JPH06291068A - Liquid phase epitaxial growth method - Google Patents
Liquid phase epitaxial growth methodInfo
- Publication number
- JPH06291068A JPH06291068A JP9665693A JP9665693A JPH06291068A JP H06291068 A JPH06291068 A JP H06291068A JP 9665693 A JP9665693 A JP 9665693A JP 9665693 A JP9665693 A JP 9665693A JP H06291068 A JPH06291068 A JP H06291068A
- Authority
- JP
- Japan
- Prior art keywords
- substrate
- growth
- melt
- slider
- crystal
- 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
Links
- 238000000034 method Methods 0.000 title claims description 17
- 239000007791 liquid phase Substances 0.000 title claims description 10
- 239000000758 substrate Substances 0.000 claims abstract description 39
- 239000013078 crystal Substances 0.000 claims abstract description 24
- 230000008021 deposition Effects 0.000 claims abstract description 8
- 239000000155 melt Substances 0.000 description 23
- 239000010410 layer Substances 0.000 description 21
- 239000000203 mixture Substances 0.000 description 6
- 238000001556 precipitation Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 229910001218 Gallium arsenide Inorganic materials 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 229910002804 graphite Inorganic materials 0.000 description 4
- 239000010439 graphite Substances 0.000 description 4
- 230000002159 abnormal effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000013081 microcrystal Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
Landscapes
- Led Devices (AREA)
- Liquid Deposition Of Substances Of Which Semiconductor Devices Are Composed (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、発光ダイオ−ド及び半
導体レ−ザ等の液相エピタキシャル層形成のための液相
エピタキシャル成長方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a liquid phase epitaxial growth method for forming a liquid phase epitaxial layer such as a light emitting diode and a semiconductor laser.
【0002】[0002]
【従来の技術】図2は、従来一般に使用されている液相
エピタキシャル成長を行わせるためのスライデングボ−
トの一例を示す概略断面図である。1は溶液収容体、2
は各収容部3に収容されたメルト(溶液)、4は矢印方
向に移動可能なスライダ、5は結晶成長用の均一な厚さ
の基板6を収容した凹部である。この成長方法は、80
0℃で高温保持後、0.2 ℃/minの冷却速度で平衡冷
却を行いながらスライダ4を結晶成長基板6と各溶液と
対応する位置に移動させて成長を行わせるようにしてい
るものである。ところが、このような方法で行う場合、
幾層かの成長過程で、全体的に不均一な成長層が出来上
がってしまう。特に、基板端部が厚く成長してしまう傾
向にあり、結晶層の成長過程や成長基板の加工時に種々
の弊害をもたらしてしまうものであった。2. Description of the Related Art FIG. 2 shows a sliding board for carrying out liquid phase epitaxial growth which is generally used in the past.
It is a schematic sectional drawing which shows an example of G. 1 is a solution container, 2
Is a melt (solution) contained in each container 3, 4 is a slider movable in the arrow direction, and 5 is a recess containing a substrate 6 of uniform thickness for crystal growth. This growth method is 80
After being kept at a high temperature of 0 ° C., the slider 4 is moved to a position corresponding to the crystal growth substrate 6 and each solution while performing equilibrium cooling at a cooling rate of 0.2 ° C./min so that growth is performed. However, when using this method,
In the growth process of several layers, an entirely non-uniform growth layer is formed. In particular, the edges of the substrate tend to grow thick, which causes various adverse effects during the growth process of the crystal layer and the processing of the growth substrate.
【0003】これを是正するために、基板6を図3
(A)に示すように厚く成長してしまう箇所に、予め段
部6aを形成したり、図3(B)に示すように傾斜部6
bを形成して、成長層の表面を平面状にするようにした
ものがある。図4(A)は、図3(A)に示した形状の
基板6によって成長を行わせた時のの成長結果を示す
図、図4(B)は図3(B)に対応した図面である。To correct this, the substrate 6 is shown in FIG.
As shown in FIG. 3A, a step portion 6a is formed in advance at a location where it grows thick, or as shown in FIG.
There is one in which b is formed so that the surface of the growth layer becomes flat. FIG. 4A is a diagram showing a growth result when growing the substrate 6 having the shape shown in FIG. 3A, and FIG. 4B is a diagram corresponding to FIG. 3B. is there.
【0004】[0004]
【発明が解決しようとする課題】ところが、前記図3
(A),図3(B)に示す形状の基板6を用いても、そ
れらの段部6aや傾斜部6bに溶液が残り、この上面に
成長を行わせる溶液と混ざってしまい、この周辺部分の
結晶組成が混在してしまう。また、スライダ4を摺動さ
せる際、溶液中で形成された微結晶がスライドの際、そ
の一部が基板上に到着して溶液残りが生じてしまうとい
う問題点がある。そこで、本発明はこのような問題点を
除去した液相エピタキシャル成長方法を提供することに
ある。However, in the case of FIG.
