JPH0566916B2 - - Google Patents
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- Publication number
- JPH0566916B2 JPH0566916B2 JP33311087A JP33311087A JPH0566916B2 JP H0566916 B2 JPH0566916 B2 JP H0566916B2 JP 33311087 A JP33311087 A JP 33311087A JP 33311087 A JP33311087 A JP 33311087A JP H0566916 B2 JPH0566916 B2 JP H0566916B2
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- Japan
- Prior art keywords
- substrate
- melt
- growth
- slider
- temperature
- Prior art date
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- 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】
[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
熱して溶解し、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ツク
バーガ法、ブリツ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, Bridgeman 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
義にはフローテイングゾーン法も含むが、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
配と拡散によつ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、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℃で10℃−200℃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 provided within a solution (melt), and the solute is dissolved (supplied) in the high temperature part, and the solute is precipitated from the supersaturated solution in the low temperature part. In other words, in the temperature difference liquid phase crystal growth method, a temperature difference is applied to a solution (melt) in which a growth material (solute) is dissolved, and the solute is transported toward the substrate by the temperature gradient and diffusion, thereby forming crystals on the substrate. This is a method of growing crystals at a constant temperature, which allows a large number of crystals with uniform impurity concentration and composition and good crystallinity to be obtained in succession.
For example, in the case of GaAlAs-based crystals, a melt made of Ga solution is placed in a melt bath made of graphite,
Crystal growth is performed at 800℃-1000℃ with a temperature difference of 10℃-200℃. Using this method, light emitting diodes, lasers, etc. 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。[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 a temperature difference perpendicular to the surface and a uniform temperature within the surface.
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に温度分布を均一にしようと
していた。 Conventionally, as shown in Japanese Patent Publication No. 59-43087, attempts have been made to make the temperature distribution uniform within the substrate surface by balancing the heating furnace and the cooling source.
しかし、これらの方法で均一温度分布を実現す
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 with these methods, and the growth results often have an uneven thickness distribution as shown in Figure 11. In addition, slight differences and fluctuations in the growth system of the furnace body cause the thickness to vary. The distribution will fluctuate.
このような均一でない厚み分布は、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。 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 reduced production yield.
そこで、本発明の目的は均一な面内温度分布を
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。 Therefore, an object of the present invention is to provide a temperature difference method liquid phase crystal growth technique that can realize a uniform in-plane temperature distribution.
[問題点を解決するためにおこなつた検討]
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, the mechanism of crystal growth in continuous liquid phase crystal growth using the temperature difference method was investigated.
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を通つて押
し上げられる。入口側予備室51は予備加熱炉5
9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の下部でメルト
と接触した結晶成長を行う。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7
7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。 FIG. 4 schematically shows an example of a temperature difference method liquid phase 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 push-up mechanism 55 . The entrance side preliminary chamber 51 is a preliminary heating furnace 5
Preferably, it is preheated at 9. 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 the main heater 67 heats the melt tank 64. The substrate 69 on the slider 53 contacts the melt at the bottom of the melt tank 64 and undergoes crystal growth. The slider carrying the substrate on which crystal growth has been completed is sent to the outside of the growth chamber 57 via the gate valve 73, and is sent to the slider receiving mechanism 7.
7 and is stored in the outlet side preliminary chamber 79 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。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中のAlの量はPメルト槽65中
のAlの量より大きくするのがよい。たとえば、
赤色発光Ga1-xAlxAs発光ダイオードを得るには、
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、800℃−1000℃の温度で温度差を10℃−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か溶質収容部
を作つ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。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。 FIG. 5 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. Further, as impurities, Zn is dissolved in the P melt tank 65 and Te is dissolved in the N melt tank. 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 preferably made larger than the amount of Al in the P-melt tank 65. for example,
To obtain the 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, at a temperature of 800℃-1000℃, the temperature difference is 10℃-200℃
establish. To continuously supply the solute, the solute is floated above the melt, which is a high-temperature part, or a solute storage part is created and 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. 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. A large number of substrates 69 are transferred to such a melt low temperature section.
are brought into contact sequentially. For example, with a growth time of about 60 minutes,
A growth layer of 50-60 μm is obtained.
