JPH0222196A - Liquid phase crystal growth method and apparatus - Google Patents
Liquid phase crystal growth method and apparatusInfo
- Publication number
- JPH0222196A JPH0222196A JP33311087A JP33311087A JPH0222196A JP H0222196 A JPH0222196 A JP H0222196A JP 33311087 A JP33311087 A JP 33311087A JP 33311087 A JP33311087 A JP 33311087A JP H0222196 A JPH0222196 A JP H0222196A
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- Prior art keywords
- substrate
- melt
- slider
- temperature
- cavity
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- Liquid Deposition Of Substances Of Which Semiconductor Devices Are Composed (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は液相結晶成長に関し、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連
続液相成長に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to liquid phase crystal growth, and in particular to a process in which a certain temperature difference is created in a melt containing dissolved solute, and the solute is continuously transported from a high temperature area to a low temperature area. This paper relates to continuous liquid phase growth using a temperature difference method in which crystals are grown in a low-temperature region.
[従来の技術]
液相結晶成長は特に化合物半導体の結晶成長技術として
広く用いられている。液相結晶成長法として徐冷法や温
度差法等が知られている。[Prior Art] Liquid phase crystal growth is widely used as a crystal growth technique, especially for compound semiconductors. A slow cooling method, a temperature difference method, and the like are known as liquid phase crystal growth methods.
徐冷法は、たとえば、結晶材料をルツボ内で加熱して溶
融し、徐々に冷却して結晶化させる方法である。冷却方
法、ルツボ形状等によりストックバーガ法、ブリッジマ
ン法等に分かれる。The slow cooling method is, for example, a method in which a crystalline material is heated and melted in a crucible, and then gradually cooled and crystallized. It is divided into the Stockburger method, Bridgman method, etc. depending on the cooling method, crucible shape, etc.
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、広義にはフローティング
ゾーン法等も含むが、狭義には溶液(メルト)内に温度
差を設け、高温部で溶質を溶解(供給)すると共に低温
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法は、成長用材料(溶質)
を溶解した溶液(メルト)に温度差をつけ、温度勾配と
拡散によって溶質を基板方向に輸送し、基板上に結晶を
成長させる方法で、一定温度で成長できるため均一な不
純物濃度や組成をもつ結晶性の良い結晶が多数枚連続し
て得られる方法である例えば、GaAIAS系結晶の場
合、グラファ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℃で10℃−200
°Cの温度差を設けて結晶成長を行う、この方法により
、特性の優れた発光グイオート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 zone and a low-temperature zone are formed with a certain temperature difference (or temperature gradient), and raw materials are supplied from the high-temperature zone and crystals are precipitated in the low-temperature zone. However, in a narrow sense, it refers to a method in which a temperature difference is created in a solution (melt), the solute is dissolved (supplied) in the high temperature part, and the solute is precipitated from a supersaturated solution in the low temperature part, that is, temperature difference method liquid phase crystallization. Growth method uses growth material (solute)
A method in which a temperature difference is applied to a solution (melt) in which the solute is dissolved, and the solute is transported toward the substrate by the temperature gradient and diffusion to grow crystals on the substrate. Because the crystal can be grown at a constant temperature, it has a uniform impurity concentration and composition. For example, in the case of GaAIAS crystals, a melt made of Ga solution is placed in a melt bath made of graphite, and a melt made of Ga solution is heated at 800°C-1000°C and 10°C-200°C.
Using this method of growing crystals with a temperature difference of .degree. C., light-emitting diodes, lasers, and the like with excellent characteristics have been manufactured.
[発明が解決しようとする問題点]
溶質を基板に向けて輸送するために基板面に垂直の方向
に温度差をつける。しかし基板面内にわたり均一に成長
させるためには面内方向に均一な温度分布を設けること
が必要である。しかし面に垂直な温度差と面内の均一な
温度との両者を両立させることは容易ではない
従来は、特公昭59−43087号公報に示されている
ように、加熱用炉体や冷却源のバランスをとることによ
り基板面内の温度分布を均一にしようとしていた。[Problems to be Solved by the Invention] In order to transport solute toward the substrate, a temperature difference is created in the direction perpendicular to the substrate surface. However, in order to grow uniformly over the substrate surface, it is necessary to provide a uniform temperature distribution in the in-plane direction. However, it is not easy to achieve both the temperature difference perpendicular to the surface and the uniform temperature within the surface. The attempt was made to make the temperature distribution uniform within the substrate plane by balancing the
しかし、これらの方法で均一な温度分布を実現するのは
困難であり、第11図に示すような均一でない厚み分布
の成長結果が多く、また、炉体の成長システムのわずか
な相違、変動により厚み分布が変動してしまう。However, it is difficult to achieve a uniform temperature distribution using these methods, and the growth results often have an uneven thickness distribution as shown in Figure 11. Also, due to slight differences and fluctuations in the growth system of the furnace body, The thickness distribution will fluctuate.