Even if the substrate 6 having the shape shown in FIGS. 3A and 3B is used, the solution remains on the stepped portion 6a and the inclined portion 6b and is mixed with the solution for growing on the upper surface, and the peripheral portion The crystal compositions of the above are mixed. In addition, when the slider 4 is slid, when the fine crystals formed in the solution slide, a part of the fine crystals arrives on the substrate, and the solution remains. Therefore, the present invention is to provide a liquid phase epitaxial growth method that eliminates such problems.
【0005】[0005]
【課題を解決するための手段】本発明は前記問題点に鑑
みてなされたものであり、以下の方法を提供しようとい
うものである。即ち、結晶成長用溶液をスライディング
ボ−トを用いて基板上に成長させる液相エピタキシャル
成長方法において、前記結晶成長用溶液を前記基板上に
80%以上の析出効率の厚さで成長を行わせるようにし
たことを特徴とする液相エピタキシャル成長方法。The present invention has been made in view of the above problems, and it is an object of the present invention to provide the following method. That is, in a liquid phase epitaxial growth method in which a crystal growth solution is grown on a substrate by using a sliding boat, the crystal growth solution is grown on the substrate with a thickness of precipitation efficiency of 80% or more. A liquid phase epitaxial growth method characterized in that
【0006】[0006]
【実施例】以下、図面を参照して、本発明の一実施例に
つき説明する。図1(A)〜(E)はスライデングボ−
トによってダブルヘテロ構造GaAlAs赤外発光ダイ
オ−ド用結晶を得るための工程図である。スライデング
ボ−トは、グラファイト製で、第1スライダ11、第2
スライダ12及び固定板13から成る3層構造である。
固定板13には基板結晶を固定するための凹部24が穿
たれ、その深さは0.8mmとされており、その底部には
基板25が収納されるようになっている。固定板13上
には摺動可能に前記第2スライダ12が設けられ、メル
ト(溶液)落下用の細い垂直通路20a,20b,20
cと、これの直角方向に連通する溜部21a,21b,
21cとが、ちょうど断面L字形状を呈するようにそれ
ぞれ3箇所設けられている。これら溜部21a,21
b,21cの高さは、それぞれ3mm、1mm及び3m
mとされ、ここに溜められる成長メルトを基板25上に
80%以上の析出効率で成長を行わせるようにするため
の高さとしてある。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. 1 (A) to 1 (E) are sliding board.
FIG. 3 is a process diagram for obtaining a crystal for a double heterostructure GaAlAs infrared light emitting diode according to the present invention. The sliding boat is made of graphite and has a first slider 11 and a second slider.
It has a three-layer structure including a slider 12 and a fixing plate 13.
The fixing plate 13 is provided with a recess 24 for fixing the substrate crystal, the depth thereof is 0.8 mm, and the substrate 25 is accommodated at the bottom thereof. The second slider 12 is slidably provided on the fixed plate 13, and thin vertical passages 20a, 20b, 20 for dropping the melt (solution) are provided.
c and the reservoirs 21a, 21b, which communicate with each other in the direction perpendicular to this
21c and 3c are respectively provided at three positions so as to have an L-shaped cross section. These reservoirs 21a, 21
The heights of b and 21c are 3 mm, 1 mm and 3 m, respectively.
The height is set to m so that the growth melt accumulated here can be grown on the substrate 25 at a deposition efficiency of 80% or more.
【0007】そして、第2スライダ12の上面側には、
この第2スライダ12と摺動可能なように第1スライダ
11が設けられ、Ga,多結晶GaAs,Al及びド−
パントを収納するためのメルト溜14,15,16が夫
々設けられ、これらの形状は成長時に余剰な多結晶が各
溜部21a,21b,21c内の成長メルトに落下しな
いようにロ−ト状に絞り込まれた形状となっている。Then, on the upper surface side of the second slider 12,
A first slider 11 is provided so as to be slidable with respect to the second slider 12, and Ga, polycrystalline GaAs, Al and a drain are provided.
Melt reservoirs 14, 15 and 16 for accommodating the punts are provided respectively, and these shapes are funnel-shaped so that excess polycrystal does not drop into the growth melt in the reservoirs 21a, 21b and 21c during growth. The shape is narrowed down to.
