JPH0566914B2 - - Google Patents
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- Publication number
- JPH0566914B2 JPH0566914B2 JP33310887A JP33310887A JPH0566914B2 JP H0566914 B2 JPH0566914 B2 JP H0566914B2 JP 33310887 A JP33310887 A JP 33310887A JP 33310887 A JP33310887 A JP 33310887A JP H0566914 B2 JPH0566914 B2 JP H0566914B2
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- Japan
- Prior art keywords
- substrate
- melt
- slider
- heat
- contact
- 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]
本発明は液相結晶に成長し、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 grows into a liquid phase crystal, and in particular, creates a certain temperature difference in the melt in which the solute is dissolved, so that the solute is continuously transferred from the high temperature area to the 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 area by transport.
[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
勾配による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℃−20℃の温度差
を設けて結晶成長を行う。この方法により、特性
の優れた発光ダイオードやレーザー等が製作され
ている。 The temperature difference method is a method in which a high-temperature 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), and the solute is dissolved (supplied) in the high-temperature part, while the solute is precipitated from the supersaturated solution in the low-temperature part. That is,
In the temperature difference method liquid phase crystal growth method, the growth material (solute)
This method creates a temperature difference in a solution (melt) in which the solute is dissolved, transports the solute toward the substrate by diffusion due to the temperature gradient, and grows crystals on the substrate. Because it can grow at a constant temperature, it can achieve a uniform impurity concentration and composition. This method allows a large number of crystals with good crystallinity to be obtained in succession. For example, in the case of a GaAlAs-based crystal, a melt made of a Ga solution is placed in a melt bath made of graphite, and crystal growth is performed at a temperature of 800°C to 1000°C with a temperature difference of 10°C to 20°C. Using this method, light emitting diodes, lasers, etc. with excellent characteristics are manufactured.
[発明が解決しようとする問題点]
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の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 within the substrate surface uniform by balancing the heating furnace and the cooling source.
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12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 12. 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、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 a temperature difference method was investigated.
第5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63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
と接触し結晶成長を行う。結晶成長の終わつた基
板を載せたスライダはゲートバルブ73を介して
成長室57の外に送られ、スライダ受取機構77
によつてゲートバルブ74をあして出口側予備室
79に収められる。 FIG. 5 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 63 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 comes into contact with the melt at the bottom of the melt tank 64 to cause crystal growth. The slider carrying the substrate on which the crystal growth has been completed is sent out of the growth chamber 57 via the gate valve 73, and is sent to the slider receiving mechanism 77.
It is stored in the outlet side preliminary chamber 79 after passing through the gate valve 74.
第6図はメルト槽64部分の1例の拡大説明図
である。溶媒であるGaの中に溶質のAl、GaAs
が溶解されて、Pメルト槽65とNメルト槽66
に収容されている。さらに不純物としてPメルト
槽65にはZnがNメルト槽には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GaAl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. 6 is an enlarged explanatory view of one example of the melt tank 64 portion. Solutes Al and GaAs in the solvent Ga
is melted, and the P melt tank 65 and the N melt tank 66
is housed in. 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 GaAl 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7図は温度と時間との関係を示す。図から判
るように温度分布は一定に保たれる。初め1番目
の基板がPメルトの下に接し、P型層を成長させ
る。次にスライダを移動させて1番目の基板がN
メルトの下に接し、2番目の基板がPメルトの下
に接するようにする。そこで、それぞれの成長層
を形成する。これで1番目の基板上には下にP型
層、上にN型層が成長され、ダイオードが形成さ
れる。この様な操作を繰り返して多数枚の基板上
にエピタキシヤル成長を行う。 FIG. 7 shows the relationship between temperature and time. As can be seen from the figure, the temperature distribution remains constant. Initially, the first substrate contacts the bottom of the P melt and grows a P type layer. Next, move the slider so that the first board 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8図、第9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 approximately equal] (see FIGS. 8 and 9) 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 tank. 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 concentration 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10図、第11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]によ比べより均一ある。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 10 and 11) 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]. Also, the temperature distribution within the substrate surface is 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の分布
の成長が実現されず、たとえば、第12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. 12, 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、基板の下方の冷却板の内部に基板面積より大
きい外周部の空洞を設け、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、基板
とほぼ同じ横断面積にわたり、上壁面が液体金属
の上表面と接触し、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 the temperature difference method liquid phase crystal growth, a cavity is provided in the outer circumferential portion of the cooling plate below the substrate, which is larger than the area of the substrate, and the growth temperature is controlled in this cavity. A step is provided on the upper wall of this cavity so that the upper wall is in contact with the upper surface of the liquid metal over approximately the same cross-sectional area as the substrate, and the upper wall is in contact with the upper surface of the liquid metal. The upper wall surface is made high so that it does not come into contact with the liquid metal and a space is formed above the liquid metal, and this space is connected to the outside through pores.
