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JPS6353158B2 - - Google Patents
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JPS6353158B2 - - Google Patents

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Publication number
JPS6353158B2
JPS6353158B2 JP54061829A JP6182979A JPS6353158B2 JP S6353158 B2 JPS6353158 B2 JP S6353158B2 JP 54061829 A JP54061829 A JP 54061829A JP 6182979 A JP6182979 A JP 6182979A JP S6353158 B2 JPS6353158 B2 JP S6353158B2
Authority
JP
Japan
Prior art keywords
epitaxial layer
solution
reaction system
impurity
impurities
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP54061829A
Other languages
Japanese (ja)
Other versions
JPS55154399A (en
Inventor
Morio Inoe
Tamotsu Uragaki
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP6182979A priority Critical patent/JPS55154399A/en
Publication of JPS55154399A publication Critical patent/JPS55154399A/en
Publication of JPS6353158B2 publication Critical patent/JPS6353158B2/ja
Granted legal-status Critical Current

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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】 本発明は、1つの溶液槽を使用し、一導電型の
エピタキシヤル層と、さらにこの上に、これとは
逆導電型のエピタキシヤル層または同一導電型で
低不純物濃度のエピタキシヤル層を連続的に成長
させる方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention uses one solution bath, and forms an epitaxial layer of one conductivity type and an epitaxial layer of the opposite conductivity type or an epitaxial layer of the same conductivity type with low impurity. The present invention relates to a method for continuously growing a concentrated epitaxial layer.

液相エピタキシヤル成長方法は、―族化合
物半導体基板上に砒化ガリウム(GaAs),燐化
ガリウム(GaP)あるいは砒化ガリウムアルミニ
ウム(GaAlAs)等のエピタキシヤル層を形成す
るにあたり広く採用されている方法であり、半導
体レーザあるいは発光ダイオードの製造の基本を
なす処理方法といえる。たとえば、かかる液相エ
ピタキシヤル成長方法によつて半導体基板上に
pn接合を形成するにあたり、通常実施されてい
る方法の一つに、一導電型の不純物が添加された
溶液を収納する溶液槽を準備し、この溶液槽内の
溶液に先ず半導体基板を接触させて第1のエピタ
キシヤル層を成長させたのち、溶液槽内の溶液に
逆導電型の不純物を気相あるいは固相から添加す
ることによつて一導電型の不純物を補償し、半導
体基板上にエピタキシヤル成長された第1のエピ
タキシヤル層上にこれとは逆導電型の第2のエピ
タキシヤル層を成長させる方法がある。
The liquid phase epitaxial growth method is a widely used method for forming epitaxial layers of gallium arsenide (GaAs), gallium phosphide (GaP), gallium aluminum arsenide (GaAlAs), etc. on - group compound semiconductor substrates. It can be said to be the basic processing method for manufacturing semiconductor lasers or light emitting diodes. For example, by such a liquid phase epitaxial growth method,
One of the commonly used methods for forming a p-n junction is to prepare a solution bath containing a solution containing impurities of one conductivity type, and to first contact the semiconductor substrate with the solution in the solution bath. After growing the first epitaxial layer, impurities of one conductivity type are compensated for by adding impurities of the opposite conductivity type to the solution in the solution bath from the gas phase or solid phase, and the epitaxial layer is grown on the semiconductor substrate. There is a method of growing a second epitaxial layer of the opposite conductivity type on the epitaxially grown first epitaxial layer.

