JPH0610085B2 - Method for purifying indium solution using indium as solvent - Google Patents

Method for purifying indium solution using indium as solvent

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Publication number
JPH0610085B2
JPH0610085B2 JP4715584A JP4715584A JPH0610085B2 JP H0610085 B2 JPH0610085 B2 JP H0610085B2 JP 4715584 A JP4715584 A JP 4715584A JP 4715584 A JP4715584 A JP 4715584A JP H0610085 B2 JPH0610085 B2 JP H0610085B2
Authority
JP
Japan
Prior art keywords
solution
inp
thin film
purity
indium
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP4715584A
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Japanese (ja)
Other versions
JPS60195011A (en
Inventor
進 近藤
治男 永井
利昌 天野
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NTT Inc
Original Assignee
Nippon Telegraph and Telephone Corp
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Priority to JP4715584A priority Critical patent/JPH0610085B2/en
Publication of JPS60195011A publication Critical patent/JPS60195011A/en
Publication of JPH0610085B2 publication Critical patent/JPH0610085B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Crystals, And After-Treatments Of Crystals (AREA)

Description

【発明の詳細な説明】 (本発明の属する技術分野) 本発明は、半導体光素子用の材料として好適なインジウ
ム燐(InP)、インジウムガリウム砒素(InGaAs)及びイン
ジウムガリウム砒素燐(InGaAsP)などのインジウムを含
むIII−V族化合物半導体の液相成長薄膜の高純度化技
術に関し、特に液相成長に使用することを目的としたイ
ンジウム(以下、Inと記す)を溶媒とするIII族とV族
の元素の化合したIn溶液の純化方法に関するものであ
る。
TECHNICAL FIELD The present invention relates to indium phosphide (InP), indium gallium arsenide (InGaAs), indium gallium arsenide phosphide (InGaAsP) and the like suitable as materials for semiconductor optical devices. TECHNICAL FIELD The present invention relates to a technique for purifying a liquid phase growth thin film of a III-V group compound semiconductor containing indium, and particularly to a group III and a group V using indium (hereinafter referred to as In) as a solvent for the purpose of use in liquid phase growth. The present invention relates to a method for purifying an In solution containing a combination of the above elements.

(従来技術) 近年、光伝送システムの長波長化に伴ない、0.9〜1.6μ
m帯にバンドギャップをもつInP,InGaAs及びInGaAsP等
のInを含むIII−V族化合物半導体の薄膜単結晶が注目
されている。この光素子用材料として上記III−V族化
合物半導体薄膜を用いる場合、当該薄膜層のキャリア密
度を低下させる必要があり、そのためには結晶中の酸
素、イオウ及びその他の残留不純物金属を減らし結晶を
高純度化する技術が重要である。
(Prior art) 0.9-1.6μ due to the long wavelength of optical transmission system
Attention has been focused on thin film single crystals of III-V group compound semiconductors containing In such as InP, InGaAs, and InGaAsP having a band gap in the m band. When the above III-V compound semiconductor thin film is used as the material for this optical element, it is necessary to reduce the carrier density of the thin film layer, and for that purpose oxygen, sulfur and other residual impurity metals in the crystal are reduced to reduce the crystal. Technology for high purification is important.

しかし現在の技術では、Inを溶媒とするインジウム溶液
(以下、「In溶液」と記す)から酸素、イオウ及びその
他の残留不純物金属等を減ずる高純度化に限界があり、
このような不純物の残ったIn溶液を用いた液相エピタキ
シャル成長方法では成長する薄膜の高純度化に限界があ
った。
However, in the current technology, there is a limit to high purification by reducing oxygen, sulfur, and other residual impurity metals from an indium solution using In as a solvent (hereinafter referred to as “In solution”),
In the liquid phase epitaxial growth method using the In solution containing such impurities remaining, there is a limit to the purification of the growing thin film.

また、極めて抵抗値の高い半絶縁性InP,InGaAsP,InGaAs
等のIn系薄膜は、素子の基板材料あるいは素子間を電気
的に分離する素子分離用薄膜として重要である。これら
の薄膜を高抵抗化するためには、鉄(Fe)やニッケル(Ni)
等を薄膜中に添加し、これら遷移金属の形成する深い準
位を利用することが知られている。
In addition, semi-insulating InP, InGaAsP, InGaAs with extremely high resistance
In-based thin films such as are important as element isolation thin films for electrically isolating the substrate material of elements or elements. To increase the resistance of these thin films, iron (Fe) or nickel (Ni) must be used.
It is known that the deep levels formed by these transition metals are utilized by adding such substances to the thin film.

しかし、現在の技術ではFe又はNi等の遷移金属を添加し
たIn溶液から酸素、イオウその他の残留不純物金属等を
減ずる高純度化に限界があり、この溶液を用いた液相エ
ピタキシャル成長方法では成長する結晶薄膜の高抵抗化
に限界があった。
However, the current technology has a limit to high purification by reducing oxygen, sulfur and other residual impurity metals from an In solution added with a transition metal such as Fe or Ni, and a liquid phase epitaxial growth method using this solution grows. There is a limit to increase the resistance of the crystal thin film.

