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JPH0140000B2 - - Google Patents
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JPH0140000B2 - - Google Patents

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Publication number
JPH0140000B2
JPH0140000B2 JP56180845A JP18084581A JPH0140000B2 JP H0140000 B2 JPH0140000 B2 JP H0140000B2 JP 56180845 A JP56180845 A JP 56180845A JP 18084581 A JP18084581 A JP 18084581A JP H0140000 B2 JPH0140000 B2 JP H0140000B2
Authority
JP
Japan
Prior art keywords
carbon
boat
impurities
epitaxial layer
heat treatment
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
JP56180845A
Other languages
Japanese (ja)
Other versions
JPS5884181A (en
Inventor
Toshiharu Kawabata
Susumu Furuike
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 JP56180845A priority Critical patent/JPS5884181A/en
Publication of JPS5884181A publication Critical patent/JPS5884181A/en
Publication of JPH0140000B2 publication Critical patent/JPH0140000B2/ja
Granted legal-status Critical Current

Links

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  • Crystals, And After-Treatments Of Crystals (AREA)
  • Ceramic Products (AREA)
  • Carbon And Carbon Compounds (AREA)

Description

【発明の詳細な説明】 本発明は半導体基板へのエピタキシヤル成長、
不純物ドーピングなどに用いるカーボンボート、
基板支持などのカーボン部材の純化処理方法に関
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to epitaxial growth on a semiconductor substrate,
Carbon boats used for impurity doping, etc.
The present invention relates to a method for purifying carbon members such as substrate supports.

エピタキシヤル成長の技術は半導体素子の形成
に当り広く用いられ、特に燐化ガリウム(GaP)、
砒化ガリウム(GaAs)等の―化合物半導体
素子の形成に欠くことのできない方法である。そ
して―化合物半導体の不純物としてドーピン
グされる元素は、ドナーとしてS、Te、Si等が、
アクセプタとしてZn、Mg、Si等が用いられる。
Epitaxial growth techniques are widely used in the formation of semiconductor devices, especially gallium phosphide (GaP),
This is an indispensable method for forming compound semiconductor devices such as gallium arsenide (GaAs). And - elements doped as impurities in compound semiconductors include S, Te, Si, etc. as donors,
Zn, Mg, Si, etc. are used as acceptors.

通常エピタキシヤル成長用ボート部材には石英
あるいはカーボンが用いられるが、酸素やSiの汚
染を防止するためにはカーボンを用いなければな
らない。しかしながら一般にボートのカーボン部
材には非結晶粒子の焼結体が用いられ、これは、
しばしば不純物を吸収、吸着したり、あるいは不
純物と化学反応を起すことがある。とりわけ、エ
ピタキシヤル成長時にカーボンボートは上述のよ
うに種々の不純物と接するため、この工程で汚染
される。そして、カーボンボートが汚染されたま
ま、あるいはその純化処理が不十分であれば、次
に成長するエピタキシヤル層は汚染され半導体素
子の特性は大きな影響を受ける。特に低不純物濃
度のエピタキシヤル層を成長する場合、その影響
は大きい。
Quartz or carbon is usually used for epitaxial growth boat members, but carbon must be used to prevent oxygen and Si contamination. However, generally, a sintered body of amorphous particles is used for carbon parts of boats, and this
They often absorb, adsorb, or chemically react with impurities. Particularly, during epitaxial growth, the carbon boat comes into contact with various impurities as described above and is therefore contaminated during this process. If the carbon boat remains contaminated or its purification treatment is insufficient, the epitaxial layer to be grown next will be contaminated and the characteristics of the semiconductor device will be greatly affected. This effect is particularly large when growing an epitaxial layer with a low impurity concentration.

たとえば、n型基板上にn型エピタキシヤル層
を形成しさらにp型層を形成した構造の窒素
(N)ドープGaP(緑色)あるいはGaAsP(黄色)
発光ダイオード(LED)は、n型層のドナー濃
度が低下する程発光出力は増加するため、低ドナ
ー濃度のエピタキシヤル層を成長することが必要
となる。しかしカーボンボートの純化処理が不十
分でドナー不純物が残つていた場合、低濃度のエ
ピタキシヤル層の成長は不可能で、発光出力は低
下する。また、ドナー不純物を取除いてもアクセ
プタ不純物が残つていた場合、n型層の一部がp
型に反転する特性不良が発生する。
For example, nitrogen (N)-doped GaP (green) or GaAsP (yellow) has a structure in which an n-type epitaxial layer is formed on an n-type substrate and a p-type layer is further formed.
In light emitting diodes (LEDs), the emission output increases as the donor concentration of the n-type layer decreases, so it is necessary to grow an epitaxial layer with a low donor concentration. However, if the purification process of the carbon boat is insufficient and donor impurities remain, it is impossible to grow a low concentration epitaxial layer and the light emitting output decreases. In addition, if acceptor impurities remain even after removing donor impurities, part of the n-type layer may
A characteristic defect occurs in which the mold is reversed.