このような均一でない厚み分布は1発光ダイオードの製
造においては発光効率のバラツキに直結しており、製造
歩留まりの低下の主要な原因である
そこで1本発明の目的は均一な面内湯度分布を実現でき
る温度差法液相結晶成長技術を提供することである。Such non-uniform thickness distribution is directly linked to variations in luminous efficiency in the production of light-emitting diodes, and is a major cause of decreased manufacturing yield.Therefore, the purpose of the present invention is to realize a uniform in-plane temperature distribution. The purpose of this invention is to provide a temperature difference method liquid phase crystal growth technology that can be used.
[問題点を解決するなめにおこなった検討]上記の問題
点を解決するために、温度差法連続液相結晶成長での結
晶成長のメカニズムを検討した。[Studies conducted to solve the problems] In order to solve the above problems, we investigated the mechanism of crystal growth in continuous liquid phase crystal growth using the temperature difference method.
第4図に温度差法液相成長装置の例を概略的に示す、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、スライダ押上機構55により順次ゲ
ートバルブ62を通って押し上げられる。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63を通って送られる。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の下部でメルトと接触し結晶成長を
行う、結晶成長の終わっ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1スライ
ダ受取機栴77によってゲートバルブ74を介して出口
側予備室79に収められる。FIG. 4 schematically shows an example of a temperature difference method liquid phase growth apparatus. Inside the entrance side preliminary chamber 51 is a slider 53 on which a semiconductor substrate is placed.
are housed therein, and are successively pushed up through the gate valve 62 by the slider push-up mechanism 55. Preferably, the entrance side preliminary chamber 51 is preheated in a preliminary heating furnace 59.
The pushed-up slider is sent into the growth chamber 57 through the gate valve 63 by the slider drive mechanism 61. A melt tank 64 is provided in the growth chamber 57, and a main heater 67
is heating the melt tank 64. The substrate 69 on the slider 53 contacts the melt at the bottom of the melt tank 64 to perform crystal growth.The slider carrying the substrate on which the crystal growth has been completed is sent out of the growth chamber 57 via the gate valve 73 and receives one slider. It is stored in the outlet side preliminary chamber 79 by the machine 77 via the gate valve 74.
第5図はメルト槽64部分の1例の拡大説明図である。FIG. 5 is an enlarged explanatory view of one example of the melt tank 64 portion.
溶媒であるGaの中に溶質のAI、GaAsが溶解され
て、Pメルト低温部と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
域のバンドギャップをP型頭域のバンドギャップより大
きくするためNメルト槽66中のAIの量はPメルト槽
65中のAIの量より大きくするのがよい、たとえば、
赤色発光Ga AI As発光ダイ第1−x
x
−ドを得るには、AlAsの組成割合XをP型頭域で約
0.35.n型領域で約0.6−0.85となるように
AIとGaAsの量を決める0両メルト槽65,66内
には図中布に示すような垂直方向の温度差が設定される
。たとえば、800℃−1000℃の温度で温度差を1
0℃−200℃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力科容買収
容部を作ってメルトと接触させる。溶質は高温部で飽和
溶解度まで溶解し、拡散で低温部に輸送される。Solutes AI and GaAs are dissolved in Ga, which is a solvent, and stored in the P melt low temperature section and the N melt tank 66. Furthermore, as impurities, Zn is dissolved in the P melt tank 65 and Te is dissolved in the N melt tank. The amount of AI in is preferably larger than the amount of AI in the P melt tank 65, for example,
Red light emitting Ga AI As light emitting die No. 1-x
To obtain the x-do, the AlAs composition ratio X should be approximately 0.35. The amounts of AI and GaAs are determined to be about 0.6-0.85 in the n-type region.A vertical temperature difference as shown by the cloth in the figure is set in the two melt tanks 65 and 66. For example, at a temperature of 800℃-1000℃, the temperature difference is 1
Set the temperature between 0°C and 200°C. In order to continuously supply the solute, a container is created in which the solute floats above the melt, which is a high-temperature part, and is brought into contact with the melt. The solute dissolves to saturation solubility in the high temperature section and is transported to the low temperature section by diffusion.
