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JPH0428678B2 - - Google Patents
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JPH0428678B2 - - Google Patents

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Publication number
JPH0428678B2
JPH0428678B2 JP58157626A JP15762683A JPH0428678B2 JP H0428678 B2 JPH0428678 B2 JP H0428678B2 JP 58157626 A JP58157626 A JP 58157626A JP 15762683 A JP15762683 A JP 15762683A JP H0428678 B2 JPH0428678 B2 JP H0428678B2
Authority
JP
Japan
Prior art keywords
crystal
growth
raw material
crystal growth
tank
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 - Lifetime
Application number
JP58157626A
Other languages
Japanese (ja)
Other versions
JPS6051695A (en
Inventor
Toshio Sagawa
Tsunehiro Unno
Shoji Kuma
Junkichi Nakagawa
Yoshiharu Takahashi
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 JP15762683A priority Critical patent/JPS6051695A/en
Publication of JPS6051695A publication Critical patent/JPS6051695A/en
Publication of JPH0428678B2 publication Critical patent/JPH0428678B2/ja
Granted legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-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
    • C30B19/00Liquid-phase epitaxial-layer growth
    • C30B19/06Reaction chambers; Boats for supporting the melt; Substrate holders
    • C30B19/062Vertical dipping system

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

【発明の詳細な説明】[Detailed description of the invention]