この方法は1つの溶液槽の使用により第1,第
2のエピタキシヤル層を形成することのできる方
法であり、液相成長装置の槽構造が簡単なため、
広く実用に供されている。ところでこの方法では
第2のエピタキシヤル層の形成にあたり、不純物
の補償が必要であるため、第1のエピタキシヤル
層に比して第2のエピタキシヤル層の不純物濃度
が必然的に高くなる。したがつて第2のエピタキ
シヤル層の不純物濃度を任意の値に制御できず、
また第2のエピタキシヤル層の不純物濃度が高く
なるため、この層の結晶性は悪く、この方法では
十分な発光出力をもつ発光ダイオードを得ること
が困難である。
This method allows the formation of the first and second epitaxial layers using one solution tank, and the tank structure of the liquid phase growth apparatus is simple.
It is widely used in practical applications. However, in this method, compensation for impurities is required in forming the second epitaxial layer, so the impurity concentration of the second epitaxial layer is inevitably higher than that of the first epitaxial layer. Therefore, the impurity concentration of the second epitaxial layer cannot be controlled to an arbitrary value;
Furthermore, since the impurity concentration of the second epitaxial layer becomes high, the crystallinity of this layer is poor, and it is difficult to obtain a light emitting diode with sufficient light emitting output using this method.

この問題を解決する方法として本出願人は、第
1のエピタキシヤル層を成長させた後、反応系を
真空排気して溶液中の不純物を蒸発させ、再度第
2のエピタキシヤル層を成長させる方法を特願昭
54―4381号明細書ですでに提案している。この方
法では、溶液中の不純物の除去が容易であるもの
の、蒸発した不純物や溶質の原子が反応系全体に
飛散して各部を汚染させる問題が依然として残
り、第2のエピタキシヤル層各部の不純部濃度の
制御性の面でさらに改善の余地が残されている。
As a method to solve this problem, the applicant has developed a method in which after growing the first epitaxial layer, the reaction system is evacuated to evaporate impurities in the solution, and the second epitaxial layer is grown again. Special request for
This has already been proposed in specification No. 54-4381. Although this method makes it easy to remove impurities in the solution, there still remains the problem that evaporated impurities and solute atoms scatter throughout the reaction system and contaminate various parts. There is still room for further improvement in terms of concentration controllability.

本発明は、上記の真空排気を導入した方法にお
いて派生する蒸発不純物等の飛散による反応後の
汚染の問題を排除し、不純物濃度の制御性を改善
した液相エピタキシヤル成長方法を提供するもの
であり、本発明の特徴は、一導電型の不純物を含
む溶液に、半導体基板を接触させ、一導電型のエ
ピタキシヤル層を形成したのち、反応系をキヤリ
アガスを流しながら真空排気し、前記溶液中の不
純物を蒸発させて、反応系外へ取去ることによつ
て、この不純物濃度の低い溶液を得、ついでこの
溶液を用いて、再度エピタキシヤル層を成長させ
ることにある。
The present invention provides a liquid phase epitaxial growth method that eliminates the problem of post-reaction contamination due to the scattering of evaporated impurities, etc., which is generated in the above-mentioned method using vacuum evacuation, and improves controllability of impurity concentration. The present invention is characterized in that after a semiconductor substrate is brought into contact with a solution containing impurities of one conductivity type to form an epitaxial layer of one conductivity type, the reaction system is evacuated while flowing a carrier gas, and the reaction system is evacuated while flowing a carrier gas. By evaporating the impurities and removing them from the reaction system, a solution with a low impurity concentration is obtained, and this solution is then used to grow the epitaxial layer again.

以下、実施例に基いて図面とともに本発明の液
相エピタキシヤル成長方法について詳しく説明す
る。
Hereinafter, the liquid phase epitaxial growth method of the present invention will be explained in detail based on Examples and drawings.

第1図は、本発明の方法によつてGaP緑色発光
ダイオード用のGaPエピタキシヤル成長を行う際
に用いる液相エピタキシヤル成長装置の構成を示
す図、また第2図は、エピタキシヤル層の成長温
度プログラムを示す図である。
FIG. 1 is a diagram showing the configuration of a liquid phase epitaxial growth apparatus used when performing GaP epitaxial growth for GaP green light emitting diodes by the method of the present invention, and FIG. FIG. 3 is a diagram showing a temperature program.