通常溶解度は温度と共に増加するので、低温部では過飽
和溶液となって析出できる状態となる。このようなメル
ト低温部へ多数枚の基板69を順次接触させる。たとえ
ば、成長時間約60分で50−60μmの成長層が得ら
れる。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 be precipitated. A large number of substrates 69 are sequentially brought into contact with such a melt low temperature section. For example, a growth time of about 60 minutes yields a growth layer of 50-60 μm.
第6図は温度と時間との関係を示す0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1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。このような操作をくりかえして多数枚の基板上に
エピタキシャル成長を行う。As can be seen from Figure 6, which shows the relationship between temperature and time, the temperature distribution is kept constant. Initially, the first substrate is in contact with the bottom of the P melt, and the P type layer is grown.First, the slider is moved so that the first substrate is in contact with the bottom of the N melt, and the second substrate is in contact with the bottom of the P melt. do it like this. Therefore, respective growth layers are formed. Now, on the first substrate, a P-type layer is grown on the bottom and an N-type layer is grown on top, forming a diode. Such operations are repeated to perform epitaxial growth on a large number of substrates.
さて、結晶成長を行えるのはメルト下部の低温部である
が、メルトと通常グラファイトであるメルト槽を作って
いる耐熱材とは熱伝導率等の熱的特性が異なる。メルト
下部で面内均一な温度分布を実現するために解明すべき
問題の1つはグラファイトに囲まれたメルトと基板との
関係であろうそこで、以下の場合に分けて検討しな。Now, crystal growth can occur in the low-temperature area at the bottom of the melt, but the melt and the heat-resistant material that makes up the melt tank, which is usually graphite, have different thermal properties such as thermal conductivity. One of the issues that must be solved in order to realize a uniform in-plane temperature distribution at the bottom of the melt is the relationship between the melt surrounded by graphite and the substrate, so let's consider the following cases separately.
[A、メルトの底面の大きさと基板の大きさがほぼ等し
い場合] (第7図、第8図参照)基板中心付近81に
比べて周辺部83の成長速度が遅い、これはメルト槽の
内壁がらは溶質の供給がないことが1つの原因と考えら
れる。またメルト槽の側壁(グラファイト)の熱伝導率
はメルト(Ga)の熱伝導率より大きい、このため、基
板中心付近81に比べて周辺部83の温度勾配が小さい
、したがって濃度勾配が小さく周辺部83の成長速度が
遅いと考えられる。[A. When the size of the bottom surface of the melt and the size of the substrate are almost equal] (See Figures 7 and 8) The growth rate in the peripheral area 83 is slower than in the vicinity 81 of the substrate center. This is due to the inner wall of the melt tank. One reason for this is thought to be that there is no supply of solutes. In addition, the thermal conductivity of the side wall (graphite) of the melt tank is higher than that of the melt (Ga). Therefore, the temperature gradient in the peripheral area 83 is smaller than that near the center of the substrate 81, and therefore the concentration gradient is small in the peripheral area. It is considered that the growth rate of 83 is slow.
[B、メルトの底面の大きさが基板の大きさより大きい
場合] (第9図、第10図参照)基板の大きさがメル
トの底面の大きさより小さいため、基板周辺部87もメ
ルト槽の側壁から離れ基板中心付近85と基板の周辺部
87との温度勾配の差は[AIに比べ大きくない、また
基板面内の温度分布も[AIに比べより均一である。し
たがって成長速度は[AIより面内で比較的均一になる
。[B. When the size of the bottom surface of the melt is larger than the size of the substrate] (See FIGS. 9 and 10) Since the size of the substrate is smaller than the size of the bottom surface of the melt, the peripheral portion 87 of the substrate also overlaps the side wall of the melt tank. The difference in temperature gradient between the center of the substrate 85 and the periphery 87 of the substrate is not large compared to AI, and the temperature distribution within the substrate surface is also more uniform than AI. Therefore, the growth rate is relatively uniform within the plane compared to [AI].