[発明の背景と目的] 本発明は液相エピタキシヤル結晶成長装置に係
り、特に浸漬法による連続液相エピタキシヤル結
晶成長装置の改良に関するものである。 従来の液相エピタキシヤル結晶成長方法は、第
1図に示すスライドボード法による液相結晶成長
方法のように、結晶成長炉1を加熱ヒータ2で加
熱し、結晶成長炉1内にはガス流入口3から不活
性ガスを導入し、ガス流出口4から排出させて、
結晶成長炉1内の溶液槽5内の半導体成分の飽和
成長用溶液6内に基板7を浸漬した後、成長用溶
液6の温度を徐冷することにより基板7上に過飽
和の半導体成分を晶出させる方法であつた。な
お、8は熱電対である。したがつて、基板7上の
液相成長層の厚さ方向では成長温度が徐々に変化
するため、不純物あるいは原子の偏析係数が変化
して均一な特性を有する結晶成長層ができないと
いう欠点があつた。また、一回の結晶成長により
結晶成長できるエピタキシヤル基板の枚数は1枚
程度であり、さらに結晶成長は昇温→徐冷→降温
→サンプル取り出しなどといつた操作が必要であ
り、極めて煩雑な温度プロセスおよび操作が必要
であり、また、一回あたりの時間が非常に長く、
量産化が困難であるという欠点があつた。 なお、量産性を向上させるため、複数個並べた
結晶成長容器内の成長用溶液に、移動可能な軸に
取り付けた基板を順次浸漬して、多層結晶を成長
させる方法が提案されている(特開昭50−39875
号公報)。この方法では、成長用溶液に原料結晶
が存在していたのでは、微小な原料結晶が基板表
面に付着したり、成長した層の厚さのバラツキが
大きいなど良好なエピタキシヤル成長はできない
ため、原料結晶を完全に溶解させておかなければ
ならない。しかし、成長用溶液に入れた原料結晶
や原料結晶と混晶を形成する混晶用原料を全て溶
解させてしまう方法では、これら原料を極めて正
確に秤量することが困難なために、同一の温度で
同一の飽和度及び混晶比を成長毎に再現すること
は不可能であり、同じ結晶成長容器で得られるエ
ピタキシヤル成長層の膜厚及び混晶比を各成長毎
に同じにすることは不可能である。また、成長に
より析出した結晶の量と同じ量の結晶を原料溶液
へ補充することは不可能であるため、この方法で
は、一回の成長毎に原料溶液を交換しなければな
らなかつた。 本発明は上記に鑑みなされたもので、その目的
とするところは、連続して所望の膜厚及び所望の
混晶比を有する成長層を再現性よく短時間で大量
に得ることができ、更に成長溶液に原料を補充し
たり或いは成長用溶液を一回の成長毎に交換した
りする必要のない量産性に優れた液相エピタキシ
ヤル成長装置を提供することにある。 [発明の概要] 本発明の特徴は、不活性ガス置換を行う第1の
ガス置換室と、該第1のガス置換室の後段に順次
直列に配置された複数の結晶成長炉と、該結晶成
長炉内に加熱する加熱ヒータと、前記結晶成長炉
に置かれた成長用溶液を収容するための結晶成長
容器と、前記結晶成長炉の後段に設けられた第2
のガス置換室と、基板を取り付けた基板ケースを
前記第1のガス置換室から前記第2のガス置換室
まで搬送する手段とを備え、前記結晶成長容器
は、前記基板ケースが前記成長用溶液中に浸漬さ
れる結晶成長槽と、前記結晶成長槽と連通して前
記原料溶液が満たされかつ原料結晶及び該原料結
晶との組合わせにより混晶結晶を形成する混晶用
原料をそれぞれ収容するための原料結晶溶解槽及
び混晶用原料溶解槽と、前記原料結晶溶解槽を加
熱して前記原料結晶を溶解し前記成長用溶液の飽
和度を調節する第1ヒータと、前記混晶原料溶解
槽を加熱して前記混晶用原料を溶解し前記成長用
溶液から得られる混晶結晶の混晶比を調節する第
2ヒータとを備えていることにある。 [実施例] 以下本発明を第2図、第3図に示した実施例お
よび第4図、第5図を用いて詳細に説明する。 第2図は本発明の装置の一実施例を示す正面図
で、第3図は第2図の各結晶成長容器の一実施例
を示す縦断面図である。第2図において、9a,
9bはそれぞれガス流入口10a,10b、ガス
流出口11a,11bを有するガス置換室で、ガ
ス置換室9aには基板搬入口12a、基板搬出口
12bがある。13a,13b,13cはそれぞ
れガス流入口14a,14b,14cガス流出口
15a,15b,15cを設けてある結晶成長炉
で、結晶成長炉13a,13b,13cはそれぞ
れ加熱ヒータ16a,16b,16cで加熱でき
るようになつている。 結晶成長炉13a,13b,13c内にはそれ
ぞれ結晶成長容器17a,17b,17cが収納
してあり、これらの結晶成長容器17a〜17c
(17で示す)は、第3図に示すように構成して
ある。第3図において、18は結晶成長槽、19
は原料結晶溶解槽、20は混晶用原料溶解槽で、
原料結晶溶解槽19と混晶用原料溶解槽20とは
それぞれ図示のように結晶成長槽18と連通させ
て、各槽内に成長用溶液を満たすようにしてあ
る。21は原料結晶溶解加熱ヒータ(第1ヒー
タ)、22は混晶用原料溶解槽加熱ヒータ(第2
ヒータ)であり、後述するようにそれぞれ独立し
て温度制御可能である。 なお、結晶成長容器17aと17bとの間には
仕切り23があり、結晶成長容器17bと17c
との間には仕切り24がある。25はガス流入口
26、ガス流出口27を有するガス置換室で、2
8は基板搬出口である。 結晶成長炉13a〜13bは第2図に示すよう
に直列に多段に配列してあり、基板29は基板ケ
ース30に設置してあり、基板搬送架線31によ
つてガス置換室9aの基板搬入口12aよりガス
置換室9a内に搬入され、ガス置換室9a,9b
を通過後、結晶成長炉13a,13b,13cを
通過し、ガス置換室25を通過後基板搬出口28
より取り出される。 この場合、結晶成長炉13a〜13cはそれぞ
れ加熱ヒータ16a〜16cで加熱されて、第4
図に示すように、それぞれ目的に合つた温度プロ
フアイルを持つている。 結晶成長容器17a〜17cは、よく洗滌した
長さ20cm、高さ8cmの良質のグラフアイトボート
よりなり、結晶成長槽18は幅8cm、原料結晶溶
解槽19は幅5cm、混晶用原料溶解槽20は幅4
cmの大きさとなつている。 第1表は各結晶成長容器17a〜17cの結晶
成長槽18、混晶結晶溶解槽19、混晶用原料溶
解槽20の温度と上記各槽内の溶質を表に示した
ものである。
BACKGROUND AND OBJECTS OF THE INVENTION The present invention relates to a liquid phase epitaxial crystal growth apparatus, and particularly to an improvement of a continuous liquid phase epitaxial crystal growth apparatus using an immersion method. In the conventional liquid phase epitaxial crystal growth method, as in the liquid phase crystal growth method using the slide board method shown in FIG. Inert gas is introduced from the inlet 3 and discharged from the gas outlet 4,