これまで、高純度のInP,InGaAs及びInGaAsP等のInを含
むIII−V族化合物半導体薄膜(以下「In系薄膜」とい
う)を、通常のカーボンボートを用いた液相エピタキシ
ャル方法で成長させる場合、極めて長時間の熱処理が必
要であった。
Up to now, when a high-purity InP, InGaAs, InGaAsP, or other In-containing III-V compound semiconductor thin film (hereinafter referred to as “In-based thin film”) is grown by a liquid phase epitaxial method using a normal carbon boat, A very long heat treatment was required.

すなわち、従来のカーボンボートを用いた液相エピタキ
シャル成長方法の概要を説明すると、まず、薄膜を成長
させるための溶液用原料をカーボンボートに入れ、当該
原料を真空中あるいは高純度水素雰囲気中で、640℃
〜850℃の高温で、10時間から数十時間加熱する。
これにより、溶液中に含まれる不純物を蒸発させ、溶液
の純度を高めている。しかる後にこの溶液を室温まで冷
却し、さらに基板結晶をカーボンボートに設置して、再
度加熱し、溶液を充分溶かした後除冷し、溶液の飽和温
度より低い適当な温度で基板結晶を一定時間溶液に接触
させることにより、高純度のInP,InGaAs,In
GaAsP等のIn系薄膜を成長させている。
That is, to explain the outline of a conventional liquid phase epitaxial growth method using a carbon boat, first, a raw material for a solution for growing a thin film is placed in a carbon boat, and the raw material is placed in a vacuum or a high-purity hydrogen atmosphere at 640. ℃
Heat at a high temperature of ~ 850 ° C for 10 to several tens of hours.
This evaporates the impurities contained in the solution and improves the purity of the solution. After that, the solution was cooled to room temperature, and the substrate crystal was placed on a carbon boat, heated again, and the solution was sufficiently melted and then cooled. The substrate crystal was kept at an appropriate temperature lower than the saturation temperature of the solution for a certain period of time. By contacting with a solution, high purity InP, InGaAs, In
In-based thin films such as GaAsP are grown.

また、より高純度の結晶薄膜を得るためには、前述の成
長工程を数回繰り返すことが必要であった。すなわち、
前述の方法である程度の厚さの薄膜を成長させたら、基
板を一旦反応炉から引き出し、再び溶液を数十時間加熱
した後、基板を再度溶液に接触させ更に薄膜を成長させ
ることを繰り返す。
Further, in order to obtain a crystal thin film of higher purity, it was necessary to repeat the above-mentioned growth process several times. That is,
After the thin film having a certain thickness is grown by the above-described method, the substrate is once pulled out from the reaction furnace, the solution is heated again for several tens of hours, and then the substrate is brought into contact with the solution again to further grow the thin film.

このように、従来では高純度の上記薄膜を成長させるた
めには、原料中の不純物を蒸発させ純度を高めるため
に、原料を真空中あるいは高純度水素雰囲気中で高温,
長時間の熱処理を要し、極めて長時間の熱処理を必要と
するという欠点があった。
As described above, conventionally, in order to grow the above-mentioned thin film of high purity, in order to evaporate impurities in the raw material and increase the purity, the raw material is heated at high temperature in a vacuum or in a high-purity hydrogen atmosphere.
There is a drawback that heat treatment for a long time is required and heat treatment for an extremely long time is required.

(本発明の目的) 本発明の目的は、液相エピタキシャル成長法で成長する
In系薄膜の高純度化を実現するにあたり、液相エピタ
キシャル成長法で使用するInを溶媒とするIn溶液の
純化方法を提供することにある。
(Object of the Present Invention) An object of the present invention is to provide a method for purifying an In solution using In used as a solvent in a liquid phase epitaxial growth method in realizing high purification of an In-based thin film grown by the liquid phase epitaxial growth method. To do.

本発明の他の目的は、処理時間が短くてすむ、In溶液
の純化方法を提供することにある。
Another object of the present invention is to provide a method for purifying an In solution that requires a short processing time.

(本発明の概要) 本発明は、In,InP等及びCo又はIn,InP等,Co及び遷移金
属を加熱溶融しInを溶媒とするIn溶液を純化する。前述
の加熱溶融に際しては、In,InP等及びCoを一時に一緒に
加熱溶融する方法と、In及びCo又はIn,Co及び遷移金属
を一旦加熱溶融した後、InP等を加えて再度加熱溶融す
る方法とがある。
(Outline of the Present Invention) The present invention purifies an In solution containing In, InP, etc. and Co or In, InP, etc., Co, and a transition metal by heating to melt In. In the above heating and melting, a method of heating and melting In, InP, etc. and Co at the same time, and once heating and melting In and Co or In, Co and transition metal, adding InP, etc. and heating and melting again. There is a method.

