JPS6054919B2 - low pressure reactor - Google Patents
low pressure reactorInfo
- Publication number
- JPS6054919B2 JPS6054919B2 JP9319776A JP9319776A JPS6054919B2 JP S6054919 B2 JPS6054919 B2 JP S6054919B2 JP 9319776 A JP9319776 A JP 9319776A JP 9319776 A JP9319776 A JP 9319776A JP S6054919 B2 JPS6054919 B2 JP S6054919B2
- Authority
- JP
- Japan
- Prior art keywords
- tube
- reaction
- low
- pressure
- gas
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
Landscapes
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Crystals, And After-Treatments Of Crystals (AREA)
Description
【発明の詳細な説明】
本発明は低圧反応装置及びそれによる反応処理方法例
えは低圧反応装置による半導体装置の製造方法に関する
。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a low-pressure reactor and a reaction processing method using the same, such as a method for manufacturing a semiconductor device using a low-pressure reactor.
低圧反応装置としては第1図に示すように石英ガラス
で円筒状に形成した反応管2を横方向に設け、この中の
サセプタ4にSiウェーハ5を支持させて挿入しウェー
ハ5に気相成長(Siエピタキシャル、Si多結晶など
)を行うものが考えられる。As shown in FIG. 1, the low-pressure reactor is equipped with a cylindrical reaction tube 2 made of quartz glass installed laterally, into which a Si wafer 5 is supported and inserted into a susceptor 4, and the wafer 5 undergoes vapor phase growth. (Si epitaxial, Si polycrystalline, etc.) can be considered.
しかし、このような低圧反応装置においては、反応管
2の内壁に反応物質が付着し易く、とくにモノシラン(
SiH、)と反応ガスとして用いた場合には、その分解
温度が400℃以下と低いためにとくに付着が激しく、
このため反応ガスの流れ方向に沿つて成長層の厚さのば
らつきが生じることが判つた。また一方反応管として角
形の反応管を用いた場合にはその耐圧が低いため、低圧
反応にはむかないことが判つた。 本発明はこのような
反応装置の欠点を解消する ものであつて、その目的と
するところは気相成長層の厚さのばらつきが少なくかつ
反応管内の汚染度の少ない低圧反応装置を提供するにあ
る。However, in such a low-pressure reactor, reactants tend to adhere to the inner wall of the reaction tube 2, especially monosilane (
When used as a reaction gas with SiH,), the decomposition temperature is as low as 400°C or less, so the adhesion is particularly severe.
It was found that this caused variations in the thickness of the grown layer along the flow direction of the reactant gas. On the other hand, when a rectangular reaction tube is used as the reaction tube, it has been found that it is not suitable for low-pressure reactions because of its low pressure resistance. The present invention aims to eliminate these drawbacks of the reactor, and its purpose is to provide a low-pressure reactor with less variation in the thickness of the vapor-phase growth layer and with less contamination in the reaction tube. be.
また他の目的はエピタキシャル成長の場合に上記に加え
てオートドーピングの少ない低圧エピタキシャル装置を
提供するにある。 このような目的を達成するための本
発明の要旨は、被処理体を収納し、反応ガスが導入され
る内側管と、上記内側管を囲む外側管と、上記外側管外
部に存在する加熱源とを有し、上記内側管と外側管との
間にガスを流しかつ上記内側管内に反応ガスを導入して
上記被処理体を処理することを特徴とする低圧反応装置
にある。Another object of the present invention is to provide a low-pressure epitaxial device in which autodoping is reduced in the case of epitaxial growth. The gist of the present invention for achieving such objects is to provide an inner tube that houses the object to be processed and into which a reaction gas is introduced, an outer tube that surrounds the inner tube, and a heating source that is present outside the outer tube. A low-pressure reaction apparatus is characterized in that the object to be processed is treated by flowing a gas between the inner tube and the outer tube and introducing a reaction gas into the inner tube.
以下添付図面に関連して本発明の実施例について説明す
る。 第2図は本発明の低圧反応装置の一部を省略した
斜視図、第3図は第2図を矢印方向から見た図である。Embodiments of the present invention will be described below with reference to the accompanying drawings. FIG. 2 is a partially omitted perspective view of the low-pressure reactor of the present invention, and FIG. 3 is a view of FIG. 2 viewed from the direction of the arrow.