第6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
板上にエピタキシヤル成長を行う。 FIG. 6 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 is
The second substrate should touch the bottom of the P-melt. 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アイトであるメ
ルト槽を作つ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
ア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た。 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 achieve uniform in-plane temperature distribution at the bottom of the melt is the relationship between the melt surrounded by graphite and the substrate. Therefore, we considered 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。これはメルト層の内壁からは溶質の供
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(グラフアイト)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。したがつて温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 FIGS. 7 and 8) The growth rate of the peripheral portion 83 is slower than that of the vicinity 81 of the substrate center. One reason for this is thought to be that no solute is supplied from the inner wall of the melt layer. Further, the thermal conductivity of the side wall of the melt tank (graphite) is higher than that of the melt (Ga). Therefore, the temperature gradient in the peripheral portion 83 is smaller than that in the vicinity 81 of the substrate center. Therefore, the temperature gradient is small and the peripheral area 83
It is thought that the growth rate 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[A]に比べ大きくない。また基板面
内の温度分布も[A]に比べより均一である。し
たがつて成長速度は[A]より面内で比較的均一
になる。[B: When the size of the bottom of the melt is larger than the size of the substrate] (See Figures 9 and 10) Since the size of the substrate is smaller than the size of the bottom of the melt, the peripheral part 87 of the substrate is also separated from the side wall of the melt tank. The difference in temperature gradient between the center area 85 of the separated substrate and the peripheral area 87 of the substrate is not large compared to [A]. Moreover, the temperature distribution within the substrate surface is also more uniform than in [A]. Therefore, the growth rate becomes relatively uniform within the plane than in [A].
しかし、基板より外の周辺部89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
をエピタキシヤル成長させることのできないグラ
フアイトからなるスライダ53に接している。し
たがつて基板外の周辺部89において基板面内8
5,87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つて流れる。すなわち、
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。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。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8
7の成長速度が小さくなる。 However, the bottom surface of the melt in the peripheral portion 89 outside the substrate is in contact with the slider 53 made of graphite, which has a higher thermal conductivity than the substrate and on which crystals cannot be epitaxially grown. Therefore, in the peripheral part 89 outside the board, the inside of the board 8
5, 87, or more heat flows from the melt toward the slider. That is,
Even in this region, solute transport by diffusion is always occurring. However, since there are no substrate crystals, the transported solute becomes supersaturated, causing microcrystals to precipitate in the melt near the slider surface. Since the solute is constantly being transported, these microcrystals serve as seeds and are continuously precipitated into microcrystals. Due to the precipitation of microcrystals within the melt in the peripheral area 89 outside the substrate, solute transport in the internal peripheral area 87 of the substrate is affected, and compared to the central area 85 , the transport of solutes in the internal peripheral area 87 of the substrate is affected.
7 growth rate becomes smaller.
[A][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[A][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。 [A] [B] In either case, growth with a uniform thickness distribution is not achieved, and for example, as shown in FIG. 11, the growth thickness at the periphery tends to be smaller than at the center. Furthermore, in both [A] and [B], if temperature fluctuation occurs due to slider movement, 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89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 melt in the outer peripheral portion 89 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続させ、その外側の上
壁は高くして液体金属と接続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 stored in the cavity, and a step is provided on the upper wall of the cavity to form a downward convex portion directly below the substrate, so that the surface area is approximately the same as that of the substrate. The upper wall on the outside thereof is made high so as not to be connected to the liquid metal, but to form a space on the upper surface of 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横断面
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
金属が熱対流によつて移動するため、基板面内方
向に温度分布があつても均熱化される。[Function] To explain with reference to FIGS. 1 and 2, a cavity with a cross-sectional area larger than the substrate area is provided inside the slider below the substrate, and a metal that becomes liquid at the crystal growth temperature (liquid metal) is placed in the cavity. Since this liquid metal moves by thermal convection, even if there is a temperature distribution in the in-plane direction of the substrate, the temperature is equalized.