After the substrate 7 is immersed in the solution 6 for saturated growth of semiconductor components in the solution tank 5 in the crystal growth furnace 1, the temperature of the growth solution 6 is gradually cooled to crystallize the supersaturated semiconductor component on the substrate 7. It was a way to get him to come out. Note that 8 is a thermocouple. Therefore, since the growth temperature gradually changes in the thickness direction of the liquid phase grown layer on the substrate 7, there is a drawback that the segregation coefficient of impurities or atoms changes, making it impossible to form a crystal grown layer with uniform characteristics. Ta. In addition, the number of epitaxial substrates that can be grown in one crystal growth process is about one, and crystal growth requires operations such as heating → slow cooling → cooling → sample removal, which is extremely complicated. Temperature processes and operations are required, and the time per process is very long.
The drawback was that mass production was difficult. In order to improve mass productivity, a method has been proposed in which multilayer crystals are grown by sequentially immersing substrates attached to a movable shaft into a growth solution in a plurality of crystal growth containers arranged side by side. Kaisho 50-39875
Publication No.). In this method, if raw material crystals are present in the growth solution, good epitaxial growth cannot be achieved, such as fine raw material crystals adhering to the substrate surface or large variations in the thickness of the grown layer. The raw material crystals must be completely dissolved. However, with the method of dissolving all the raw material crystals added to the growth solution and the raw materials for the mixed crystal that form a mixed crystal with the raw material crystals, it is difficult to weigh these raw materials extremely accurately, so It is impossible to reproduce the same saturation and mixed crystal ratio for each growth, and it is impossible to make the thickness and mixed crystal ratio of the epitaxial growth layer the same for each growth in the same crystal growth container. It's impossible. Furthermore, since it is impossible to replenish the raw material solution with the same amount of crystals as the amount of crystals precipitated by growth, this method requires replacing the raw material solution after each growth. The present invention has been made in view of the above, and its purpose is to be able to continuously obtain a large amount of grown layers having a desired film thickness and a desired mixed crystal ratio in a short period of time with good reproducibility; It is an object of the present invention to provide a liquid phase epitaxial growth apparatus which is excellent in mass productivity and does not require replenishing raw materials to a growth solution or replacing a growth solution for each growth. [Summary of the Invention] The present invention is characterized by a first gas replacement chamber that performs inert gas replacement, a plurality of crystal growth furnaces sequentially arranged in series after the first gas replacement chamber, and a crystal growth furnace that performs inert gas replacement. A heater for heating the inside of the growth furnace, a crystal growth container for accommodating a growth solution placed in the crystal growth furnace, and a second crystal growth container provided at the rear stage of the crystal growth furnace.