この低圧反応装置10は石英ガラスでつくつた円形ない
しは楕円の筒状保護管11を有し、これを横にねかせて
配置し、この内側には石”英ガラスて矩形筒状に形成し
た角形反応管12を保護管11の中心軸に沿うように挿
入し、角形反応管12の外側に高周波誘導加熱用の高周
波コイル(RFコイル)13をまきつけて管12内には
シリコンカーバイトSiCをコートしたグラフアイ、ト
製のサセプタ14を入れ、その上にSiウェーハ15を
載置する。そして、角形反応管12内に鴇またはN2な
どのキャリヤガスを流しながら図示しない真空ポンプで
、たとえば0.1〜300T′0mの範囲の一定圧力の
低圧に保持する。また、角形反応管12と保護管11の
間も同時に低圧に保持しながら鴇またはN2などの冷却
ガスを流し、この際、反応管12の破壊を防止するため
反応管12の内外の圧力のバランスを取る。すなわち、
内外管の間の圧力は反応管12と同等かまたは多少高い
たとえば1.1〜2倍程度にする。そして、高周波コイ
ル(RFコイル)13の高周波誘導加熱によりサセプタ
14を所定の温度(反応目的、反応ガスによつて異なる
が約500〜1200゜Cの範囲の一定温度)に加熱し
、反応管12内に流した反応ガスで低圧下で反応させ、
Sfウェーハ15上に気層成長層を形成する。This low-pressure reactor 10 has a circular or elliptical cylindrical protection tube 11 made of quartz glass, which is placed horizontally, and inside this is a prismatic reaction tube made of quartz glass and formed into a rectangular tube shape. The tube 12 was inserted along the central axis of the protective tube 11, a high frequency coil (RF coil) 13 for high frequency induction heating was wound around the outside of the rectangular reaction tube 12, and the inside of the tube 12 was coated with silicon carbide SiC. A susceptor 14 made by Graphai Co., Ltd. is placed thereon, and a Si wafer 15 is placed thereon.Then, while a carrier gas such as carbon dioxide or N2 is flowing into the rectangular reaction tube 12, a vacuum pump (not shown) is used to reduce the The pressure is maintained at a constant low pressure in the range of ~300T'0m.Also, a cooling gas such as carbon dioxide or N2 is flowed between the rectangular reaction tube 12 and the protection tube 11 while maintaining the pressure at a low level at the same time. Balance the pressure inside and outside the reaction tube 12 to prevent destruction of the reaction tube 12. In other words,
The pressure between the inner and outer tubes is equal to or slightly higher than that of the reaction tube 12, for example, about 1.1 to 2 times. Then, the susceptor 14 is heated to a predetermined temperature (a constant temperature in the range of approximately 500 to 1200°C depending on the reaction purpose and reaction gas) by high-frequency induction heating of the high-frequency coil (RF coil) 13, and the reaction tube 12 The reaction is carried out under low pressure with the reaction gas flowing inside.
A vapor layer growth layer is formed on the Sf wafer 15.
前述した反応ガスはたとえば、被処理体であるSiウェ
ーハ上にSi多結晶を成長させる場合にはN2+SiH
4を、Si単結晶を成長させる場合にはH2+Si桟+
ドーパワト(PH3、B5H6など)を用いる。The above-mentioned reactive gas is, for example, N2+SiH when growing Si polycrystals on a Si wafer to be processed.
4, when growing Si single crystal, H2 + Si crosspiece +
Dopower (PH3, B5H6, etc.) is used.
なおSfH4の代りにSiCl4,SiHCl3,Si
H2Cl2などを使用してもよい。また、高周波コイル
(RFコイル)13は保護管11の外側に巻いてもよく
、この高周波コイル(RFコイル)13に代えてランプ
で加熱する構造のものでもよい。また、冷却ガスはH2
,H2以外にH2Olフレオンなどの蒸気でもよく、成
長させる材料はSiのみでなくSl3N4,SiO2,
Af2O3のような化合物(CVD成長)でもよく。Note that SiCl4, SiHCl3, Si
H2Cl2 etc. may also be used. Further, the high frequency coil (RF coil) 13 may be wound on the outside of the protective tube 11, and instead of this high frequency coil (RF coil) 13, a structure may be used in which heating is performed using a lamp. In addition, the cooling gas is H2
, H2, vapors such as H2Ol Freon may be used, and the materials to be grown are not only Si but also Sl3N4, SiO2,
Compounds such as Af2O3 (CVD grown) may also be used.
GaA3,GaPのような化合物半導体(とくに有機化
合物を反応ガスとするもの)の成長てもよい。なお、前
記実施例においては外側の保護管11を石英ガラスでつ
くつているが、これを金属管とし、図示しない温度測定
用の窓を設けたものでもよい。Compound semiconductors such as GaA3 and GaP (especially those using an organic compound as a reactive gas) may be grown. In the above embodiment, the outer protective tube 11 is made of quartz glass, but it may also be a metal tube provided with a temperature measurement window (not shown).