[作用]
第1図、第2図を参照して説明すると、基板の
下方の冷却板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(液相金属)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。[Operation] 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 cooling plate below the substrate, and a metal that becomes liquid at the crystal growth temperature (liquid phase metal) is formed in the cooling plate below the substrate. ), and this liquid metal moves by thermal convection, so 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、基板とほぼ同じ表面積
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。その外側の冷却板部材の
空洞上壁面と接していない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89に
おける基板面に垂直方向の熱抵抗は、基板部8
5,87における熱抵抗より大きく、基板外の周
辺部89に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 surface area as the substrate, thereby forming a heat flow path. A gas space is provided on the upper surface of the liquid metal that is not in contact with the upper cavity wall surface of the outer cooling plate member. 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
5 and 87, and can suppress heat flowing to the peripheral portion 89 outside the substrate.
[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15が底の開口を塞ぐようになつてい
る。スライダ15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。スライダは冷却板21の
凹状レール23内を摺動し、図面の紙面と垂直の
方向に動く、冷却板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
は本実施例ではスライダ15とほぼ同じ寸法とし
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27は基板1
9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31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 15 closes the bottom opening. A recess 17 is provided in the center of the slider 15, 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 in a concave rail 23 of a cooling plate 21 and moves in a direction perpendicular to the plane of the drawing, and a cavity 25 is formed in the interior of the cooling plate below the melt bath. Although the lateral dimension of the cavity is approximately the same as that of the slider 15 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 portion 27 is
It is designed to have approximately the same cross-sectional area as the recess 9 or the recess 17 of the slider and a horizontal lower surface. Furthermore, a communication hole 29 is formed to connect the outside of the cavity 25, allowing liquid metal and atmospheric gas to enter and exit. A liquid metal (for example, Ga) 31 is placed in the cavity 25.
As the liquid is added, 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15、冷却板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、その外側では上から下に
の熱流が制限されることが望ましい。 The melt tank 11, slider 15, and cooling plate 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,
For GaAlAsP, GaP, GaSb, etc., Ga, InAs,
In the case of InAsP etc., In is used. The liquid metal 31 only needs to be liquid at the operating temperature (approximately the crystal growth temperature), and 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, the temperature distribution on the substrate 19 must be uniform within the plane, and the temperature gradient must also be uniform within the plane, and furthermore, microcrystals must not be generated in the portion 89 outside the substrate 19. is desirable.
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 heat flow from top to bottom 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5、冷却板21上部(凸部2
7を含む)、液体金属31、冷却板21下部と熱
が流れる。その外側では冷却板21上部に凸部2
7が存在せず、代わりに空間33が入る。 First, within the cross-sectional area of the substrate 19, the melt 13 is applied from above.
Board 19, slider 5, upper part of cooling plate 21 (convex part 2
7), the liquid metal 31, and the lower part of the cooling plate 21. On the outside, a convex portion 2 is formed on the upper part of the cooling plate 21.
7 does not exist, and 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アイト等の
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 heat-resistant 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、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, the thermal conductivity of the constituent materials (300°K)
Representative examples of [W/cm·deg] are as follows.