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ず、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基板外の周辺部89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, the liquid metal does not contact the upper wall surface of the cavity, and a gas space is provided on the upper surface of the liquid metal. Therefore, the thermal resistance in the direction perpendicular to the substrate surface in the peripheral area 89 outside the substrate where the melt is in direct contact with the slider is
The peripheral portion 89 outside the board is larger than the thermal resistance at
The heat flowing through 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。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つてい
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。従つて半導体基板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
レール(図示せず)を摺動し、図面の紙面と垂直
の方向の動く。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
大きめとしてあるが、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。この凸部2
7は基板19ないしスライダの凹部17とほぼ同
じ横断面積をも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が残つている。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3
1の中になかば没する。 Inside the melt tank 11 is a melt 13 for crystal growth.
is accommodated. The bottom of the melt tank 11 is open, and the slider 21 closes the bottom opening. 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 covered with the melt 13.
It touches the center of the bottom. 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. Although the lateral dimension of the cavity is slightly larger than the bottom area of the melt 13 in this embodiment, it is not limited thereto. However, it is preferable that the cross-sectional area is approximately the same as or larger than the cross-sectional area of the melt 13. A downward protrusion 27 is formed on the upper wall of the cavity 25 . This convex part 2
7 is designed to have approximately the same cross-sectional area as the substrate 19 or the recess 17 of the slider and 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 a 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 rises, the space 33 gradually becomes smaller, and the convex part 27 becomes the liquid metal 3.
Halfway down in 1.
メルト槽11、スライダ21はグラフアイトの
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、GaAlAsP、
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(ほぼ
結晶成長温度)で液体であれば良く、Ga、In、
Hg等が用いられる。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。 The melt tank 11 and slider 21 are 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, GaAlAsP,
Ga is used for GaP, GaSb, etc., and In is used for InAs, InAsP, etc. The liquid metal 31 only needs to be liquid at the operating temperature (approximately the crystal growth temperature), and may be Ga, In,
Hg etc. are used. 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 impurity prevention, thermal design, etc. In order to obtain crystal growth with a uniform thickness, it is desirable that the temperature distribution on the substrate 19 be uniform within the plane and the temperature gradient be uniform within the plane, and furthermore, it is desirable that no microcrystals occur in the portion 89 outside the substrate 19. . For this purpose, it is desirable that a uniform heat flow flows from top to bottom within the cross-sectional area of the substrate 19, and that the heat flow is restricted outside the cross-sectional area.
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)、
液体金属31、スライダ21下部と熱が流れる。
その外側ではスライダ21上部に凸部27が存在
せず、代わりに気体空間33が入る。 First, within the cross-sectional area of the substrate 19, the melt 13 is applied from above.
Substrate 19, upper part of slider 21 (including convex portion 27),
Heat flows through the liquid metal 31 and the lower part of the slider 21.
On the outside thereof, the convex portion 27 does not exist on the top of the slider 21, and a gas space 33 enters 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つても熱を
輸送できるので、温度分布に不均一が生じた場合
対流によつ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 the 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89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. Since the thermal conductivity of gases is much lower than that of refractory materials such as graphite, heat flow is greatly restricted. Therefore, precipitation of microcrystals in the portion 89 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/cm−deg]の代表例は以下の通り
である。 For example, typical examples of the thermal conductivity (300°K) [W/cm-deg] of the constituent materials of the crystal growth apparatus are as follows.
H2 0.0018
Ga 0.335
グラフイト 1.2
GaAs 0.54
この液体金属31の熱対流による均熱化と基板
外の周辺領域89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。 H 2 0.0018 Ga 0.335 Graphite 1.2 GaAs 0.54 By equalizing the temperature by thermal convection of the liquid metal 31 and suppressing the precipitation of microcrystals in the peripheral region 89 outside the substrate, a grown crystal with a uniform thickness as shown in FIG. 3 is grown. can get.
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
なつても内部圧力が上昇する危険はない。 Furthermore, since the space provided on the upper surface of the liquid metal is connected to the outside atmosphere through the pores, there is no risk of internal pressure increasing even at high temperatures.
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89
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, by adjusting the volume of the space 33 on the upper surface of the liquid metal in the peripheral area, the outer peripheral area 89 of the substrate can be adjusted.