本発明で用いる液相エピタキシヤル成長装置は
第1図で示すように、主電気炉1および補助電気
炉2、これらの電気炉1,2内に配置され、かつ
一端が第1のバルブ3を介してガス供給系につな
がり、他端が、第2のバルブ4を介して排気系に
つながる石英製の反応管5、および出発材料とな
るGaP基板を保持するための基板保持部6と溶液
槽7とで構成される成長用ボートを主たる構成要
素として具備している。なお、8はGaP基板、9
は溶液槽7内に収納されたエピタキシヤル成長用
の溶液、10は溶液槽7を移動させるための操作
ハンドル、11は不純物ボート、12は同ボート
11内に入れられた不純物、たとえば亜鉛Zn、
そして13は真空ポンプである。
As shown in FIG. 1, the liquid phase epitaxial growth apparatus used in the present invention includes a main electric furnace 1 and an auxiliary electric furnace 2, which are arranged inside these electric furnaces 1 and 2, and one end of which has a first valve 3. A reaction tube 5 made of quartz, the other end of which is connected to a gas supply system through a second valve 4 and an exhaust system through a second valve 4, and a substrate holder 6 and a solution tank for holding a GaP substrate serving as a starting material. The main component is a growth boat consisting of 7. In addition, 8 is a GaP substrate, 9
10 is an operating handle for moving the solution tank 7; 11 is an impurity boat; 12 is an impurity contained in the boat 11; for example, zinc, Zn,
And 13 is a vacuum pump.

ところで、GaP緑色発光ダイオードの製造に用
いられるGaPエピタキシヤル成長用の溶液9は、
たとえば溶媒としてガリウムGaを10g、溶質とし
て多結晶GaPを350mg、n型不純物としてテルル
Te 100μgを溶液槽7に入れ、これを加熱して形
成したGaPの飽和溶液である。
By the way, the GaP epitaxial growth solution 9 used for manufacturing GaP green light emitting diodes is as follows:
For example, 10g of gallium Ga as a solvent, 350mg of polycrystalline GaP as a solute, and tellurium as an n-type impurity.
This is a GaP saturated solution formed by putting 100 μg of Te into a solution bath 7 and heating it.

以下に、第2図の温度プログラムに基いてエピ
タキシヤル層を成長させる過程を具体的に説明す
る。
The process of growing an epitaxial layer will be specifically explained below based on the temperature program shown in FIG.

まず、主電気炉1のみを作動させ、加熱し、温
度T1まで上昇させたのち、第1のバルブ3から
1/minでH2ガスを流しつつ第2のバルブ4
から排気しながら、時刻t1からt2まで時間τ1(約30
分間)にわたり反応管内のボートを温度T1(1050
℃)に保持し、Teを含むGaPの飽和溶液9をつ
くる。次に時刻t2で操作ハンドル10を操作して
溶液槽7を移動させGaPの飽和溶液9をGaP基板
8に接触させ、時刻t3までの時間τ2(約20分間)
にわたりこの状態に保つ。
First, only the main electric furnace 1 is operated and heated, and after raising the temperature to T 1 , the second valve 4 is turned on while flowing H 2 gas from the first valve 3 at a rate of 1/min.
The time τ 1 ( approximately 30
temperature T 1 (1050 min) for the boat in the reaction tube
℃) to prepare a saturated solution 9 of GaP containing Te. Next, at time t 2 , the operation handle 10 is operated to move the solution tank 7 to bring the GaP saturated solution 9 into contact with the GaP substrate 8 , and the time τ 2 (approximately 20 minutes) until time t 3
Keep it in this state for a long time.

そして、時刻t3から、1℃/minの冷却速度で
徐冷を開始し、温度T2(たとえば920℃)に達す
る時刻t4までの時間τ3にわたりこの徐冷を続け、
GaP基板8の上にn型エピタキシヤル層を成長さ
せる。
Then, from time t 3 , slow cooling is started at a cooling rate of 1° C./min, and this slow cooling is continued for a time τ 3 until reaching temperature T 2 (for example, 920° C.) at time t 4 ,
An n-type epitaxial layer is grown on the GaP substrate 8.