H2 0.018
Ga 0.335
グラフアイト 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
外周辺領域89における微結晶析出の抑制によ
り、均一な厚さの成長結晶が得られる。 H2 0.018 Ga 0.335 Graphite 1.2 GaAs 0.54 By equalizing the temperature of the liquid metal 31 by thermal convection and suppressing the precipitation of microcrystals in the peripheral region 89 outside the substrate, a grown crystal with a uniform thickness can be obtained.
期待される成長結晶の膜厚分布の1例を第3図
に示す。 An example of the expected thickness distribution of the grown crystal is shown in FIG.
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.
また、液面を上下できるようにして液面を下げ
て凸部27でも液面から冷却板21の上部を離す
と、熱流を一時的に制限することもできる。 Further, by lowering the liquid level so that the liquid level can be moved up and down and separating the upper part of the cooling plate 21 from the liquid level at the convex portion 27, the heat flow can be temporarily restricted.
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.
P層N層を連続的に成長して発光ダイオード用
ウエーハを製造する場合の実施例を第4図に示
す。 FIG. 4 shows an example in which a wafer for light emitting diodes is manufactured by continuously growing P layers and N layers.
石英製の反応管35内にグラフアイト製の結晶
成長機構37が収容され、ヒータ38,39で加
熱されている。冷却板21上をスライダ15が滑
つて図中の右から左へ移行する。スライダ15上
の基板19はまずPメルト41の下でP層の成長
を受け、次にNメルト42の下でN層の成長を受
ける。各メルト下部には空洞43,44が設けら
れ、その上壁からはほぼ基板19とおなじ断面形
状の凸部45,46が基板19と位置を合わせ下
方に延びている。液体金属31が凸部45,46
と接し、その外周には空間47,48を作る。メ
ルト41,42内には図中右に示すような垂直方
向の一定の温度勾配を形成する。 A crystal growth mechanism 37 made of graphite is housed in a reaction tube 35 made of quartz and heated by heaters 38 and 39. The slider 15 slides on the cooling plate 21 and moves from right to left in the figure. Substrate 19 on slider 15 first undergoes P layer growth under P melt 41 and then N layer growth under N melt 42. Cavities 43 and 44 are provided in the lower part of each melt, and convex portions 45 and 46 having approximately the same cross-sectional shape as the substrate 19 extend downward from the upper wall thereof, aligned with the substrate 19. Liquid metal 31 forms convex portions 45 and 46
, and spaces 47 and 48 are created around its outer periphery. A constant temperature gradient in the vertical direction is formed in the melts 41 and 42 as shown on the right side of the figure.
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, crystallization 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
板外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 outside of the substrate is increased, and the temperature inside the melt around the outside of the substrate is increased. Precipitation of microcrystals 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図は成長層の膜厚分布の例、第4図は他
の実施例による液相結晶成長装置の部分概略図、
第5図は従来の液相結晶成長装置の概略図、第6
図は第5図の部分拡大図、第7図は成長操作を説
明する温度対時間のグラフ、第8図は従来技術の
液相結晶装置の部分拡大図、第9図は第8図の横
断面図、第10図は従来技術の液相結晶装置の部
分拡大図、第11図は第10図の横断面図、第1
2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、15……スライダ、17……スライダの凹
部、19……基板、21……冷却板、23……冷
却板の凹状レール、25……空洞、27……凸
部、29……連絡孔、31……液体金属、33…
…空間、35……反応管、37……結晶成長機
構、38……ヒータ、39……ヒータ、41……
Pメルト、42……Nメルト、43……空洞、4
4……空洞、45……凸部、46……凸部、47
……空間、48……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 the film thickness distribution of the grown layer, and FIG. 4 is a partial schematic diagram of a liquid phase crystal growth apparatus according to another embodiment,
Figure 5 is a schematic diagram of a conventional liquid phase crystal growth apparatus;
The figure is a partially enlarged view of Fig. 5, Fig. 7 is a graph of temperature versus time to explain the growth operation, Fig. 8 is a partially enlarged view of a conventional liquid phase crystallization device, and Fig. 9 is a cross section of Fig. 10 is a partially enlarged view of a conventional liquid phase crystal device, FIG. 11 is a cross-sectional view of FIG. 10, and FIG.