a gas exchange chamber, and means for transporting a substrate case with a substrate attached thereto from the first gas exchange chamber to the second gas exchange chamber, and the crystal growth container includes a gas exchange chamber in which the substrate case is attached to the growth solution. A crystal growth tank immersed therein communicates with the crystal growth tank and is filled with the raw material solution and accommodates a raw material crystal and a raw material for a mixed crystal that forms a mixed crystal crystal in combination with the raw material crystal. a first heater that heats the raw material crystal dissolving tank to melt the raw material crystals and adjust the degree of saturation of the growth solution; and a second heater that heats the tank to dissolve the mixed crystal raw material and adjust the mixed crystal ratio of the mixed crystal obtained from the growth solution. [Example] The present invention will be described in detail below with reference to the embodiment shown in FIGS. 2 and 3, and FIGS. 4 and 5. FIG. 2 is a front view showing an embodiment of the apparatus of the present invention, and FIG. 3 is a longitudinal sectional view showing an embodiment of each crystal growth container shown in FIG. In FIG. 2, 9a,
Reference numeral 9b denotes a gas exchange chamber having gas inlets 10a, 10b and gas outlets 11a, 11b, respectively.The gas exchange chamber 9a has a substrate loading port 12a and a substrate loading port 12b. 13a, 13b, 13c are crystal growth furnaces provided with gas inlets 14a, 14b, 14c and gas outlets 15a, 15b, 15c, respectively, and crystal growth furnaces 13a, 13b, 13c are provided with heaters 16a, 16b, 16c, respectively It can be heated. Crystal growth vessels 17a, 17b, and 17c are housed in the crystal growth furnaces 13a, 13b, and 13c, respectively, and these crystal growth vessels 17a to 17c
(indicated by 17) is constructed as shown in FIG. In FIG. 3, 18 is a crystal growth tank, 19
20 is a raw material crystal dissolving tank, 20 is a mixed crystal raw material dissolving tank,
The raw material crystal dissolving tank 19 and the mixed crystal raw material dissolving tank 20 are each communicated with the crystal growth tank 18 as shown in the figure, so that each tank is filled with a growth solution. 21 is a raw material crystal melting heater (first heater); 22 is a mixed crystal raw material melting tank heater (second heater);
(heaters), and their temperatures can be controlled independently, as will be described later. Note that there is a partition 23 between the crystal growth containers 17a and 17b, and a partition 23 is provided between the crystal growth containers 17b and 17c.
There is a partition 24 between the two. 25 is a gas exchange chamber having a gas inlet 26 and a gas outlet 27;
8 is a board exit. The crystal growth furnaces 13a to 13b are arranged in series in multiple stages as shown in FIG. 12a into the gas exchange chamber 9a, and the gas exchange chambers 9a, 9b
After passing through the crystal growth furnaces 13a, 13b, and 13c, and after passing through the gas exchange chamber 25, the substrate exit 28
taken out. In this case, the crystal growth furnaces 13a to 13c are heated by the heaters 16a to 16c, respectively, and the fourth
As shown in the figure, each has a temperature profile suitable for its purpose. The crystal growth vessels 17a to 17c are made of well-washed high-quality graphite boats with a length of 20 cm and a height of 8 cm, the crystal growth tank 18 has a width of 8 cm, the raw material crystal dissolution tank 19 has a width of 5 cm, and a mixed crystal raw material dissolution tank. 20 is width 4
It has a size of cm. Table 1 shows the temperatures of the crystal growth tank 18, mixed crystal crystal dissolution tank 19, and mixed crystal raw material dissolution tank 20 of each of the crystal growth containers 17a to 17c, and the solutes in each of the tanks.