It is also possible to adjust the thermal resistance in the direction perpendicular to the substrate plane, and to compensate for differences in growth conditions due to slight differences in growth systems such as heating furnaces and cooling sources.
この方法は、GaAlAsのみならず、
GaPGaAsInP、InP、InGaAsP、あるいは、
ZnSe、ZnTe、HgCdTeその他の温度差法液相エ
ピタキシヤル成長法による結晶の成長に適用でき
る。 This method is applicable not only to GaAlAs but also to
GaPGAAsInP, InP, InGaAsP, or
It can be applied to the growth of ZnSe, ZnTe, HgCdTe, and other crystals by temperature difference liquid phase epitaxial growth.
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.
[発明の効果]
以上のように、空洞と熱対流によつても均熱化
を達しやすい液体金属とを用いることにより、基
板周辺の熱抵抗を大きくし、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 that can easily achieve temperature uniformity through thermal convection, the thermal resistance around the substrate is increased, and the microscopic temperature inside the melt around the outside of the substrate is increased. Precipitation of crystals is suppressed and grown crystals with uniform thickness can be obtained.
従つて、均一な発光効率の発光ダイオード用エ
ピタキシヤルウエーハが高歩留まりで製造され、
安価に大量に高発光効率の発光ダイオードいを供
給することができる。 Therefore, epitaxial wafers for light emitting diodes with uniform luminous efficiency can be manufactured with high yield.
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、2
1……スライダ、25……空洞、27……凸部、
29……連絡孔、31……液体金属、33……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, third is an example of measuring the film thickness distribution of a grown layer, and FIG. is a schematic diagram of a conventional liquid phase crystal growth apparatus, and FIG.
6 is a graph of temperature vs. time to explain the growth operation, FIG. 7 is a partially enlarged view of a conventional liquid phase crystallization device, and FIG. 8 is a cross-sectional view of FIG. 7.
Figure 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, 2
1...Slider, 25...Cavity, 27...Protrusion,
29...Communication hole, 31...Liquid metal, 33...Space.
Claims (1)
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
結晶をエピタキシヤ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。 2 成長用材料を溶解したメルトを保持し、底部
に開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を
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ヤ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。[Scope of Claims] 1. A melt tank made of a heat-resistant material that holds a melt containing a growth material and has an opening at the bottom, and a slider made of a heat-resistant material that holds a crystal substrate on top. Move the slider so that the substrate is in contact with the opening of the melt tank, and then bring the substrate into contact with the melt at the opening of the melt tank to collect crystals from the melt onto the substrate. In the liquid phase crystal growth method using the temperature difference method for epitaxial growth, a cavity is provided inside the slider below the substrate, the outer periphery of which is larger than the area of the substrate, and which communicates with the outside through a hole. A convex portion having approximately the same cross-sectional area as the substrate and extending downward is formed, a metal that becomes liquid at the growth temperature is contained in this cavity, and the upper surface of the liquid metal and the convex portion are formed directly below the substrate. A liquid phase crystal growth method characterized by controlling the flow of heat by contacting the liquid metal and forming a space on the upper surface of the liquid metal around the convex portion. 2. It is equipped with a melt tank made of a heat-resistant material and with an opening at the bottom that holds the melt containing the growth material, and a slider made of the heat-resistant material that holds the crystal substrate on top. Create a temperature difference so that the upper part 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 epitaxy crystals from the melt onto the substrate. In a liquid phase crystal growth apparatus using the temperature difference method for dual growth, a cavity is provided inside the slider below the substrate, the outer periphery of which is larger than the area of the substrate, and which communicates with the outside through a hole. A convex portion having approximately the same cross-sectional area as the substrate and extending downward is formed, and when a metal that becomes liquid at the growth temperature is contained in this cavity, the upper surface of the liquid metal and the convex portion are formed directly below the substrate. 1. A liquid phase crystal growth apparatus characterized in that a space is formed on the upper surface of the liquid metal in contact with the convex portion 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 JPH0222196A (en) | 1990-01-25 |
| JPH0566916B2 true 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 |
|---|---|
| JPH0222196A (en) | 1990-01-25 |
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