【0008】このような構成のスライデングボ−トによ
って、例えば、nクラッド層 Ga0.3 Al0.7 As/
P活性層Ga0.97Al0.03As/Pクラッド層Ga0.3
Al0.7 Asの成長を行なわせる工程につき、以下図面
にしたがって説明する。成長厚は、発光効率を上げるた
めに基板除去を行う必要があるので、厚く成長させるこ
とが要求される。しかし、無限に成長厚を厚くできな
い。成長層の厚さは、加工に耐える強度があればよく、
その全厚が120μm程度あれば耐えられることが経験
的に分かっているので、この厚さを得るように成長を行
わせればよいことになる。従って、このことを考慮して
成長を行わせる必要がある。With the sliding boat having such a structure, for example, the n-clad layer Ga 0.3 Al 0.7 As /
P active layer Ga 0.97 Al 0.03 As / P clad layer Ga 0.3
The process of growing Al 0.7 As will be described below with reference to the drawings. The growth thickness is required to be thick because it is necessary to remove the substrate in order to increase the luminous efficiency. However, the growth thickness cannot be increased infinitely. The thickness of the growth layer should be strong enough to withstand processing,
Since it has been empirically known that the total thickness of about 120 μm can be endured, it suffices to carry out the growth so as to obtain this thickness. Therefore, it is necessary to grow in consideration of this fact.
【0009】第1スライダ11のメルト溜14,15,
16には、Alの混晶比がそれぞれ0.7 、0.03及び0.7
となるように入れ、メルト溜14,15には所定のP型
キャリア濃度が、メルト溜16には所定のN型キャリア
濃度が得られるように適当量のZn,Teを入れる。そ
して、凹部24に300μm厚のP型GaAs基板25
をセットする。このようにセットしたボ−トを図示しな
い反応管に導入する。真空引きしてからH2 還元雰囲気
ガスを31/min流量で流す。次に900℃まで昇温
後、2時間均熱保持する(図1(A))。The melt reservoirs 14, 15 of the first slider 11
No. 16 has Al mixed crystal ratios of 0.7, 0.03 and 0.7, respectively.
The melt reservoirs 14 and 15 are filled with a predetermined P-type carrier concentration, and the melt reservoir 16 is filled with an appropriate amount of Zn and Te so as to obtain a predetermined N-type carrier concentration. Then, a P-type GaAs substrate 25 having a thickness of 300 μm is formed in the recess 24.
Set. The boat thus set is introduced into a reaction tube (not shown). After vacuuming, H 2 reducing atmosphere gas is flowed at a flow rate of 31 / min. Next, after the temperature is raised to 900 ° C., the temperature is kept uniform for 2 hours (FIG. 1 (A)).
【0010】第2スライダ12の通路20aに第1スラ
イダ11のメルト溜14のメルト孔を重ね溜部21aに
メルト17を流し込む。更に第1スライダ11を図1
(A)上右方に引き、メルト溜14に入ったメルト17
と切り離す。この時、メルト溜15,16のメルト孔が
垂直通路20b,20cと対向しないようにする(図1
(B))。The melt holes of the melt reservoir 14 of the first slider 11 are overlapped with the passages 20a of the second slider 12 and the melt 17 is poured into the reservoir 21a. Further, the first slider 11 is shown in FIG.
(A) Melt 17 drawn in the melt reservoir 14 by pulling to the upper right
And disconnect. At this time, the melt holes of the melt reservoirs 15 and 16 are prevented from facing the vertical passages 20b and 20c (see FIG. 1).
(B)).
【0011】3〜5℃降下させた後、第1,2スライダ
共もに図面上左方向に移動し、溜部21a内の成長メル
ト17を基板25上に乗せる(図1(C))。After the temperature is lowered by 3 to 5 ° C., both the first and second sliders move to the left in the drawing, and the growth melt 17 in the reservoir 21a is placed on the substrate 25 (FIG. 1C).
【0012】冷却速度0.1℃/minで800℃まで
冷却し、第1層目の成長を行なわせる。第1スライダ1
1を右方向に移動し、メルト溜15,16を第2スライ
ダ12の垂直通路20b,20c上に重ねメルト18,
19を溜部21b,21cに流す。そして、更に第1ス
ライダ11を右方向に移動して溜部21b,21cに入
ったメルト18,19とそれぞれ切り離す(図1
(D))。The first layer is grown by cooling to 800 ° C. at a cooling rate of 0.1 ° C./min. First slider 1
1 is moved to the right, and the melt reservoirs 15 and 16 are overlapped on the vertical passages 20b and 20c of the second slider 12 to melt 18,
19 is poured into the reservoirs 21b and 21c. Then, the first slider 11 is further moved to the right to separate from the melts 18 and 19 contained in the reservoirs 21b and 21c, respectively (see FIG. 1).