【表】 すなわち、原料結晶溶解槽19にはソース結晶
(GaAsまたはp−GaAs)を入れておき、常に均
一な飽和溶液を供給するようにしている。また、
混晶用原料溶解槽20には得ようとする混晶結晶
が例えばGaAlAs等の混晶の場合には、Alをいれ
て混晶結晶の組成を一定に保つよう目的の温度に
保持するようにする。なお、混晶用原料溶解槽2
0に原料を入れない場合にはその温度を特に制御
する必要はない。このようにした結晶成長容器1
7a〜17cをそれぞれ結晶成長炉13a〜13
c中に配置し、それぞれガス流入口14a〜14
cより不活性ガスを導入して炉内を不活性ガスで
置換後、各結晶成長炉13a〜13cの温度をそ
れぞれ第4図に示すような所定の温度に調整す
る。 このようにして、基板運搬架線31によつて基
板ケース30に設置された基板29を、基板搬入
口12aから不活性ガスで置換されたガス置換室
9a内に搬入し、次に、仕切り板12bを開けて
不活性ガスで置換されたガス置換室13b内に搬
入し、不活性ガスを充填後、結晶成長炉13a〜
13c内の結晶成長容器17a〜17cの結晶成
長槽18内に順次搬入し、結晶成長を行う。 なお、基板運搬架線31は断続的に移動できる
ようになつており、各結晶成長槽18内で所定の
時間結晶成長を行うことができるようにしてあ
る。 そして各結晶成長槽18で結晶成長後、ガス置
換室25に搬入してガス置換を行い、その後、基
板搬出口28より結晶成長後の基板29を外部に
取り出す。 次に、第5図に示すように例えばn−GaAs基
板29にn−GaAs41、p−GaAs42、p−
GaAlAs43を順次結晶成長させたものにn電極
44,p電極45を取り付けることによつて太陽
電池を得ることができる。この太陽電池の効率は
12%であつた。 上記した本発明の実施例によれば、各結晶成長
炉13a〜13cの結晶成長容器17a〜17c
の結晶成長槽18、原料結晶溶解槽19、混晶用
原料溶解槽20にそれぞれ温度差をつけることが
でき、また、基板29もしくはそれに結晶成長し
たものをバツチ式の結晶成長槽18に順次浸漬す
ることにより、結晶成長の難しいものでも簡単に
再現性よく結晶成長を行うことができ、短時間で
大量に成長層の膜厚の均一な半導体液相エピタキ
シヤル結晶板を再現性良く得ることができる。特
に高効率の発光ダイオード、太陽電池等の組成の
異なる多層構造を有する結晶板を得る場合、従来
のスライドボード法に比べて工業上著しい効果が
ある。 また、結晶成長槽18には原料結晶や混晶用原
料を入れていないため、それらが基板表面に付着
することはない。 更に、成長用溶液から析出した結晶の不足分
は、原料結晶溶解槽19,混晶用原料溶解槽20
から原料結晶,混晶用原料を溶かし込むことによ
り常に供給することができる。また、成長用溶液
を交換することなく連続使用が可能である。 なお、装置の各部の大きさ、材質等は適宜目的
に合うように選定することができ、また、不活性
ガスによるガス置換は、真空排気後行うようにし
てもよく、このようにすると酸素等の不純物ガス
が取り除かれるので好ましい。この場合、基板搬
送架線31の移動が停止しているとき、真空シー
ルしてガス置換室9a,9bの真空排気を行うよ
うにすれば、容易に真空にすることができ、その
後不活性ガスあるいは還元性ガスを流すようにす
る。 [発明の効果] 以上説明したように、本発明によれば、一回毎
の成長で原料の補充や成長用溶液の交換をするこ
となく、常に成長用溶液の飽和度を所定の状態に
設定できるため、連続して所望の膜厚の多層の成
長層を再現性よく短時間で大量に得ることができ
る。また、成長用溶液の混晶比を容易に所定の状
態に設定することが可能であるため、所望の混晶
比の混晶結晶を再現性良く連続エピタキシヤル成
長でき、特に高効率の発光ダイオード、太陽電池
等の組成の異なる多層構造を有する結晶板を得る
場合、工業上著しい効果がある。
[Table] That is, a source crystal (GaAs or p-GaAs) is placed in the raw material crystal dissolving tank 19 so that a uniform saturated solution is always supplied. Also,
If the mixed crystal to be obtained is a mixed crystal such as GaAlAs, Al is added to the mixed crystal raw material dissolving tank 20 to keep the composition of the mixed crystal constant at a desired temperature. do. In addition, mixed crystal raw material dissolving tank 2
When no raw material is added to the temperature, there is no need to particularly control the temperature. Such a crystal growth container 1
7a to 17c are crystal growth furnaces 13a to 13, respectively.
gas inlets 14a to 14, respectively.
After replacing the inside of the furnace with inert gas by introducing an inert gas from c, the temperature of each crystal growth furnace 13a to 13c is adjusted to a predetermined temperature as shown in FIG. 4, respectively. In this way, the substrate 29 installed in the substrate case 30 is carried through the substrate carrying overhead wire 31 into the gas exchange chamber 9a, which has been substituted with an inert gas, through the substrate loading port 12a, and then the partition plate 12b is opened and carried into the gas replacement chamber 13b, which has been replaced with inert gas, and after being filled with inert gas, the crystal growth furnaces 13a to
The crystals are sequentially transported into the crystal growth vessels 18 of the crystal growth vessels 17a to 17c in the crystal growth chamber 13c, and crystal growth is performed. Note that the substrate carrying overhead wire 31 can be moved intermittently, so that crystal growth can be performed in each crystal growth tank 18 for a predetermined period of time. After crystal growth in each crystal growth tank 18, the substrate 29 is carried into the gas exchange chamber 25 for gas exchange, and then the substrate 29 after crystal growth is taken out from the substrate outlet 28. Next, as shown in FIG. 5, for example, n-GaAs41, p-GaAs42, p-
A solar cell can be obtained by attaching an n-electrode 44 and a p-electrode 45 to a crystal of GaAlAs 43 grown sequentially. The efficiency of this solar cell is
It was 12%. According to the embodiment of the present invention described above, the crystal growth vessels 17a to 17c of each crystal growth furnace 13a to 13c
It is possible to set a temperature difference between the crystal growth tank 18, the raw material crystal dissolution tank 19, and the mixed crystal raw material dissolution tank 20, and the substrate 29 or the crystal grown thereon can be sequentially immersed in the batch-type crystal growth tank 18. By doing so, it is possible to easily grow crystals with good reproducibility even when crystal growth is difficult, and it is possible to obtain semiconductor liquid phase epitaxial crystal plates with uniform growth layer thickness in large quantities in a short time with good reproducibility. can. In particular, when obtaining a crystal plate having a multilayer structure with different compositions, such as a highly efficient light emitting diode or solar cell, this method is industrially more effective than the conventional slide board method. Moreover, since the crystal growth tank 18 does not contain raw material crystals or mixed crystal raw materials, they do not adhere to the substrate surface. Furthermore, the shortage of crystals precipitated from the growth solution is removed from the raw material crystal dissolving tank 19 and the mixed crystal raw material dissolving tank 20.
It can be constantly supplied by melting raw material crystals and raw materials for mixed crystals. Furthermore, continuous use is possible without replacing the growth solution. The size, material, etc. of each part of the device can be appropriately selected to suit the purpose, and gas replacement with inert gas may be performed after evacuation. This is preferable because it removes impurity gases. In this case, when the movement of the substrate transport overhead line 31 is stopped, if the gas replacement chambers 9a and 9b are vacuum-sealed and the gas exchange chambers 9a and 9b are evacuated, the vacuum can be easily created. Allow reducing gas to flow. [Effects of the Invention] As explained above, according to the present invention, the saturation level of the growth solution can always be set to a predetermined state without replenishing raw materials or replacing the growth solution for each growth. Therefore, it is possible to continuously obtain a large amount of multi-layered growth layers of a desired thickness in a short period of time with good reproducibility. In addition, since it is possible to easily set the mixed crystal ratio of the growth solution to a predetermined state, it is possible to continuously epitaxially grow mixed crystals with a desired mixed crystal ratio with good reproducibility. This method has a significant industrial effect when obtaining a crystal plate having a multilayer structure with different compositions, such as for solar cells.