加熱溶融によりIn溶液をつくる際に、添加されているCo
がリン(P)又はヒ素(As)と反応し非常に安定なコバ
ルトリン化合物(CoP,Co2P,Co3P)又はコバルトヒ素化合
物(CoAs,Co2As,Co3As)を形成する。これらの化合物はそ
の形成時に酸素、イオン又はシリコンや亜鉛のように分
配係数の大きな残留不純物金属をその化合物中に取り込
む。その結果、高純度なIn溶液を得ることができる。
Co added when the In solution is prepared by heating and melting
React with phosphorus (P) or arsenic (As) to form a very stable cobalt phosphorus compound (CoP, Co 2 P, Co 3 P) or cobalt arsenic compound (CoAs, Co 2 As, Co 3 As). When these compounds are formed, oxygen, ions, or residual impurity metals having a large partition coefficient such as silicon and zinc are incorporated into the compounds. As a result, a high-purity In solution can be obtained.

また高純度化に要する処理時間が短かくてすむ利点があ
る。
Further, there is an advantage that the processing time required for high purification is short.

(本発明の実施例) 以下本発明を実施例に基づいて説明する。(Examples of the present invention) The present invention will be described below based on examples.

実施例1 まず、本発明の実施例について半絶縁性InP基板上に高
純度InP薄膜を通常のスライドボートによる液相エピタ
キシャル法により成長させる場合を例にとって詳細に説
明する。
Example 1 First, an example of the present invention will be described in detail by taking as an example a case where a high-purity InP thin film is grown on a semi-insulating InP substrate by a liquid phase epitaxial method using an ordinary slide boat.

まず純度99.9999%のInを3.5g、純度99.9999%のCoを
約40mg、例えばキャリア濃度が5×1015cm-3の無添
加InP単結晶を185mgそれぞれ秤量し(CoがPと結合
し、Pの飽和度が落ちる事を考慮して無添加の場合にく
らべInP量は多くしている。)、カーボンボートの一槽
に入れ高純度水素雰囲気(流量800cc/分)中で850℃3
時間熱処理を行う。この熱処理によりコバルトリン化合
物がIn溶液中で形成され、この化合物形成時にIn溶液中
の各種残留不純物が化合物中にとりこまれるので高純度
なIn溶液を得ることができる。次いでこの高純度In溶液
を冷却しInP成長用の原料を得る。この後、半絶縁性InP
基板をボートにセットした後、高純度の水素雰囲気中で
飽和温度720℃で1時間保持し、この後0.6℃/分で
徐冷し、先に得られた原料を再度溶融したInP成長用溶
液710℃で、前記基板に接触させ690℃までInP薄膜を
成長させる。
First, 3.5 g of 99.9999% pure In, about 40 mg of 99.9999% pure Co, for example, 185 mg of an additive-free InP single crystal with a carrier concentration of 5 × 10 15 cm −3 were weighed (Co bound to P, P The amount of InP is larger than that when no additive is added in consideration of the decrease in the degree of saturation.), And put it in a tank of a carbon boat in a high-purity hydrogen atmosphere (flow rate 800 cc / min) at 850 ° C 3
Perform heat treatment for an hour. By this heat treatment, a cobalt phosphorus compound is formed in the In solution, and various residual impurities in the In solution are incorporated into the compound when the compound is formed, so that a high-purity In solution can be obtained. Then, this high-purity In solution is cooled to obtain a raw material for InP growth. After this, semi-insulating InP
After the substrate was set in a boat, it was kept in a high-purity hydrogen atmosphere at a saturation temperature of 720 ° C. for 1 hour, then slowly cooled at 0.6 ° C./min, and the raw material obtained above was melted again to prepare an InP growth solution. At 710 ° C., the InP thin film is grown by contacting the substrate to 690 ° C.

この様にして成長したInP薄膜の膜厚は約7μmで、その
表面は鏡面状態が保たれた。格子定数及びフォトルミス
ペクトルのピーク波長は不純物を添加しないで成長させ
たInP薄膜と一致した。
The InP thin film thus grown had a film thickness of about 7 μm, and its surface was kept in a mirror state. The lattice constant and the peak wavelength of the photolumi spectrum are consistent with the InP thin film grown without adding impurities.

また、成長したInP薄膜をホール測定した結果、室温で
の移動度約4700cm2/V.Sキャリア濃度1×1016cm-877°
Kでの移動度22000cm2/V.Sキャリア濃度8×1015cm-3
であった。
In addition, as a result of Hall measurement of the grown InP thin film, the mobility at room temperature was about 4700 cm 2 / VS carrier concentration 1 × 10 16 cm -8 77 °
Mobility at K 22000 cm 2 / VS carrier concentration 8 × 10 15 cm -3
Met.

この値はCoを添加しないIn溶液を用い他の熱処理条件等
の成長条件は同様にして成長させたInP薄膜の移動度
(室温〜4200cm2/V.S、77°K〜16000cm2/V.S)に比べ
室温で約500cm2/V.S77°Kで5000cm2/V.S程度大き
い。この事は、In溶液にCoを添加する事により移導度が
大きくなり、すなわち純度が高くなった事を示してい
る。
This value is compared to the mobility (room temperature ~ 4200cm 2 / VS, 77 ° K ~ 16000cm 2 / VS) of the InP thin film grown under the same growth conditions as other heat treatment conditions using an In solution without addition of Co. about 5000 cm 2 / VS larger at about 500cm 2 /V.S77°K at room temperature. This shows that the addition of Co to the In solution increased the degree of transfer, that is, the purity was increased.