(D)).
【0013】この後、第1,2スライダとを一体的に左
方向に移動し、メルト18,19を順次基板25上に移
動させ、第2,3層の成長を行わせる。750℃になっ
たら、更に第1,2スライダとを左方向に移動し、基板
25上からメルトを除去し室温まで冷やす(図1
(E))。After that, the first and second sliders are integrally moved to the left, and the melts 18 and 19 are sequentially moved onto the substrate 25 to grow the second and third layers. When the temperature reaches 750 ° C., the first and second sliders are further moved to the left to remove the melt from the substrate 25 and cool it to room temperature (see FIG. 1).
(E)).
【0014】このようにして、成長した表面層にはメル
ト残りは全くなく組成均一な良好な結晶層が得られた。
また、Pクラッド層、P活性層及びnクラッド層の厚さ
は、夫々125μm、o.2 μm及び10μmであった。
基板端部の成長厚は、250μmと厚くなったが基板凹
部24が0.8 mmと深く、第2スライダ12が摺動の
際、端部の異常成長部にぶつかったり、その破片が基板
上に残ったり、或は、成長層をキズつけたりするような
ことはない。また、基板凹部24が深くてメルトが成長
面全体に残ったりもしない。これは、前述したように溜
部21a,21b,21cの高を、それぞれ3mm、1
mm及び3mmとし、成長メルトを基板25上に80%
以上の析出効率で成長するようにしたためである。In this way, a good crystal layer having a uniform composition with no melt residue on the grown surface layer was obtained.
The thicknesses of the P-clad layer, P-active layer and n-clad layer were 125 μm, 0.2 μm and 10 μm, respectively.
The growth thickness of the edge portion of the substrate is as thick as 250 μm, but the recessed portion 24 of the substrate is as deep as 0.8 mm, and when the second slider 12 slides, it hits an abnormal growth portion of the edge portion, or fragments thereof remain on the substrate. Or, the growth layer is not scratched. Further, the substrate recess 24 is deep and the melt does not remain on the entire growth surface. This is because the heights of the reservoirs 21a, 21b, 21c are 3 mm and 1 mm, respectively, as described above.
mm and 3 mm, and the growth melt is 80% on the substrate 25.
This is because the growth is performed with the above precipitation efficiency.
【0015】このことにつき更に詳しく説明する。析出
効率は、成長メルトに溶けている溶質が結晶化に寄与し
た割合を示し、この関係は次式で示される。 η=S・ρ0 ・d0 /ρ1 ・d1 このとき、η :析出効率 S :溶解度 ρ0 :溶媒の密度 ρ1 :結晶の密度 d0 :結晶厚 d1 :成長メルト厚This will be described in more detail. The precipitation efficiency indicates the ratio of the solute dissolved in the growth melt to crystallization, and this relationship is expressed by the following equation. η = S · ρ 0 · d 0 / ρ 1 · d 1 where η: precipitation efficiency S: solubility ρ 0 : solvent density ρ 1 : crystal density d 0 : crystal thickness d 1 : growth melt thickness
【0016】この関係式より、成長メルト厚が厚くなる
にしたがって析出効率は低くなってくることが分る。こ
れは、成長メルト厚が厚くなると、同じだけ温度を冷却
したとき過飽和度が大きくなるので、基板と対向したグ
ラファイト上での析出もしやすくなるためである。いっ
たん成長が始まると、最初に成長した微結晶が核とな
り、次々と成長し大きくなっていく。基板上でのメルト
残りは、グラファイトとこの微結晶との結合が弱いの
で、スライダを移動した時の振動やメルトの抵抗でその
一部が成長メルト中に落下して基板上に到着し、そのま
ま留まってしまうために起こると考えられる。これを防
止するためには、グラファイト上に析出する微結晶の成
長を抑えること、即ち、析出効率を向上させることが必
要になる。From this relational expression, it can be seen that the deposition efficiency decreases as the growth melt thickness increases. This is because as the thickness of the growth melt increases, the degree of supersaturation increases when the temperature is cooled by the same amount, so that precipitation on the graphite facing the substrate also easily occurs. Once the growth begins, the first grown crystallites become nuclei and grow and grow one after another. In the remaining melt on the substrate, the bond between graphite and this microcrystal is weak, so part of it drops into the growth melt and arrives on the substrate due to vibration and resistance of the melt when the slider is moved. It is thought to occur because it stays. In order to prevent this, it is necessary to suppress the growth of fine crystals deposited on graphite, that is, to improve the deposition efficiency.