しかし、基板より外の周辺部8つのメルト底面が、基板
より熱伝導率が大きくかつその上に結晶をエピタキシャ
ル成長させることのできないグラファイトからなるスラ
イダ53に接している。したがって基板外の周辺部8つ
において基板面内85.87においてと同等またはそれ
以上の熱がメルトからスライダに向かって流れる。すな
わち。However, the bottom surfaces of the eight peripheral portions of the melt outside the substrate are in contact with a slider 53 made of graphite, which has a higher thermal conductivity than the substrate and on which crystals cannot be epitaxially grown. Therefore, the same or more heat flows from the melt toward the slider in the eight peripheral areas outside the substrate than in the in-plane areas 85,87 of the substrate. Namely.
この領域においても、拡散による溶質の輸送は常に行わ
れている6しかし基板結晶がないため輸送された溶質は
過飽和状態となり、メルト内のスライダ表面近傍におい
て微結晶を析出させる。溶質の輸送が常に行われている
ため、この微結晶が種となりさらに連続して微結晶への
析出が行われる。Even in this region, transport of solute by diffusion is always carried out 6 However, since there are no substrate crystals, the transported solute becomes supersaturated, causing microcrystals to precipitate in the vicinity of the slider surface within the melt. Since the solute is constantly being transported, these microcrystals serve as seeds and are continuously precipitated into microcrystals.
この基板外の周辺部89のメルト内での微結晶析出のた
めに、基板内周辺部87での溶質の輸送が影響され、中
心部85に比べ基板内周辺部87の成長速度が小さくな
る。Due to the precipitation of microcrystals within the melt in the peripheral portion 89 outside the substrate, the transport of solute in the inner peripheral portion 87 of the substrate is affected, and the growth rate of the inner peripheral portion 87 of the substrate is lower than that in the central portion 85 .
[AI [B]いずれの場合も均一な厚み分布の成長
が実現されず、たとえば、第11図に示すように周辺部
の成長厚が中心部より小さくなりやすい、さらに[AI
[B]いずれの場合もスライダの移動により温度変
動が起こると、その影響を十分吸収出来ず、連続して多
数枚成長させたときの厚みや分布の変動を生ずる。[AI
[B] In either case, if temperature fluctuation occurs due to the movement of the slider, the effect cannot be sufficiently absorbed, resulting in variations in thickness and distribution when a large number of sheets are grown in succession.
以上の検討に基ずいたとき、[B]において基板外周辺
部8つのメルト内での微結晶の析出を抑制するならばよ
り均一な厚みの結晶成長が可能になるものと考えられる
。Based on the above study, it is considered that if the precipitation of microcrystals in the eight melts around the outer periphery of the substrate is suppressed in [B], crystal growth with a more uniform thickness will be possible.
[問題点を解決するための手段]
本発明によれば、温度差法液相結晶成長において、基板
をメルトの横断面積より小さくして基板の下方のスライ
ダの内部に基板面積より大きい外周部を有する空洞を設
け、この空洞に成長温度で液状となる金属(液体金属)
を収納し、この空洞の上壁面に段差を設け基板の真下に
おいて下方に向かう凸部を形成し、基板とほぼ同じ表面
積にわたり液体金属の上表面と接触させ、その外側の上
壁面は高くして液体金属と接触せず液体金属の上面に空
間が形成されるようにし、この空間と外部とを細孔で連
結する。[Means for Solving the Problems] According to the present invention, in temperature difference method liquid phase crystal growth, the cross-sectional area of the substrate is made smaller than that of the melt, and an outer peripheral portion larger than the substrate area is formed inside the slider below the substrate. A metal that becomes liquid at the growth temperature (liquid metal) is provided in the cavity.
A step is provided on the upper wall of this cavity to form a downwardly directed convex portion directly below the substrate, and the upper wall surface on the outside is raised so that it is in contact with the upper surface of the liquid metal over approximately the same surface area as the substrate. A space is formed above the liquid metal without contact with the liquid metal, and this space is connected to the outside through a pore.
[作用]
第1図、第2図を参照して説明すると、基板の下方のス
ライダ内部に基板面積より大きい41!断面積の空洞を
設け、そこに結晶成長温度で液状となる金属(液体金属
)が充填されており、この液体金属が熱対流によって移
動するため、基板面内方向に温度分布があっても均熱化
される。[Function] To explain with reference to FIGS. 1 and 2, there is a 41! larger than the substrate area inside the slider below the substrate! A cavity with a cross-sectional area is provided, and the cavity is filled with a metal that becomes liquid at the crystal growth temperature (liquid metal). Because this liquid metal moves by thermal convection, even if there is a temperature distribution in the in-plane direction of the substrate, it is not uniform. becomes heated.