このように高純度なInP薄膜が得られるのは高純度In溶
液を用いていることと、この高純度In溶液中のコバルト
リン化合物が結晶成長時に薄膜中にとりこまれないため
である。
The reason why such a high-purity InP thin film is obtained is that the high-purity In solution is used and that the cobalt phosphorus compound in the high-purity In solution is not incorporated into the thin film during crystal growth.

この実施例では、従来技術で行われていた長時間の熱処
理が不要となるので極めて短時間でIn溶液の純化及びIn
系薄膜のエピタキシャル成長ができる。
In this example, since the long-time heat treatment that was performed in the conventional technique is unnecessary, the In solution purification and the In
Epitaxial growth of thin films is possible.

図1は、半絶縁性InP基板上にInP薄膜を成長させると
き、Co添加In溶液と無添加In溶液を用い前述した条件で
交互に連続して成長させた場合の77°Kにおける電気特
性を示す。
FIG. 1 shows the electrical characteristics at 77 ° K when InP thin films were grown on a semi-insulating InP substrate, using a Co-added In solution and a non-added In solution, and growing them alternately and continuously under the above-mentioned conditions. Show.

○印はCo添加In溶液を用いた場合、×印は無添加In溶液
を用いてInPを成長させた場合を示している。
The ∘ mark shows the case where the Co-added In solution was used, and the X mark shows the case where the InP was grown using the non-added In solution.

図1から明らかな様にCo添加In溶液を用いて成長した場
合のInP薄膜の移動度が増大し、より高純度なInP膜が得
られている。また、Co添加のI溶液を用いてInP薄膜の成
長を行ったことにより後の無添加In溶液を用いて成長し
たInP薄膜の純度(移動度)に影響を及ぼさないことが
確認された。
As is apparent from FIG. 1, the mobility of the InP thin film when grown using the Co-added In solution is increased, and a higher-purity InP film is obtained. It was also confirmed that the growth of the InP thin film by using the Co-added I solution did not affect the purity (mobility) of the InP thin film grown by using the undoped In solution later.

一方、図2はIn溶液へのCoの添加量を種々変え、成長温
度を710〜690℃に保つ様にInPの量を選んで成長
させたInP薄膜の移動度を示す。2mg程度の少量のCo添
加においても77°Kでの移動度が20,000cm2/V.S程度
のInP薄膜が得られている。
On the other hand, FIG. 2 shows the mobility of an InP thin film grown by varying the amount of Co added to the In solution and selecting the amount of InP so as to keep the growth temperature at 710 to 690 ° C. Even with the addition of a small amount of Co of about 2 mg, an InP thin film having a mobility of about 20,000 cm 2 / VS at 77 ° K was obtained.

また、InGaAsあるいはInGaAsP薄膜の成長時において
も、高温でCoはAsと極めて安定な化合物を形成する事か
ら、InPの場合と同様にして全く同様な効果が得られ
る。
Further, even when growing an InGaAs or InGaAsP thin film, Co forms an extremely stable compound with As at high temperature, and therefore, the same effect as in InP can be obtained.

実施例2 次に、実施例1よりさらに結晶薄膜の高純度化を目的と
した実施例を示す。
Example 2 Next, an example aiming at a higher purification of the crystal thin film than in Example 1 will be described.

この実施例では、In,Co及びInP単結晶を一時に加熱溶
融して純化を図るのではなく、純化工程を二段階に分け
ている点に特徴がある。即ち先ずIn及びCoを加熱溶融し
一次の純化を行った後に、これにInPを加えて加熱溶融
し二次の純化を行う。
This embodiment is characterized in that the purification process is divided into two stages, instead of purifying the In, Co and InP single crystals by heating and melting them all at once. That is, first, In and Co are heated and melted to perform the first purification, and then InP is added to this to heat and melt to perform the second purification.