一般に、エピタキシヤル層にドーピングされる
元素のうち、族元素のZn、Mg等や族元素の
Si等は蒸発しにくく、単に熱処理するだけではカ
ーボンボートから完全に取除くことはできない。
また族元素S、Te等はそれ自身は蒸発しやす
いが、カーボンと化合物を形成しやすく、単に熱
処理するだけでは完全に取除くことはできない。
In general, among the elements doped into the epitaxial layer, group elements Zn, Mg, etc.
Si etc. are difficult to evaporate and cannot be completely removed from the carbon boat simply by heat treatment.
Group elements S, Te, etc. easily evaporate by themselves, but tend to form compounds with carbon, and cannot be completely removed simply by heat treatment.

本発明は上述の問題を解決するものであり、す
べての不純物を完全に除去し高純度なエピタキシ
ヤル層を得るためのカーボンボートの純化処理方
法を提供するものである。
The present invention solves the above problems and provides a method for purifying carbon boats to completely remove all impurities and obtain a highly pure epitaxial layer.

図に本発明の方法を実施するためのカーボン純
化処理装置の一例の概略図を示す。まず第1工程
として、族元素のZn、Mg等や族元素のSi等
を取除くために、ハロゲンを含むガス雰囲気たと
えば塩化水素中でカーボンボート1を石英炉管2
内に配置し、ヒータ3でこれらを1000℃に保ち、
3時間程度熱処理する。この工程で、これらの元
素は塩化物となり蒸発しやすくなる。しかし塩化
物でもカーボンボートの奥深くに吸着されたもの
は完全に取除くことはできない。そこで第2工程
として塩化物となつた族あるいは族元素を完
全に取除くために、真空ポンプ4で排気した減圧
中でこのカーボンボートを1000℃で4時間程度熱
処理する。減圧によりカーボンボートの奥深く吸
着された塩化物も蒸発してカーボンボートから取
除くことができる。さらに第3工程として族元
素S、Te等を取除くために還元性雰囲気たとえ
ば水素中でカーボンボートを1000℃で5時間程度
熱処理する。この工程により、カーボンと化合物
を形成している族元素も水素化物となり蒸発し
てカーボンボートから取除くことができる。
The figure shows a schematic diagram of an example of a carbon purification treatment apparatus for carrying out the method of the present invention. First, in the first step, in order to remove group elements such as Zn, Mg, etc. and group elements such as Si, a carbon boat 1 is placed in a quartz furnace tube 2 in a gas atmosphere containing halogen, such as hydrogen chloride.
and keep them at 1000℃ with heater 3.
Heat treat for about 3 hours. In this process, these elements become chlorides and easily evaporate. However, even chloride cannot completely remove what is adsorbed deep inside the carbon boat. Therefore, as a second step, the carbon boat is heat-treated at 1000° C. for about 4 hours in a reduced pressure evacuated by a vacuum pump 4 in order to completely remove the group or group elements that have become chlorides. Due to the reduced pressure, chloride adsorbed deep within the carbon boat can also be evaporated and removed from the carbon boat. Furthermore, as a third step, the carbon boat is heat-treated at 1000° C. for about 5 hours in a reducing atmosphere, such as hydrogen, in order to remove group elements S, Te, etc. Through this step, the group elements forming compounds with carbon also become hydrides and can be evaporated and removed from the carbon boat.

このようにして純化したカーボンボートを用い
GaP(緑色)LEDを液相エピタキシヤル成長によ
り形成した場合、発光出力が高く、かつ素子とし
ての特性が優れたものが得られた。一方、かかる
効果を確認するために、第1あるいは第2工程を
省略した場合、n型層の1部がp型層になる特性
不良が発生した。また第3工程を省略した場合、
高ドナー濃度層が成長し発光出力が極端に低下し
た。
Using the carbon boat purified in this way,
When a GaP (green) LED was formed by liquid-phase epitaxial growth, a device with high light output and excellent device characteristics was obtained. On the other hand, when the first or second step was omitted in order to confirm this effect, a characteristic defect occurred in which part of the n-type layer became a p-type layer. Also, if the third step is omitted,
A high donor concentration layer grew and the luminescence output decreased dramatically.

このようにカーボンボートの純化処理は第1、
第2、さらに第3工程を引続き行うことが必要
で、どれ1つ欠けても高純度なエピタキシヤル層
の成長は不可能である。またドナーかアクセプタ
不純物のどちらか1方しかドーピンゲしないエピ
タキシヤル成長であつても、水や石英等からのSi
やその他の物質の汚染は避けられない。従つて上
記の3つの工程は必要になるとともに、各工程の
熱処理温度は950℃〜1200℃が望ましい。
In this way, the first step in the purification process for carbon boats is
It is necessary to perform the second and third steps successively, and if any one of them is missing, it is impossible to grow a highly pure epitaxial layer. Also, even in epitaxial growth where only one of donor or acceptor impurities is doped, Si from water, quartz, etc.
and other substances are unavoidable. Therefore, the above three steps are necessary, and the heat treatment temperature in each step is preferably 950°C to 1200°C.