FIG. 2 shows an example of measuring the thickness of a grown layer using the conventional technique. Explanation of symbols, 11...Melt tank, 13...Melt, 15...Slider, 17...Slider recess, 19...Substrate, 21...Cooling plate, 23...Concave rail of cooling plate, 25... Cavity, 27...Protrusion, 29...Communication hole, 31...Liquid metal, 33...
...Space, 35...Reaction tube, 37...Crystal growth mechanism, 38...Heater, 39...Heater, 41...
P melt, 42...N melt, 43...Cavity, 4
4...Cavity, 45...Protrusion, 46...Protrusion, 47
...Space, 48...Space.
Claims (1)
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
ーと、このスライダーをメルト槽の開口側に摺動
可能に保持接触させる耐熱材料で作られた冷却板
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液相
結晶成長法において、基板の下方の冷却板の内部
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、このスライダをメルト槽の開口部に摺動可
能に保持接触させる耐熱材料で作られた冷却板と
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ヤル成長させる温度差法の液
相結晶成長装置において、基板の下方の冷却板の
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
相結晶成長装置。[Claims] 1. A melt tank made of a heat-resistant material and having an opening at the bottom and holding a melt containing a growth material; a slider holding a crystal substrate on top and made of a heat-resistant material; This slider is slidably held and brought into contact with the opening side of the melt tank using a cooling plate made of heat-resistant material, and a temperature difference is created in the melt so that the upper part is higher than the lower part. In the temperature difference liquid phase crystal growth method, in which the substrate is brought into contact with the melt at the opening of the melt tank and crystals are epitaxially grown from the melt on the substrate, the slider is moved so that it is in contact with the cooling plate below the substrate. There is a cavity inside 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. A metal that becomes liquid at a certain temperature is contained, and the upper surface of the liquid metal is brought 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, so that heat can be removed. A liquid phase crystal growth method characterized by controlling flow. 2. A melt tank that holds the melt containing the growth material and is made of heat-resistant material and has an opening at the bottom; a slider that holds the crystal substrate on top and is made of heat-resistant material; and this slider is connected to the melt tank. A cooling plate made of a heat-resistant material is slidably held in contact with the opening of the melt tank, and a temperature difference is created in the melt so that the upper part is hotter than the lower part, and the board is brought into contact with the opening of the melt tank. In a liquid phase crystal growth apparatus using a temperature difference method in which a slider is moved to bring the substrate into contact with the melt at the opening of the melt tank and crystals are epitaxially grown from the melt onto the substrate, a cooling plate is placed below the substrate. A cavity is provided which has an outer periphery larger than the substrate area and communicates with the outside through a hole, and a convex portion having approximately the same cross-sectional area as the substrate and extending downward is formed on the upper wall of the cavity. When the liquid metal is contained, the upper surface of the liquid metal contacts the convex portion directly below the substrate, and a space is formed on the upper surface of the liquid metal around the convex portion to control the flow of heat. A liquid phase crystal growth apparatus characterized by being configured as follows.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33310887A JPH0222194A (en) | 1987-12-29 | 1987-12-29 | Method for liquid-phase crystal growth and apparatus therefor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33310887A JPH0222194A (en) | 1987-12-29 | 1987-12-29 | Method for liquid-phase crystal growth and apparatus therefor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0222194A JPH0222194A (en) | 1990-01-25 |
| JPH0566914B2 true JPH0566914B2 (en) | 1993-09-22 |
Family
ID=18262373
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP33310887A Granted JPH0222194A (en) | 1987-12-29 | 1987-12-29 | Method for liquid-phase crystal growth and apparatus therefor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0222194A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0675257A (en) * | 1992-07-30 | 1994-03-18 | Internatl Business Mach Corp <Ibm> | Nonlinear optics device |
-
1987
- 1987-12-29 JP JP33310887A patent/JPH0222194A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0222194A (en) | 1990-01-25 |
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