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

第1図は従来のスライドボード法による液相結
晶成長方法を説明するための図、第2図は本発明
の液相エピタキシヤル結晶成長装置の一実施例を
示す正面図、第3図は第2図の各結晶成長容器の
一実施例を示す縦断面図、第4図は第2図の各結
晶成長炉の温度プロフアイルを示す線図、第5図
は本発明の装置によつて製造された結晶成長板を
用いた半導体装置の模式図である。 9a,9b,25:ガス置換室、13a〜13
c……結晶成長炉、16a〜16c……加熱ヒー
タ、17a〜17c……結晶成長容器、18……
結晶成長槽、19……原料結晶溶解槽、20……
混晶用原料溶解槽、21……原料結晶溶解槽加熱
ヒータ(第1ヒータ)、22……混晶用原料溶解
槽加熱ヒータ(第2ヒータ)、29……基板、3
0……基板ケース、31……基搬搬送架線。
FIG. 1 is a diagram for explaining a conventional liquid phase crystal growth method using the slide board method, FIG. 2 is a front view showing an embodiment of the liquid phase epitaxial crystal growth apparatus of the present invention, and FIG. 2 is a vertical cross-sectional view showing an example of each crystal growth container shown in FIG. 2, FIG. 4 is a diagram showing the temperature profile of each crystal growth furnace shown in FIG. 2, and FIG. FIG. 2 is a schematic diagram of a semiconductor device using a crystal growth plate obtained by the above-mentioned method. 9a, 9b, 25: gas replacement chamber, 13a-13
c...Crystal growth furnace, 16a-16c...Heater, 17a-17c...Crystal growth container, 18...
Crystal growth tank, 19... Raw material crystal dissolution tank, 20...
Mixed crystal raw material dissolving tank, 21... Raw material crystal dissolving tank heater (first heater), 22... Mixed crystal raw material dissolving tank heater (second heater), 29... Substrate, 3
0... Board case, 31... Base transport overhead wire.