以上説明してきたところから明らかなように、
本発明によればカーボンボートに吸着したすべて
の不純物を完全に取除くことができ、高純度なエ
ピタキシヤル層の成長が可能となる。かかる本発
明の方法によれば、高純度なエピタキシヤル層を
有する高効率発光ダイオードや他の素子を生産す
ることが可能である。
As is clear from what has been explained above,
According to the present invention, all impurities adsorbed on the carbon boat can be completely removed, making it possible to grow a highly pure epitaxial layer. According to the method of the present invention, it is possible to produce highly efficient light emitting diodes and other devices having highly pure epitaxial layers.

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

図はカーボンボートの純化処理装置の概略図で
ある。 1……カーボンボート、2……石英反応管、3
……ヒーター、4……真空ポンプ。
The figure is a schematic diagram of a carbon boat purification treatment device. 1... Carbon boat, 2... Quartz reaction tube, 3
...Heater, 4...Vacuum pump.

Claims (1)

【特許請求の範囲】[Claims] 1 ハロゲンを含むガス雰囲気中で熱処理する第
1工程と、減圧あるいは真空中で熱処理する第2
工程と、還元性ガス雰囲気中で熱処理する第3工
程とを備えたことを特徴とするカーボン部材の純
化処理方法。
1 The first step is heat treatment in a gas atmosphere containing halogen, and the second step is heat treatment in reduced pressure or vacuum.
1. A method for purifying a carbon member, comprising the steps of: and a third step of performing heat treatment in a reducing gas atmosphere.
JP56180845A 1981-11-11 1981-11-11 Carbon member purifying treatment Granted JPS5884181A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56180845A JPS5884181A (en) 1981-11-11 1981-11-11 Carbon member purifying treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56180845A JPS5884181A (en) 1981-11-11 1981-11-11 Carbon member purifying treatment

Publications (2)

Publication Number Publication Date
JPS5884181A JPS5884181A (en) 1983-05-20
JPH0140000B2 true JPH0140000B2 (en) 1989-08-24

Family

ID=16090357

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56180845A Granted JPS5884181A (en) 1981-11-11 1981-11-11 Carbon member purifying treatment

Country Status (1)

Country Link
JP (1) JPS5884181A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2163519A2 (en) 2008-09-16 2010-03-17 Mitsubishi Materials Corporation Method of refining carbon parts for production of polycrystalline silicon

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5921598A (en) * 1982-07-27 1984-02-03 Matsushita Electric Ind Co Ltd Treatment for purification of carbon member
JPS6065793A (en) * 1983-09-22 1985-04-15 Matsushita Electric Ind Co Ltd Vapor-phase growing method
JPH0753635B2 (en) * 1986-07-08 1995-06-07 電気化学工業株式会社 Glassy carbon coated susceptor and method for producing the same
JPH0635325B2 (en) * 1986-09-22 1994-05-11 東洋炭素株式会社 Method for producing high-purity graphite material
JPH0780684B2 (en) * 1987-04-06 1995-08-30 東芝セラミツクス株式会社 Carbon material purification equipment
JPH0729762B2 (en) * 1987-04-06 1995-04-05 東芝セラミツクス株式会社 Carbon material purification method
JPH01104000A (en) * 1987-10-15 1989-04-21 Nippon Mining Co Ltd Production of crystal
JP2519071B2 (en) * 1987-11-30 1996-07-31 東洋炭素 株式会社 Method for producing carbon material with low outgas
JPH07106941B2 (en) * 1988-02-01 1995-11-15 三井造船株式会社 Method for cleaning graphite member
JPH0678193B2 (en) * 1988-03-18 1994-10-05 東洋炭素株式会社 Carbon fiber reinforced carbon composite material excellent in thermal shock resistance and method for producing the same
JPH02225312A (en) * 1989-01-20 1990-09-07 Toshiba Ceramics Co Ltd Purification of carbon-graphite material
JP2684106B2 (en) * 1990-02-22 1997-12-03 東洋炭素株式会社 Graphite base material for ceramic coating and internal parts for CVD furnace
JP2620606B2 (en) * 1990-05-16 1997-06-18 東洋炭素株式会社 High purity flexible expanded graphite sheet and method for producing the same
JP4880624B2 (en) * 2008-01-28 2012-02-22 東洋炭素株式会社 Vapor growth susceptor and method of manufacturing the same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2163519A2 (en) 2008-09-16 2010-03-17 Mitsubishi Materials Corporation Method of refining carbon parts for production of polycrystalline silicon
EP2505555A1 (en) 2008-09-16 2012-10-03 Mitsubishi Materials Corporation Method of refining carbon parts for production of polycrystalline silicon

Also Published As

Publication number Publication date
JPS5884181A (en) 1983-05-20

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