基板の真下においては、空洞の上壁面から下方に向かう
凸部が設けられ、基板とほぼ同じ断面積にわたり前記の
液体金属の上表面と接触し、熱流の通路を形成している
。その外側では、液体金属が空洞上壁面と接さす、液体
金属の上面には気体空間が設けられている。このため、
メルトがスライダと直接接触している基板外の周辺部8
9における基板面に垂直方向の熱抵抗は、基板部85゜
87における熱抵抗より大きく、基板外の周辺部89を
流れる熱を抑制することができる。Directly below the substrate, a convex portion extending downward from the upper wall surface of the cavity is provided, and contacts the upper surface of the liquid metal over approximately the same cross-sectional area as the substrate, thereby forming a heat flow path. On the outside, a gas space is provided on the upper surface of the liquid metal, where the liquid metal contacts the upper wall surface of the cavity. For this reason,
Perimeter outside the board 8 where the melt is in direct contact with the slider
The thermal resistance in the direction perpendicular to the substrate surface at 9 is greater than the thermal resistance at the substrate portion 85° 87, and the heat flowing through the peripheral portion 89 outside the substrate can be suppressed.
[実施例〕
第1図、第2図に本発明の1実施例による液相結晶成長
装置を部分的に示す。[Embodiment] FIGS. 1 and 2 partially show a liquid phase crystal growth apparatus according to an embodiment of the present invention.
メルト槽11の中には結晶成長用のメルト13が収容さ
れている5メルト槽11の底は開いていてスライダ21
が底の開口を塞ぐようになっている。スライダ21の中
央部には凹部17が設けられ、成長下地となる半導体基
板19が収められている。従って半導体基板19の上面
はメルト13の底部中央部と接する。スライダはガイド
部材ののレール(図示せず)を摺動し1図面の紙面と垂
直の方向に動く、スライダの内部にはメルト槽の下方に
空洞部25が形成されている。空洞の横方向寸法は本実
施例ではメルト13の底面積よりやや大きめとしである
が、これに限らない、但しメルト13の横断面積とほぼ
同じかそれ以上の横断面積をもつことが好ましい、空洞
部25の上壁には下方への凸部27が形成されている。The melt tank 11 contains a melt 13 for crystal growth.The bottom of the melt tank 11 is open and a slider 21
is designed to cover the opening at the bottom. A recess 17 is provided in the center of the slider 21, and a semiconductor substrate 19 serving as a growth base is housed therein. Therefore, the upper surface of the semiconductor substrate 19 is in contact with the bottom central portion of the melt 13. The slider slides on a rail (not shown) of a guide member and moves in a direction perpendicular to the plane of the drawing. A cavity 25 is formed inside the slider below the melt tank. In this embodiment, the lateral dimension of the cavity is slightly larger than the bottom area of the melt 13, but is not limited to this, but it is preferable that the cavity has a cross-sectional area that is approximately the same as or larger than the cross-sectional area of the melt 13. A downward convex portion 27 is formed on the upper wall of the portion 25 .
この凸部27は基板19ないしスライダの凹部17とほ
ぼ同じ横断面積をらち水平な下面をもつよう設計される
。さらにこの空洞部25と外部とを結ぶ連絡孔29が形
成され、液体金属や雰囲気ガスの出入りを可能にしてい
る。空洞部25に液体金属(例えばGa)31を入れて
いくと液面と凸部27の下面とが均一に接する。この時
凸部27の周囲には空間33が残っている。液面を上げ
ていくと空間33は次第に小さくなり、凸部27は液体
金属31の中になかば没する。The convex portion 27 is designed to have approximately the same cross-sectional area as the substrate 19 or the concave portion 17 of the slider, and to have a horizontal lower surface. Furthermore, a communication hole 29 is formed that connects this cavity 25 with the outside, allowing liquid metal and atmospheric gas to enter and exit. When liquid metal (for example, Ga) 31 is poured into the cavity 25, the liquid level and the lower surface of the convex portion 27 come into uniform contact. At this time, a space 33 remains around the convex portion 27. As the liquid level increases, the space 33 gradually becomes smaller, and the convex portion 27 is partially submerged in the liquid metal 31.