具体的に説明すると、まず純度99.9999%のInを3.5g、
純度99.999%のCoを約40mgを秤量し、カーボンボート
の一槽に入れ、酸素を0.05ppm添加した水素雰囲気中で
850℃24時間熱処理を行う。この熱処理工程で、水
素中に微量の酸素を添加する理由は、高温で水素処理を
長時間行うと、石英管からシリコン(Si)が溶液に混入し
てしまい、この溶液を用いて結晶成長した場合に結晶薄
膜中のn形不純物濃度が高くなるので、この熱処理時の
SiのIn溶液への混入を防ぐためである。なお添加する酸
素は0.01〜0.2ppmでよい。次に冷却し、InにCoを添加し
た高純度原料を得る。さらに、高純度(例えばキャリア
濃度5×1015cm-3)InP単結晶を190mgを秤量し、前
述のInとCoの高純度原料と同じ槽に入れ純水素(ガス流
量800cc/分)中で720℃20時間熱処理し高純度なI
n溶液を得る。その後、この高純度In溶液を室温まで冷
却し、InP成長用高純度原料を得る。この後、半絶縁性I
nP基板をボートにセットし、高純度水素雰囲気中で飽和
温度720℃で1時間保持し、この後0.6℃/分で徐冷
し、前述の高純度原料を再度加熱溶融したInP成長用溶
液に710℃で前記基板を接触させ690℃までInP薄
膜を成長させる。
Specifically, first, 3.5 g of 99.9999% pure In,
About 40 mg of Co having a purity of 99.999% is weighed, put in one tank of a carbon boat, and heat-treated at 850 ° C. for 24 hours in a hydrogen atmosphere containing 0.05 ppm of oxygen. The reason for adding a trace amount of oxygen to hydrogen in this heat treatment step is that if hydrogen treatment is performed at high temperature for a long time, silicon (Si) will be mixed into the solution from the quartz tube, and crystals will grow using this solution. In this case, since the n-type impurity concentration in the crystal thin film becomes high,
This is to prevent mixing of Si into the In solution. The oxygen added may be 0.01 to 0.2 ppm. Then, it is cooled to obtain a high-purity raw material in which Co is added to In. Further, 190 mg of high-purity (for example, carrier concentration 5 × 10 15 cm −3 ) InP single crystal was weighed, put in the same tank as the high-purity In and Co raw materials described above, and placed in pure hydrogen (gas flow rate 800 cc / min). Heat-treated at 720 ℃ for 20 hours to obtain high purity I
Obtain a solution. Then, this high-purity In solution is cooled to room temperature to obtain a high-purity raw material for InP growth. After this, semi-insulating I
The nP substrate was set in a boat, kept in a high-purity hydrogen atmosphere at a saturation temperature of 720 ° C. for 1 hour, then slowly cooled at 0.6 ° C./min, and the above-mentioned high-purity raw material was again heated and melted into an InP growth solution. The substrate is contacted at 710 ° C. and an InP thin film is grown to 690 ° C.

この様にして成長させたInP薄膜の膜厚は約7μmで、薄
膜の表面は鏡面状態が保たれた。成長したInP薄膜をホ
ール測定した結果、n形で室温での移動度4800cm2/V.
S、抵抗率2.3Ωcm、キャリア濃度5.7×1014cm-3、77°
Kでの移動度72,000cm2/V.S、抵抗率0.15Ωcm、キャリ
ア濃度5.3×1014cm-3であった。
The InP thin film thus grown had a thickness of about 7 μm, and the surface of the thin film was kept in a mirror state. As a result of Hall measurement of the grown InP thin film, n-type mobility at room temperature was 4800 cm 2 / V.
S, resistivity 2.3 Ωcm, carrier concentration 5.7 × 10 14 cm -3 , 77 °
The mobility at K was 72,000 cm 2 / VS, the resistivity was 0.15 Ωcm, and the carrier concentration was 5.3 × 10 14 cm -3 .

比較のために、Coを添加せずInPの量を85mgとし、他の
熱処理をはじめとする成長条件を同じにして成長させた
InP薄膜の電気特性は、室温での移動度4400〜4100cm2
V.S、キャリア濃度5〜2×1015cm-377°Kでの移動度3
8,000〜30,000cm2/V.Sキャリア濃度4.5〜1.5×1015cm
-3程度である。
For comparison, the amount of InP was 85 mg without adding Co, and the growth conditions including other heat treatments were the same.
The electrical characteristics of the InP thin film are that the mobility at room temperature is 4400 to 4100 cm 2 /
VS, carrier concentration 5 to 2 × 10 15 cm -3 Mobility at 77 ° K 3
8,000 to 30,000 cm 2 / VS carrier concentration 4.5 to 1.5 × 10 15 cm
-It is about -3 .

実施例2の中で述べたと同様の条件で、Co添加In溶液と
無添加In溶液を用いて交互に成長させた場合のInP薄膜
の77°Kでの移動度の変化を図3に示す。(77°Kでの
移動度は、実質的なInP薄膜の純度を示している。○印
はCo添加のIn溶液を用いた場合、×印は無添加In溶液を
用いた場合を示す。Co添加のIn溶液を用いた場合、無添
加のIn溶液を用いる場合にくらべ成長したInP薄膜の移
動度が30,000〜40,000cm2/V.S高い値を示しており、Co
添加のIn溶液を用いて成長させたInP薄膜が極めて高純
度である事がわかる。
FIG. 3 shows a change in mobility of the InP thin film at 77 ° K when alternately grown with a Co-added In solution and a non-added In solution under the same conditions as described in Example 2. (The mobility at 77 ° K indicates the substantial purity of the InP thin film. ◯ indicates the case where the Co-added In solution was used, and X indicates the case where the non-added In solution was used. In the case of using the added In solution, the mobility of the grown InP thin film is 30,000 to 40,000 cm 2 / VS higher than that of the case of using the non-added In solution.
It can be seen that the InP thin film grown using the added In solution has extremely high purity.

この実施例では、純化を二段階に分けて行うのでより高
純度なIn溶液を得られ、またより高純度なInP薄膜を形
成できる。
In this example, since the purification is performed in two steps, a higher purity In solution can be obtained and a higher purity InP thin film can be formed.