このようにして、n型エピタキシヤル層を成長
させたのち、時刻t4から時刻t5までの時間τ4(30〜
40分間)にわたり、第1のバルブ3から微量の
H2ガスを流しつつ、真空ポンプ13を作動させ
管内を真空排気する。この真空排気によつて溶液
9中のTeが蒸発し、H2ガスによつて反応系の外
へ排出される。すなわち、時間τ4が経過したのち
の溶液9中の不純物Te濃度は無視しうる程度ま
で低下する。次に時刻t5で補助電気炉8を作動さ
せて、不純物ボート11内のZnを加熱して蒸発
させ、p型不純物であるZnを気相から導入し、
時間τ5が経過した時刻t6から、Znの導入を維持し
つつ1℃/minの冷却速度で温度T3(たとえば800
℃)に達するまで徐冷し、n型エピタキシヤル層
上にp型エピタキシヤル層を成長させる。そして
最後に、時刻t7で、GaP基板8と溶液9との接触
を断つことによつて全ての処理が終了する。
After growing the n-type epitaxial layer in this way, the time τ 4 ( 30 ~
40 minutes) from the first valve 3.
While flowing H 2 gas, the vacuum pump 13 is activated to evacuate the inside of the tube. Te in the solution 9 is evaporated by this vacuum evacuation, and is discharged out of the reaction system by H 2 gas. That is, after the time τ 4 has elapsed, the impurity Te concentration in the solution 9 decreases to a negligible level. Next, at time t5 , the auxiliary electric furnace 8 is operated, Zn in the impurity boat 11 is heated and evaporated, and Zn, which is a p-type impurity, is introduced from the gas phase.
From time t 6 when time τ 5 has elapsed, the temperature T 3 (for example, 800
℃), and a p-type epitaxial layer is grown on the n-type epitaxial layer. Finally, at time t7 , the contact between the GaP substrate 8 and the solution 9 is cut off, thereby ending all the processing.

以上説明してきた本発明の方法では、真空排気
中の反応系内にキヤリアガスの流れがあるため溶
液中から蒸発した不純物Teがキヤリアガスとと
もに反応系から外部へ排出され、従来のように、
蒸発した不純物が飛散して不純物ボート11や反
応管1の内面などに付着し、これらの部分を汚染
することがないので第2のエピタキシヤル層の不
純物濃度の制御性が改善され、また多数回にわた
るエピタキシヤル成長を行う場合も反応管を洗浄
する必要がなく作業性も向上する。
In the method of the present invention described above, since there is a flow of carrier gas in the reaction system during vacuum evacuation, the impurity Te that has evaporated from the solution is discharged from the reaction system together with the carrier gas.
Since the evaporated impurities do not scatter and adhere to the impurity boat 11, the inner surface of the reaction tube 1, etc. and contaminate these parts, the controllability of the impurity concentration in the second epitaxial layer is improved. Even when performing epitaxial growth over a long period of time, there is no need to clean the reaction tube, which improves work efficiency.

なお、真空排気時に反応管5へ流すキヤリアガ
ス流量を50〜500ml/minとし反応管内の圧力を
30〜300Torrに保つた場合、不純物除去のために
好適であり、ガス流量が50ml/min以下である
と、不純物の排出が不十分となり、一方、500
ml/min以上であると管内の温度を下げる結果と
なる。すなわちキヤリアガス流の流量を上述の範
囲に選ぶことがのぞましい。
In addition, the flow rate of the carrier gas flowing into the reaction tube 5 during vacuum evacuation is set to 50 to 500 ml/min to reduce the pressure inside the reaction tube.
If the gas flow rate is kept at 30 to 300 Torr, it is suitable for removing impurities; if the gas flow rate is less than 50 ml/min, the removal of impurities is insufficient;
If it is more than ml/min, the temperature inside the tube will be lowered. That is, it is desirable to select the flow rate of the carrier gas flow within the above-mentioned range.