メルト槽11.スライダ21はグラファイトのような耐
熱材料で作られている。メルト13は通常成長すべき半
導体材料の構成元素の1つを溶媒としている。GaAs
、GaAlAs、GaAIAsP、GaP、GaSb等
の場合はGa、InAs、InAsP等の場合はInを
用いる。液体金属31は使用温度(はぼ結晶成長温度)
で液体であれば良<、Ga、In、Hg等が用いられる
。Melt tank 11. Slider 21 is made of a heat-resistant material such as graphite. The melt 13 normally uses one of the constituent elements of the semiconductor material to be grown as a solvent. GaAs
, GaAlAs, GaAIAsP, GaP, GaSb, etc., and In for InAs, InAsP, etc., In is used. The liquid metal 31 is at the operating temperature (crystal growth temperature)
If it is a liquid, Ga, In, Hg, etc. can be used.
メルト13の主成分と液体金属の主成分とを一致させて
おくのが不純物防止、熱的設計等の面から好ましいこと
が多い、均一な厚さの結晶成長を得るには基板19上で
の温度分布が面内均一でかつ温度勾配も面内均一であり
、さらに基板19より外側の部分89では微結晶が発生
しないことが望ましい、そのためには基板19の断面積
内において均一な熱流が上から下に流れ、その外側では
熱流が制限されることが望ましい。It is often preferable to match the main components of the melt 13 with the main components of the liquid metal from the viewpoint of preventing impurities and thermal design. It is desirable that the temperature distribution is uniform within the plane and the temperature gradient is also uniform within the plane, and furthermore, no microcrystals are generated in the portion 89 outside the substrate 19. To achieve this, uniform heat flow within the cross-sectional area of the substrate 19 is desirable. It is desirable for heat flow to flow downwards from the outside of the wall, with restricted heat flow outside of it.
まず基板19の断面積内では上からメルト13基板19
.スライダ21上部(凸部27を含む)。First, within the cross-sectional area of the substrate 19, the melt 13 substrate 19 is
.. Upper part of slider 21 (including convex portion 27).
液体金属31.スライダ21下部と熱が流れる。Liquid metal 31. Heat flows to the lower part of the slider 21.
その外側ではスライダ21上部に凸部27が存在せず1
代わりに気体空間33が入る。On the outside, there is no convex portion 27 on the top of the slider 21, and 1
A gas space 33 is inserted instead.
基板19の断面積内では構造が面内で均一であり均一な
熱流を作り易くしている。さらに液体金属31は熱伝導
のみでなく熱対流によっても熱を輸送できるので、温度
分布に不均一が生じた場合対流によって均熱化する役割
を果たす。The structure is uniform within the cross-sectional area of the substrate 19, making it easy to create a uniform heat flow. Furthermore, since the liquid metal 31 can transport heat not only by thermal conduction but also by thermal convection, it plays a role of equalizing the temperature by convection when the temperature distribution is uneven.
基板19の外側では熱回路中に空間33(気体)が入る
。気体の熱伝導率はグラファイト等の耐熱材料の熱伝導
率より格段に少ないので熱流は大きく制限される。この
ため、基板19より外側の部分8つでの微結晶析出は抑
制される。Outside the substrate 19, a space 33 (gas) enters the thermal circuit. Heat flow is greatly restricted because the thermal conductivity of gases is much lower than that of heat-resistant materials such as graphite. For this reason, precipitation of microcrystals in the portions 8 outside the substrate 19 is suppressed.
たとえば、結晶成長装置の構成材料の熱伝導率(300
K ) [W/cl−deg]の代表例は以下の通り
である。For example, the thermal conductivity (300
K) Representative examples of [W/cl-deg] are as follows.
H20,0018
Ga 0. 335
グラフアイト 1,2
GaAs 0.54
この液体金[31の熱対流による均熱化と基板外の周辺
領域8つにおける微結晶析出の抑制により、第3図に示
すような均一な厚さの成長結晶が得られる。H20,0018 Ga 0. 335 Graphite 1,2 GaAs 0.54 By equalizing the temperature by thermal convection of this liquid gold [31] and suppressing the precipitation of microcrystals in eight peripheral regions outside the substrate, a uniform thickness as shown in Fig. 3 is obtained. A grown crystal is obtained.
基板の下方には空間がなく、熱抵抗は大きく影響されな
いので、成長速度は従来例とほぼ同様であり、高輝度発
光ダイオードに必要な成長厚みが確保される。Since there is no space below the substrate and the thermal resistance is not greatly affected, the growth rate is almost the same as in the conventional example, and the growth thickness necessary for high brightness light emitting diodes is ensured.