また、従来技術で行われていた熱処理、薄膜形成の工程
を繰り返し行わなくても超高純度のInP薄膜を形成でき
るので、工程の短時間化を実現できる。
Further, the ultra-high purity InP thin film can be formed without repeating the steps of heat treatment and thin film formation, which have been performed in the conventional technique, so that the process can be shortened.

表1は、実施例2と全く同様な方法を用い、成長条件を
種々変えて成長させたInP薄膜の室温でのキャリア濃度
及び77°Kにおける移動度を示す。
Table 1 shows the carrier concentration at room temperature and the mobility at 77 ° K of the InP thin film grown using the same method as in Example 2 under various growth conditions.

表2に記載していない他の成長条件は実施例2と同様で
ある。
Other growth conditions not described in Table 2 are the same as in Example 2.

実施例3 次に鉄を添加した高抵抗InP薄膜成長の一実施例をのべ
る。
Example 3 Next, an example of growth of a high resistance InP thin film to which iron is added will be described.

InP系薄膜を高抵抗化するためには、溶液中の残留不純
物を可及的に少なくし、かつ高純度のFeを添加しなけれ
ばならない。この残留不純物を可及的に少なくするため
のCo添加を併用し、Fe添加InP薄膜の成長を行った。
In order to increase the resistance of the InP-based thin film, it is necessary to reduce residual impurities in the solution as much as possible and add high-purity Fe. The Fe-doped InP thin film was grown by using Co addition to reduce the residual impurities as much as possible.

まず、純度99.9999%のIn3.5g、純度99.999%のCo40
mg、純度99.999%Fe40mgを秤量し、これらをカーボン
ボートの一槽に入れ、酸素を0.07ppm添加した水素雰囲
気中で850℃24時間加熱溶融する。その後この溶液を
室温まで冷却する。次に高純度(例えばキャリア濃度5
×1015cm-3)のInPを150mg秤量し、同じ槽に入れ高
純度水素雰囲気中で720℃で20時間加熱した後室温
まで冷却しInP成長用原料を得る。この後半絶縁性InP基
板をボートにセットした後、高純度水素雰囲気中で72
0℃1時間加熱し、この後0.6℃/分で徐冷し、前述のI
nP成長用原料を再度加熱溶融したInP薄膜成長用溶液に
710℃で前記基板を接触させ690℃までInP薄膜を
成長させる。
First, In3.5g with 99.9999% purity and Co40 with 99.999% purity.
mg, purity 99.999% Fe 40 mg are weighed, put into a tank of a carbon boat, and heated and melted at 850 ° C. for 24 hours in a hydrogen atmosphere containing 0.07 ppm of oxygen. Then the solution is cooled to room temperature. Next, high purity (for example, carrier concentration 5
× a 10 15 InP of cm -3) and 150mg weighed to obtain a raw material for cooling InP grown to room temperature after heating for 20 hours at 720 ° C. in a high purity hydrogen atmosphere placed in the same bath. After setting the latter half insulating InP substrate in a boat, the substrate was placed in a high-purity hydrogen atmosphere.
Heat at 0 ° C for 1 hour, then cool slowly at 0.6 ° C / min.
The substrate is brought into contact with an InP thin film growth solution obtained by heating and melting the nP growth raw material again at 710 ° C. to grow the InP thin film up to 690 ° C.

このInP薄膜の膜厚は約7μmで表面は滑らかであっ
た。、またこのInP薄膜は極めて高抵抗であり、通常の
ホール測定は困難であった。金ゲルマニウムニッケル合
金を電極としてシート抵抗を測定したところ抵抗率は、
約2×105Ωcmであった。
The thickness of this InP thin film was about 7 μm and the surface was smooth. Moreover, this InP thin film has a very high resistance, and it is difficult to measure the normal hole. When the sheet resistance was measured using gold germanium nickel alloy as an electrode, the resistivity was
It was about 2 × 10 5 Ωcm.

一方、Coを添加せず、Feのみを添加したIn溶液を用いて
同一条件でInP薄膜を成長させた場合(ただし実施例1
と同様にして、Coを添加しない場合はInPソースの量は
少ない。)InP薄膜は高抵抗化せず、通常の無添加InP薄
膜と同程度で抵抗率は高々数Ωcmであった。
On the other hand, when an InP thin film was grown under the same conditions using an In solution containing only Fe without adding Co (see Example 1
Similarly, the amount of InP source is small when Co is not added. The resistivity of the InP thin film did not increase, and the resistivity was at most about several Ωcm, which was comparable to that of a normal undoped InP thin film.

このように高純度かつ高抵抗のInP薄膜が得られるのは
先に実施例1で説明したように、Coによる不純物のゲッ
ター効果によりInP薄膜自体が高純度化できることに加
えて、Coを添加したIn溶液にFe又はNi等の遷移金属を更
に添加すると、遷移金属が残留不純物量にくらべ極めて
その添加量が多く、かつCoあるいはCoの化合物にくらべ
分配係数が比較的大きい事から、薄膜析出時に短時間の
熱処理で深い準位を有するFeあるいはNiがInP添加され
るからである。
As described above in Example 1, the high purity and high resistance InP thin film can be obtained. In addition to the fact that the InP thin film itself can be highly purified by the gettering effect of impurities by Co, Co is added. When a transition metal such as Fe or Ni is further added to the In solution, the amount of the transition metal added is much larger than the amount of residual impurities, and the distribution coefficient is relatively large compared to Co or the compound of Co. This is because Fe or Ni having a deep level is added to InP by heat treatment for a short time.