なお、以上の説明では、形成される第1および
第2のエピタキシヤル層の導電型を異ならせる場
合を例示したが、たとえば時刻t5からのp型不純
物である亜鉛Znの導入を中止するならば不純物
濃度の異なるn型エピタキシヤル層を形成するこ
ともできる。
In addition, in the above explanation, the case where the conductivity types of the first and second epitaxial layers to be formed are made to be different has been exemplified. For example, it is also possible to form n-type epitaxial layers having different impurity concentrations.

この場合、第2のエピタキシヤル層の不純物濃
度は真空排気時間と温度により制御することがで
きる。また、本発明はGaPのみならずGaAs,
GaAlAs等の他の化合物半導体装置の製造にも広
く適用することができる。
In this case, the impurity concentration of the second epitaxial layer can be controlled by evacuation time and temperature. In addition, the present invention is applicable not only to GaP but also to GaAs,
It can also be widely applied to the manufacture of other compound semiconductor devices such as GaAlAs.

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

第1図は本発明の方法に用いる液相エピタキシ
ヤル成長装置、第2図は本発明の方法の一実施例
を示す温度プログラム図である。 1……主電気炉、2……補助電気炉、3……第
1のバルブ、4……第2のバルブ、5……反応
管、6……基板支持台、7……溶液槽、8……基
板、9……溶液、10……操作ハンドル、11…
…不純物ボート、12……不純物、13……真空
ポンプ。
FIG. 1 is a liquid phase epitaxial growth apparatus used in the method of the present invention, and FIG. 2 is a temperature program diagram showing an embodiment of the method of the present invention. DESCRIPTION OF SYMBOLS 1... Main electric furnace, 2... Auxiliary electric furnace, 3... First valve, 4... Second valve, 5... Reaction tube, 6... Substrate support stand, 7... Solution tank, 8 ...Substrate, 9...Solution, 10...Operation handle, 11...
...Impurity boat, 12...Impurity, 13...Vacuum pump.

Claims (1)

【特許請求の範囲】[Claims] 1 一導電型の不純物が添加されたエピタキシヤ
ル成長用の溶液を真空排気が可能な液相成長炉内
に配置し、同溶液に基板を接触させ、前記基板上
に一導電型の第1のエピタキシヤル層を形成した
のち、反応系汚染防止用のキヤリヤガスを反応系
の一方の側から供給しつつ他方の側から真空排気
して反応系を減圧状態となし、前記溶液中に添加
された一導電型の不純物を蒸発させるとともに反
応系外へ取り去り、次いで不純物蒸発後の前記溶
液を用いて前記第1のエピタキシヤル層上に第2
のエピタキシヤル層を形成することを特徴とする
液相エピタキシヤル成長方法。
1. A solution for epitaxial growth doped with impurities of one conductivity type is placed in a liquid phase growth furnace that can be evacuated, a substrate is brought into contact with the solution, and a first impurity of one conductivity type is placed on the substrate. After forming the epitaxial layer, a carrier gas for preventing contamination of the reaction system is supplied from one side of the reaction system and vacuum is evacuated from the other side to bring the reaction system into a depressurized state, so that the reaction system is reduced in pressure. The impurities of the conductivity type are evaporated and removed from the reaction system, and then the solution after the impurity evaporation is used to form a second epitaxial layer on the first epitaxial layer.
A liquid phase epitaxial growth method characterized by forming an epitaxial layer of.
JP6182979A 1979-05-18 1979-05-18 Liquid epitaxial growing method Granted JPS55154399A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6182979A JPS55154399A (en) 1979-05-18 1979-05-18 Liquid epitaxial growing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6182979A JPS55154399A (en) 1979-05-18 1979-05-18 Liquid epitaxial growing method

Publications (2)

Publication Number Publication Date
JPS55154399A JPS55154399A (en) 1980-12-01
JPS6353158B2 true JPS6353158B2 (en) 1988-10-21

Family

ID=13182368

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6182979A Granted JPS55154399A (en) 1979-05-18 1979-05-18 Liquid epitaxial growing method

Country Status (1)

Country Link
JP (1) JPS55154399A (en)

Also Published As

Publication number Publication date
JPS55154399A (en) 1980-12-01

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