このような金属管においては耐圧が高いから角形管が使
用でき、装置が大形の場合には金属,管の方が製造し易
い利点がある。第4図は本発明の他の実施例であつて、
反応管12、保護管11はともに石英ガラスでつくり、
これらを溶接して一体化し、高周波コイル(RFコイル
)13を保護管11の外側に巻いたものである。第5図
、第6図は本発明のさらに他の実施態様である。Among such metal tubes, rectangular tubes can be used because of their high pressure resistance, and if the device is large, metal tubes have the advantage of being easier to manufacture. FIG. 4 shows another embodiment of the present invention,
Both the reaction tube 12 and the protection tube 11 are made of quartz glass.
These are welded and integrated, and a high frequency coil (RF coil) 13 is wound around the outside of the protective tube 11. FIGS. 5 and 6 show still other embodiments of the present invention.
第5図において、反応管12、保護管11はともに石英
ガラス製で溶接し、反応ガス供給室16、反応室17、
排気ガス排出室18および冷却室19に区分したもので
ある。反応ガス供給室16と反応室17との間に石英ガ
ラスの多孔質板からなるガス分配器20を設け、反応ガ
スがウェーハ15の列の直角方向から均一に流れるよう
にしてある。この様子は第6図の平面図で図示してある
が、また反応室17と排気ガス排出室18との間に石英
ガラスの穴あき板21を設け、反応後の排気ガスを真空
ポンプですみやかに排出する・造のものである。この場
合には反応ガスが各ウェーハ15に均一に流れるので成
長層のばらつきが非常に少なくなる。上記種々な実施例
で示したように本発明の低圧反応装置は以下のような特
長を有している。In FIG. 5, the reaction tube 12 and the protection tube 11 are both made of quartz glass and welded together, and the reaction gas supply chamber 16, reaction chamber 17,
It is divided into an exhaust gas discharge chamber 18 and a cooling chamber 19. A gas distributor 20 made of a porous plate of quartz glass is provided between the reaction gas supply chamber 16 and the reaction chamber 17, so that the reaction gas flows uniformly from a direction perpendicular to the rows of wafers 15. This situation is illustrated in the plan view of FIG. 6, but a perforated quartz glass plate 21 is provided between the reaction chamber 17 and the exhaust gas discharge chamber 18, and the exhaust gas after the reaction can be quickly removed by a vacuum pump. It is a product that is discharged and manufactured. In this case, since the reaction gas flows uniformly to each wafer 15, variations in the growth layer are greatly reduced. As shown in the various examples above, the low pressure reactor of the present invention has the following features.
反応管12と保護管11の二重構造とし、しかもその間
を反応管内部の低圧とバランスをとつた低圧にすること
から反応管12に耐圧の低い石英ガラス製の角形構造を
とることができること、また反応管12と保護管11の
間に冷却ガスを流すために反応管12の内壁への反応物
質の付着を防止でき、反応ガスの流れ方向の厚さのばら
つきが少なくなること、しかも角形反応管12てあるた
め反応ガスの直角方向のばらつきが少なくなること、反
応管12は石英ガラスてしかも構造が簡単てあるため、
装置内部からの汚染の少ない反応装置てあることなど数
々の効果が得られる。また本発明を低圧エピタキシャル
装置とする場合には上記効果に加えて低圧成長であるた
めオートドーピングが少なくなるという効果を発揮する
。又、第7図に示すように本発明を縦型反応装置に適用
した場合には、上記利点の他に、内側の管内の圧力をよ
り低圧にすることができる。The reaction tube 12 has a double structure of the reaction tube 12 and the protection tube 11, and the low pressure between them is balanced with the low pressure inside the reaction tube, so that the reaction tube 12 can have a rectangular structure made of quartz glass with low pressure resistance. In addition, since the cooling gas flows between the reaction tube 12 and the protection tube 11, it is possible to prevent the reactants from adhering to the inner wall of the reaction tube 12, and the thickness variation in the flow direction of the reaction gas is reduced. The reaction tube 12 is made of quartz glass and has a simple structure, so the variation in the reaction gas in the perpendicular direction is reduced.
Numerous benefits can be obtained, including a reactor with less contamination from inside the device. Furthermore, when the present invention is applied to a low-pressure epitaxial device, in addition to the above-mentioned effects, autodoping is reduced due to low-pressure growth. Furthermore, when the present invention is applied to a vertical reactor as shown in FIG. 7, in addition to the above advantages, the pressure inside the inner tube can be lowered.