この様にして、Feと同時にCoをIn溶液に添加し、残留不
純物濃度を減少させる事により、容易に高抵抗InP薄膜
を得る事ができた。表2に、実施例3の一部の成長条件
を変えて成長させたInP薄膜の電気特性を示す。
In this way, Co was added to the In solution at the same time as Fe to reduce the concentration of residual impurities, so that a high-resistance InP thin film could be easily obtained. Table 2 shows the electrical characteristics of the InP thin film grown in Example 3 with some growth conditions changed.

実施例4 実施例3のFeの代わりにNiを用いても同様に高抵抗のIn
Pを成長させることができる。
Example 4 Even if Ni was used instead of Fe in Example 3, In with high resistance
Can grow P.

実施例3の成長条件のうち酸素添加の水素雰囲気中の熱
処理で酸素を0.05ppmとし、高純度水素雰囲気熱処理条
件を720℃24時間とし、InP薄膜成長を開始温度6
80℃から終了温度660℃で行った。
Of the growth conditions of Example 3, oxygen was 0.05 ppm by heat treatment in an oxygen-added hydrogen atmosphere, the high-purity hydrogen atmosphere heat treatment condition was 720 ° C. for 24 hours, and the InP thin film growth start temperature was 6
It was carried out from 80 ° C. to a finish temperature of 660 ° C.

このときのNi添加のInP薄膜の膜厚は約6μmで表面は滑
らかであった。このInP薄膜に金,亜鉛合金を電極とし
てシート抵抗を測定したところ約3700Ωcmであった。
At this time, the Ni-doped InP thin film had a thickness of about 6 μm and had a smooth surface. When the sheet resistance of this InP thin film was measured using gold and zinc alloy electrodes, it was about 3700 Ωcm.

一方、Coを添加せずNiのみを添加したIn溶液を用い、他
は同一条件でInP薄膜を成長させた場合(ただし、実施
例1と同様にしてCoを添加しない場合は、溶液の飽和度
調整のためInPソースの量を少なくしている。)InP薄膜
は高抵抗化せず、この程度の熱処理時間では高々数Ωcm
であった。表3に実施例4の成長条件を一部変えて成長
させたNi添加のInP薄膜の成長条件と比抵抗を示す。
On the other hand, when an InP thin film was grown under the same conditions with the use of an In solution containing no Co and containing only Ni (however, when Co was not added as in Example 1, the saturation of the solution was The amount of InP source is reduced for adjustment.) The InP thin film does not have high resistance, and at most this heat treatment time is several Ωcm.
Met. Table 3 shows the growth conditions and the specific resistance of the Ni-doped InP thin film grown by partially changing the growth conditions of Example 4.

この様にしてNiとCoをIn溶液に添加する事により容易に
高抵抗InP膜が得られた。
In this way, a high resistance InP film was easily obtained by adding Ni and Co to the In solution.

ここでは液相エピタキシャル成長法による高純度InP薄
膜及び高抵抗InP薄膜の成長法について述べたが、Coと
Pの化合物によるゲッター作用を利用して高純度薄膜,
高抵抗薄膜を成長させている。一方CoはAsとも安定な化
合物を作ることから、この方法は高純度InGaAs,InGaAs
P,InAs,InGaPあるいは高抵抗InGaAsあるいはInGaAsP,In
As,InGaPの液相成長にも応用できる事は明らかである。
Here, the growth method of the high-purity InP thin film and the high-resistance InP thin film by the liquid phase epitaxial growth method has been described. The high-purity thin film using the getter action of the compound of Co and P,
Growing high resistance thin film. On the other hand, since Co forms a stable compound with As, this method is highly pure InGaAs and InGaAs.
P, InAs, InGaP or high resistance InGaAs or InGaAsP, In
It is obvious that it can also be applied to liquid phase growth of As and InGaP.

さらに、原料の純度が向上し原料中の残留不純物濃度が
減少すれば、水素処理温度の低温化あるいは水素処理時
間の短縮化でき、またCo,Fe,Ni等の添加金属の量を減少
させても高純度化,高抵抗化できる事はいうまでもな
い。
Furthermore, if the purity of the raw material is improved and the concentration of residual impurities in the raw material is reduced, the hydrogen treatment temperature can be lowered or the hydrogen treatment time can be shortened, and the amount of added metals such as Co, Fe and Ni can be reduced. Needless to say, can be highly purified and have high resistance.

本発明により得られた薄膜結晶をアバランシェフォトダ
イオード、PINダイオード、FET等の高純度電子デバイ
ス、あるいはこれら電子デバイスの素子分離層、半導体
レーザの埋め込み層等の薄膜材料作成に利用できる。
The thin film crystal obtained by the present invention can be used for the production of thin film materials such as high-purity electronic devices such as avalanche photodiodes, PIN diodes, and FETs, element isolation layers of these electronic devices, and buried layers of semiconductor lasers.