また液体金属の上面に設けられた空間は、細孔により外
部雰囲気と連結されているので、高温になっても内部圧
力が上昇する危険はないさらに周辺部での液体金属の上
面の空間33の容積を調節することにより、基板外周辺
領域8つにおける基板面に垂直方向の熱抵抗を調節する
こともでき、加熱用炉体や冷却源等の成長システムのわ
ずかな相違による。成長条件の相違を調節補償すること
もできる。Furthermore, since the space provided on the upper surface of the liquid metal is connected to the external atmosphere through the pores, there is no risk of internal pressure increasing even if the temperature rises. By adjusting the volume, it is also possible to adjust the thermal resistance perpendicular to the substrate surface in the eight outer peripheral regions of the substrate, due to slight differences in the growth system, such as the heating furnace and the cooling source. It is also possible to adjust and compensate for differences in growth conditions.
この方法は、GaAlAsのみならず、GaPGaAs
InP、InP、InGaAsP、あるいは、Zn5e
、ZnTe、HgCdTeその他の温度差法液相エピタ
キシャル成長法による結晶の成長に適用できる。This method applies not only to GaAlAs but also to GaPGaAs.
InP, InP, InGaAsP or Zn5e
, ZnTe, HgCdTe, and other crystals by temperature difference method liquid phase epitaxial growth method.
この構成により、基板19上に均一な熱流をつくり、そ
の外側での結晶析出を抑制し、特性の良い発光ダイオー
ドを高歩留まりで製造できる。With this configuration, a uniform heat flow is created on the substrate 19, crystal precipitation on the outside thereof is suppressed, and light emitting diodes with good characteristics can be manufactured at a high yield.
し発明の効果]
以上のように、空洞と熱対流によっても均熱化を達しや
すい液体金属とを用いることにより、基板外周辺の熱抵
抗を大きくシ、基板外周辺のメルト内での微結晶の析出
を抑制し、均一な厚みの成長結晶が得られる。[Effects of the Invention] As described above, by using a cavity and a liquid metal whose temperature can be easily uniformized by thermal convection, the thermal resistance around the outside of the substrate can be increased, and the microcrystals in the melt around the outside of the substrate can be increased. Precipitation is suppressed, and grown crystals with uniform thickness can be obtained.
従って、均一な発光効率の発光ダイオード用エピタキシ
ャルウェーへが高歩留まりで製造され。Therefore, epitaxial wafers for light emitting diodes with uniform luminous efficiency can be manufactured with high yield.
安価に大量に高発光効率の発光ダイオードを供給するこ
とができる。Light-emitting diodes with high luminous efficiency can be supplied in large quantities at low cost.
第1図は本発明の1実施例による液相結晶成長装置の部
分概略図、第2図は第1図の部分横断面図、第3図は成
長層の膜厚分布の測定例、第4図は従来の液相結晶成長
装置の概略図、第5図は第4図の部分拡大図、第6図は
成長操作を説明する温度対時間のグラフ、第7図は従来
技術の液相結晶装置の部分拡大図、第8図は第7図の横
断面図。
第9図は従来技術の液相結晶装置の部分拡大図。
第10図は第9図の横断面図、第11図は従来技術によ
る成長層の膜厚測定例である。
符号の説明
11 メルト槽
13 メルト
17 スライダの凹部
19 基板
21 スライダ
25 空洞
27 凸部
2つ
連絡孔
液体金属
空間FIG. 1 is a partial schematic diagram of a liquid phase crystal growth apparatus according to an embodiment of the present invention, FIG. 2 is a partial cross-sectional view of FIG. 1, FIG. 3 is an example of measuring the thickness distribution of a grown layer, and FIG. The figure is a schematic diagram of a conventional liquid phase crystal growth apparatus, Figure 5 is a partially enlarged view of Figure 4, Figure 6 is a graph of temperature vs. time to explain the growth operation, and Figure 7 is a conventional liquid phase crystal growth apparatus. FIG. 8 is a partially enlarged view of the device, and FIG. 8 is a cross-sectional view of FIG. 7. FIG. 9 is a partially enlarged view of a conventional liquid phase crystallization device. FIG. 10 is a cross-sectional view of FIG. 9, and FIG. 11 is an example of measuring the thickness of a grown layer according to the prior art. Explanation of symbols 11 Melt tank 13 Melt 17 Slider recess 19 Substrate 21 Slider 25 Cavity 27 Two protrusions, communication hole Liquid metal space
Claims (2)
有し耐熱材料で作られたメルト槽と結晶基板を上に保持
した耐熱材料で作られたスライダーとを用い、メルト内
に上部が下部より高温となるように温度差を付け基板を
メルト槽の開口と接するようにスライダーを移動し、メ
ルト槽の開口の位置で基板をメルトと接触させ基板上に
メルトから結晶をエピタキシャル成長させる温度差法の
液相の結晶成長方法において、基板の下方のスライダの
内部に、基板面積より大きい外周部を有し、外部と孔で
通じている空洞を設け空洞の上壁に基板とほぼ同じ横断
面積を持ち、下方に延びる凸部を形成し、この空洞に成
長温度で液状となる金属を収容し、基板の真下において
、前記の液状金属の上表面と前記凸部とを接触させ、か
つ凸部周辺の液状金属の上面には空間を形成して、熱の