【0017】このようなことから、メルト厚を薄くして
析出効率を80%以上に向上させると、基板上でのメル
ト残りは全くなく、基板上の完全なメルト残り除去のた
めには最低限80%の析出効率が必要であることが確認
されている。各組成成長メルトによりメルト厚を変える
のは、各組成によってAsの溶解度が異なるので過飽和
度が異なるためである。即ち、活性層では組成がほとん
どGaAsに近く過飽和度が大きいので、メルト厚を薄
くする必要があるために薄くなっている。過飽和度が大
きいメルトからの成長では、メルト厚を薄くしていけば
高い析出効率の成長が可能となり、メルト残りの無い安
定した組成の結晶層を得ることができる言える。尚、本
実施例では、GaAs系の成長方法の具体例で説明した
が、InP系にも適用できることは言うまでもない。From the above, when the melt thickness is reduced to improve the deposition efficiency to 80% or more, there is no melt residue on the substrate, and the minimum amount is required for complete removal of the melt residue on the substrate. It has been confirmed that a deposition efficiency of 80% is required. The reason why the melt thickness is changed depending on the composition growth melt is that the solubility of As is different depending on the composition, and thus the degree of supersaturation is different. That is, since the composition of the active layer is close to that of GaAs and the degree of supersaturation is large, it is necessary to reduce the thickness of the melt, so that the thickness is reduced. In the case of growth from a melt having a high degree of supersaturation, it can be said that if the melt thickness is made thin, growth with high precipitation efficiency becomes possible and a crystal layer having a stable composition with no melt residue can be obtained. In the present embodiment, a specific example of the GaAs-based growth method has been described, but it goes without saying that it can also be applied to the InP-based growth method.
【0018】[0018]
【発明の効果】本発明によれば、基板上に残る結晶成長
用溶液を完全に除去し得、均一成長層の結晶を得ること
ができる。また、基板端部に異常な成長ができず、複雑
な加工が不要となる等の効果を奏する。According to the present invention, the solution for crystal growth remaining on the substrate can be completely removed, and crystals of a uniform growth layer can be obtained. Further, there is an effect that abnormal growth cannot be performed at the end portion of the substrate, and complicated processing is unnecessary.
【図1】スライデングボ−トによってダブルヘテロ構造
GaAlAs赤外発光ダイオ−ド用結晶を得るための工
程図である。FIG. 1 is a process drawing for obtaining a crystal for a double heterostructure GaAlAs infrared light emitting diode by a sliding boat.
【図2】従来の液相エピタキシャル成長を行わせるため
のスライデングボ−トの一例を示す概略断面図である。FIG. 2 is a schematic sectional view showing an example of a sliding boat for performing conventional liquid phase epitaxial growth.
【図3】従来の方法に用いられる基板の形状を示す図で
ある。FIG. 3 is a diagram showing a shape of a substrate used in a conventional method.
【図4】図3に示した基板を用いた時の成長層を示した
対応図である。FIG. 4 is a corresponding diagram showing a growth layer when the substrate shown in FIG. 3 is used.
11 第1スライダ 12 第2スライダ 13 固定板 14,15,16 メルト溜 17,18,19 メルト(溶液) 20a,20b,20c 垂直通路 21a,21b,21c 溜部 24 凹部 25 基板 11 First Slider 12 Second Slider 13 Fixing Plate 14, 15, 16 Melt Reservoir 17, 18, 19 Melt (Solution) 20a, 20b, 20c Vertical Passage 21a, 21b, 21c Reservoir 24 Concave 25 Substrate
Claims (1)
を用いて基板上に成長させる液相エピタキシャル成長方
法において、 前記結晶成長用溶液を前記基板上に80%以上の析出効
率の厚さで成長を行わせるようにしたことを特徴とする
液相エピタキシャル成長方法。1. A liquid phase epitaxial growth method in which a crystal growth solution is grown on a substrate using a sliding boat, wherein the crystal growth solution is grown on the substrate at a thickness with a deposition efficiency of 80% or more. A liquid phase epitaxial growth method characterized in that it is performed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9665693A JPH06291068A (en) | 1993-03-31 | 1993-03-31 | Liquid phase epitaxial growth method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9665693A JPH06291068A (en) | 1993-03-31 | 1993-03-31 | Liquid phase epitaxial growth method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH06291068A true JPH06291068A (en) | 1994-10-18 |
Family
ID=14170884
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9665693A Pending JPH06291068A (en) | 1993-03-31 | 1993-03-31 | Liquid phase epitaxial growth method |
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| Country | Link |
|---|---|
| JP (1) | JPH06291068A (en) |
-
1993
- 1993-03-31 JP JP9665693A patent/JPH06291068A/en active Pending
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