また、実施例1〜4では各種In溶液を一旦冷却し、再び
これを加熱溶融してからInP系薄膜の成長を行っている
が、In溶液を一旦冷却することなくInP系薄膜の成長を
続けて行えることはいうまでもない。
Further, in Examples 1 to 4, various In solutions are once cooled, and the InP-based thin film is grown after being heated and melted again, but the InP-based thin film is continuously grown without once cooling the In solution. It goes without saying that you can do it.

(本発明の効果) 以上述べた様に、本発明はInを溶媒としInP、In
GaAsP、InGaAs等を含むIn溶液の純化方法
においてIn溶液にCoを添加する事により、CoとP
あるいはCoとAsの化合物をIn溶液中に析出せし
め、これらの化合物の中に残留不純物を取り込みIn溶
液中の残留不純物を減少させる事ができ、高純度なIn
溶液が容易に得られる利点がある。
(Effects of the Present Invention) As described above, the present invention uses In as a solvent and InP and In.
In the method of purifying an In solution containing GaAsP, InGaAs, etc., by adding Co to the In solution, Co and P
Alternatively, a compound of Co and As can be precipitated in an In solution, and residual impurities can be introduced into these compounds to reduce the residual impurities in the In solution.
There is an advantage that the solution can be easily obtained.

しかも上述のIn溶液の純化に要する時間が短くてすむ
利点がある。
Moreover, there is an advantage that the time required for purifying the In solution described above can be shortened.

また本発明の応用として、本発明の純化方法で純化した
In溶液に基板を接触させることによりこの基板上にI
n系薄膜を成長させれば、高純度InP、InGaAs
P、InGaAs薄膜を容易に得られる利点がある。
Further, as an application of the present invention, the substrate is brought into contact with the In solution purified by the purification method of the present invention to form I on the substrate.
If n-type thin film is grown, high purity InP, InGaAs
There is an advantage that a P, InGaAs thin film can be easily obtained.

さらに本発明の純化方法ではIn溶液中の残留不純物濃
度を減少させる事ができるので、これを液相エピタキシ
ャル成長法に応用すれば、FeあるいはNi等の遷移金
属を添加した高抵抗InP、InGaAsP、InGa
As薄膜を容易に取得できる。
Furthermore, since the residual impurity concentration in the In solution can be reduced by the purification method of the present invention, if this is applied to the liquid phase epitaxial growth method, high resistance InP, InGaAsP, InGa doped with a transition metal such as Fe or Ni can be applied.
As thin film can be easily obtained.

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

第1図は本発明のCo添加と無添加のIn溶液を用いて交互
に成長させたInP薄膜の成長回数に対する77°Kにおけ
る移動度の測定値、第2図はCoを添加In溶液を用いて成
長させたInP薄膜のCo添加量に対する77°Kにおける移
動度の測定値、第3図はCo添加と無添加のIn溶液を用い
て交互に成長させたInP薄膜の成長回数に対する77°K
における移動度の測定値である。
FIG. 1 is a measured value of the mobility at 77 ° K with respect to the number of times of growth of an InP thin film alternately grown using a Co-added and non-added In solution of the present invention, and FIG. 2 uses a Co-added In solution. Of the InP thin film grown by heating at 77 ° K with respect to the Co addition amount, Fig. 3 shows 77 ° K with respect to the number of times of growth of the InP thin film alternately grown using the Co solution and the In solution not added.
It is the measured value of the mobility in.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】インジウムを溶媒とするインジウム溶液の
純化方法において、インジウム、インジウムを含むIII
−V族化合物半導体材料及び少なくともコバルトを加熱
溶融してインジウム溶液を純化させることを特徴とする
インジウム溶液の純化方法。
1. A method of purifying an indium solution using indium as a solvent, comprising indium and indium-containing III.
A method for purifying an indium solution, which comprises heating a Group V compound semiconductor material and at least cobalt to heat and purify the indium solution.
【請求項2】前記加熱溶融工程は前記インジウム、前記
III−V族化合物半導体材料及び前記コバルトを一緒に
加熱溶融することを特徴とする特許請求の範囲第1項記
載のインジウム溶液の純化方法。
2. The heating and melting step is performed on the indium and the indium.
The method for purifying an indium solution according to claim 1, wherein the III-V compound semiconductor material and the cobalt are heated and melted together.
【請求項3】前記加熱溶融工程は前記インジウムと前記
コバルトを一旦加熱溶融し、その後前記III−V族化合
物半導体材料を加え、再び加熱溶融する二つの工程を含
んでいることを特徴とする特許請求の範囲第1項記載の
インジウム溶液の純化方法。
3. The heating and melting step includes two steps of once heating and melting the indium and the cobalt, then adding the III-V compound semiconductor material, and again heating and melting. The method for purifying an indium solution according to claim 1.
JP4715584A 1984-03-14 1984-03-14 Method for purifying indium solution using indium as solvent Expired - Lifetime JPH0610085B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publication Number Publication Date
JPS60195011A JPS60195011A (en) 1985-10-03
JPH0610085B2 true JPH0610085B2 (en) 1994-02-09

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