流れを制御することを特徴とする液相の結晶成長方法。(1) Using a melt tank made of heat-resistant material with an opening at the bottom that holds the melt containing the growth material, and a slider made of heat-resistant material that holds the crystal substrate on top, the upper part is placed inside the melt. Apply a temperature difference so that the temperature is higher than the lower part, move the slider so that the substrate is in contact with the opening of the melt tank, bring the substrate into contact with the melt at the opening of the melt tank, and make the temperature difference to epitaxially grow crystals from the melt on the substrate. In the liquid phase crystal growth method, a cavity is provided inside the slider below the substrate and has an outer circumference larger than the area of the substrate and communicates with the outside through a hole, and the upper wall of the cavity has a cross-sectional area approximately equal to that of the substrate. a convex portion extending downward; a metal that becomes liquid at the growth temperature is accommodated in the cavity; an upper surface of the liquid metal is brought into contact with the convex portion directly below the substrate; A liquid phase crystal growth method characterized by forming a space on the upper surface of the surrounding liquid metal to control the flow of heat.
口を有し耐熱材料で作られたメルト槽と、結晶基板を上
に保持し、耐熱材料で作られたスライダとを備え、メル
ト内に上部が下部より高温となるように温度差をつけ、
基板をメルト槽の開口と接するようにスライダーを移動
し、メルト槽の開口の位置で基板をメルトと接触させ基
板上にメルトから結晶をエピタキシャル成長させる温度
差法の液相の結晶成長装置において、基板の下方のスラ
イダの内部に、基板面積より大きい外周部を有し、外部
と孔で通じている空洞を設け、空洞の上壁に基板とほぼ
同じ横断面積を持ち、下方に延びる凸部を形成し、この
空洞に成長温度で液状となる金属を収容した時基板の真
下において、前記の液状金属の上表面と前記凸部とが接
触し、凸部周辺の液状金属の上面には空間が形成されて
、熱の流れを制御するごとく構成されていることを特徴
とする液相の結晶成長装置。(2) A melt tank that holds a melt containing melted growth materials, has an opening at the bottom and is made of a heat-resistant material, and a slider that holds a crystal substrate on top and is made of a heat-resistant material; Create a temperature difference inside so that the top is hotter than the bottom,
In a liquid phase crystal growth apparatus using a temperature difference method, a slider is moved so that the substrate is in contact with the opening of the melt tank, and the substrate is brought into contact with the melt at the position of the opening of the melt tank, and crystals are epitaxially grown from the melt on the substrate. Inside the lower slider is a cavity that has an outer periphery larger than the substrate area and communicates with the outside through a hole, and a convex part that has approximately the same cross-sectional area as the substrate and extends downward is formed on the upper wall of the cavity. However, when a metal that becomes liquid at the growth temperature is placed in this cavity, the upper surface of the liquid metal comes into contact with the convex portion directly below the substrate, and a space is formed on the upper surface of the liquid metal around the convex portion. 1. A liquid phase crystal growth apparatus characterized in that the apparatus is configured to control the flow of heat.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33311087A JPH0222196A (en) | 1987-12-29 | 1987-12-29 | Liquid phase crystal growth method and apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33311087A JPH0222196A (en) | 1987-12-29 | 1987-12-29 | Liquid phase crystal growth method and apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0222196A true JPH0222196A (en) | 1990-01-25 |
| JPH0566916B2 JPH0566916B2 (en) | 1993-09-22 |
Family
ID=18262394
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP33311087A Granted JPH0222196A (en) | 1987-12-29 | 1987-12-29 | Liquid phase crystal growth method and apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0222196A (en) |
-
1987
- 1987-12-29 JP JP33311087A patent/JPH0222196A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0566916B2 (en) | 1993-09-22 |
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