Claims (1)

【特許請求の範囲】[Claims] 1 不活性ガス置換を行う第1のガス置換室と、
該第1のガス置換室の後段に順次直列に配置され
た複数の結晶成長炉と、該結晶成長炉内を加熱す
る加熱ヒータと、前記結晶成長炉に置かれた成長
用溶液を収容するための結晶成長容器と、前記結
晶成長炉の後段に設けられた第2のガス置換室
と、基板を取り付けた基板ケースを前記第1のガ
ス置換室から前記第2のガス置換室まで搬送する
手段とを備え、前記結晶成長容器は、前記基板ケ
ースが前記成長用溶液中に浸漬される結晶成長槽
と、前記結晶成長槽と連通して前記原料溶液が満
たされかつ原料結晶及び該原料結晶との組合わせ
により混晶結晶を形成する混晶用原料をそれぞれ
収容するための原料結晶溶解槽及び混晶用原料溶
解槽と、前記原料結晶溶解槽を加熱して前記原料
結晶を溶解し前記成長用溶液の飽和度を調節する
第1ヒータと、前記混晶原料溶解槽を加熱して前
記混晶用原料を溶解し前記成長用溶液から得られ
る混晶結晶の混晶比を調節する第2ヒータとを備
えていることを特徴とする基板上に連続的に多層
結晶を成長させる液相エピタキシヤル結晶成長装
置。
1 a first gas replacement chamber that performs inert gas replacement;
For accommodating a plurality of crystal growth furnaces sequentially arranged in series after the first gas exchange chamber, a heater for heating the inside of the crystal growth furnace, and a growth solution placed in the crystal growth furnace. a crystal growth container, a second gas exchange chamber provided at the rear stage of the crystal growth furnace, and means for transporting a substrate case with a substrate attached from the first gas exchange chamber to the second gas exchange chamber. The crystal growth container includes a crystal growth tank in which the substrate case is immersed in the growth solution, and a crystal growth tank that communicates with the crystal growth tank and is filled with the raw material solution and that contains raw material crystals and the raw material crystal. A raw material crystal dissolving tank and a mixed crystal raw material dissolving tank for accommodating raw materials for a mixed crystal, respectively, which form a mixed crystal by a combination of the above, and the raw material crystal dissolving tank is heated to melt the raw material crystal and grow. a first heater that adjusts the degree of saturation of the growth solution, and a second heater that heats the mixed crystal raw material dissolving tank to dissolve the mixed crystal raw material and adjust the mixed crystal ratio of the mixed crystal crystal obtained from the growth solution. 1. A liquid phase epitaxial crystal growth apparatus for continuously growing multilayer crystals on a substrate, characterized by comprising a heater.
JP15762683A 1983-08-29 1983-08-29 Liquid phase epitaxial crystal growth method and its equipment Granted JPS6051695A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15762683A JPS6051695A (en) 1983-08-29 1983-08-29 Liquid phase epitaxial crystal growth method and its equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15762683A JPS6051695A (en) 1983-08-29 1983-08-29 Liquid phase epitaxial crystal growth method and its equipment

Publications (2)

Publication Number Publication Date
JPS6051695A JPS6051695A (en) 1985-03-23
JPH0428678B2 true JPH0428678B2 (en) 1992-05-14

Family

ID=15653837

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15762683A Granted JPS6051695A (en) 1983-08-29 1983-08-29 Liquid phase epitaxial crystal growth method and its equipment

Country Status (1)

Country Link
JP (1) JPS6051695A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63183275U (en) * 1987-05-19 1988-11-25
JP4548031B2 (en) * 2004-07-30 2010-09-22 株式会社島津製作所 Crystal manufacturing method and crystal manufacturing apparatus
CN102732950B (en) * 2012-06-20 2015-04-15 常州天合光能有限公司 Apparatus for continuously growing quasi-monocrystalline crystals

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS569009B2 (en) * 1973-08-13 1981-02-26
JPS515636A (en) * 1974-07-04 1976-01-17 Tokyo Gas Co Ltd Ekitainenryono chitsusosankabutsuteihatsuseinenshohoho

Also Published As

Publication number Publication date
JPS6051695A (en) 1985-03-23

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