparing the slow cooling method and the temperature difference method in relation to the weight ratio [Al][Ga],
Fig. 5 is a schematic diagram of a liquid phase crystal growth apparatus using the temperature difference method, Fig. 6 is a partially enlarged view of Fig. 5, Fig. 7 is a graph of temperature versus time to explain the growth operation, and Fig. 8 is a temperature difference Composition x in the method vs. [Al]/in the melt
FIG. 9 is a graph of the [GaAs] weight ratio, and FIG. 9 is a graph showing EPMA measurement data, and FIG. 10 is a graph showing the relationship between the composition x and the growth temperature T using the [Al]/[GaAs] weight ratio as a parameter. Explanation of symbols, 50... Control device with built-in computer, 64, 65, 66... Melt tank, 53...
Slider, 69...Substrate, 1P...P-type layer on the first substrate, 1N...N-type layer on the first substrate, 2P
...p-type layer on the second substrate, 2N...n-type layer on the second substrate.
Claims (1)
度差をつけ、このメルトの低温部に基板を接触さ
せてGaAlAs結晶を成長させる温度差法による
GaAlAsの液相の結晶成長方法においてGa溶媒
に溶解するAlとGaAsの重量比[Al]/[GaAs]
=yと成長温度T℃とを希望するGa1-xAlxAs結
晶の組成xと x=A・T+B・log(y)+C A=0.00343,B=0.64,C=−1.82 に基づいて決定し、メルトを準備して結晶成長を
行うことを特徴とするGaAlAsの液相の結晶成長
方法。 2 特許請求の範囲第1項記載のGaAlAsの液相
の結晶成長方法において、成長温度Tより40ない
し70℃高い温度におけるAl−Ga溶液に対する
GaAsの溶解度と求めた[Al]/[GaAs]=yと
からGaAsとGaの重量比[GaAs]/[Ga]を決
定し、メルトを準備して結晶成長を行うことを特
徴とするGaAlAsの液相の結晶成長方法。[Claims] 1. A temperature difference method in which a temperature difference is applied to a melt in which Al and GaAs are dissolved in a Ga solvent, and a substrate is brought into contact with the low temperature part of this melt to grow GaAlAs crystals.
Weight ratio of Al and GaAs dissolved in Ga solvent in GaAlAs liquid phase crystal growth method [Al]/[GaAs]
= y and the growth temperature T°C are determined based on the desired composition x of the Ga 1-x Al x As crystal and x = A・T+B・log(y)+C A=0.00343, B=0.64, C=-1.82 A method for growing GaAlAs liquid phase crystals, which is characterized by preparing a melt and performing crystal growth. 2. In the GaAlAs liquid phase crystal growth method according to claim 1, for an Al-Ga solution at a temperature 40 to 70°C higher than the growth temperature T.
The GaAlAs method is characterized by determining the weight ratio [GaAs]/[Ga] of GaAs and Ga from the solubility of GaAs and the determined [Al]/[GaAs]=y, preparing a melt, and performing crystal growth. Liquid phase crystal growth method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP76488A JPH01179794A (en) | 1988-01-07 | 1988-01-07 | Liquid phase growth method for crystal of ga-al-as |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP76488A JPH01179794A (en) | 1988-01-07 | 1988-01-07 | Liquid phase growth method for crystal of ga-al-as |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01179794A JPH01179794A (en) | 1989-07-17 |
| JPH0477717B2 true JPH0477717B2 (en) | 1992-12-09 |
Family
ID=11482763
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP76488A Granted JPH01179794A (en) | 1988-01-07 | 1988-01-07 | Liquid phase growth method for crystal of ga-al-as |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01179794A (en) |
-
1988
- 1988-01-07 JP JP76488A patent/JPH01179794A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01179794A (en) | 1989-07-17 |
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