第1図は低圧反応装置の断面図、第2図は本発明の低圧
反応装置の一部を省略した斜視図、第3図は第2図を矢
印方向に見た拡大図、第4図〜第7図は本発明の反応装
置の他の実施例を示す図である。
2・・・・・・反応管、4・・・・・・サセプタ、5・
・・・・・Siウェーハ、10・・・・・・低圧反応装
置、11・・・・・・筒形保護管、12・・・・・・角
形反応管、13・・・・・・高周波コイル(RFコイル
)、14・・・・・・サセプタ、15・・・・・・Si
ウェーハ、16・・・・・・反応ガス供給室、17・・
・・・・反応室、18・・・・・・排気ガス排出室、1
9・・・・・・冷却室、20・・・・・・ガス分配器、
21・・・・・・穴あき板、22・・・●●●ベルジヤ
ー。FIG. 1 is a cross-sectional view of the low-pressure reactor, FIG. 2 is a partially omitted perspective view of the low-pressure reactor of the present invention, FIG. 3 is an enlarged view of FIG. 2 viewed in the direction of the arrow, and FIGS. FIG. 7 is a diagram showing another embodiment of the reaction apparatus of the present invention. 2...Reaction tube, 4...Susceptor, 5.
... Si wafer, 10 ... Low pressure reaction device, 11 ... Cylindrical protection tube, 12 ... Square reaction tube, 13 ... High frequency Coil (RF coil), 14...susceptor, 15...Si
Wafer, 16...Reaction gas supply chamber, 17...
...Reaction chamber, 18...Exhaust gas discharge chamber, 1
9... Cooling room, 20... Gas distributor,
21...Perforated board, 22...●●●Belgear.
Claims (1)
、上記内側管を囲む外側管と、上記外側管外部に存在す
る加熱源とを有し、上記内側管と外側管との間にガスを
流しかつ上記内側管内に反応ガスを導入して上記被処理
体を処理することを特徴とする低圧反応装置。1 An inner tube that houses the object to be processed and into which a reaction gas is introduced, an outer tube that surrounds the inner tube, and a heat source that is present outside the outer tube, and has a A low-pressure reaction apparatus characterized in that the object to be processed is processed by flowing gas through the inner tube and introducing a reaction gas into the inner tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9319776A JPS6054919B2 (en) | 1976-08-06 | 1976-08-06 | low pressure reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9319776A JPS6054919B2 (en) | 1976-08-06 | 1976-08-06 | low pressure reactor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5319181A JPS5319181A (en) | 1978-02-22 |
| JPS6054919B2 true JPS6054919B2 (en) | 1985-12-02 |
Family
ID=14075844
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9319776A Expired JPS6054919B2 (en) | 1976-08-06 | 1976-08-06 | low pressure reactor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6054919B2 (en) |
Families Citing this family (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5591815A (en) * | 1978-12-29 | 1980-07-11 | Fujitsu Ltd | Silicon epitaxial growth |
| JPS5648127A (en) * | 1979-09-26 | 1981-05-01 | Fujitsu Ltd | Epitaxial growth |
| JPS5698823A (en) * | 1980-01-09 | 1981-08-08 | Nec Corp | Method of vapor growth of semiconductor of 3-5 group compound |
| JPS5773174A (en) * | 1980-10-24 | 1982-05-07 | Semiconductor Energy Lab Co Ltd | Manufacturing apparatus for coating film |
| JPS57184213A (en) * | 1981-05-08 | 1982-11-12 | Kokusai Electric Co Ltd | Vapor growth device for semiconductor |
| JPS58169907A (en) * | 1982-03-30 | 1983-10-06 | Fujitsu Ltd | Apparatus for producting thin film |
| JPS58181796A (en) * | 1982-04-19 | 1983-10-24 | Matsushita Electric Ind Co Ltd | Method for growing crystal |
| JPS58209113A (en) * | 1982-05-31 | 1983-12-06 | Semiconductor Energy Lab Co Ltd | Purification of reactive gas for semiconductor |
| JPS59104117A (en) * | 1982-12-06 | 1984-06-15 | Agency Of Ind Science & Technol | Vacuum deposition device |
| JPS59158437U (en) * | 1983-04-08 | 1984-10-24 | 富士通株式会社 | Vapor phase growth equipment |
| JP2526219B2 (en) * | 1986-10-23 | 1996-08-21 | 日立フェライト 株式会社 | Lumped constant type circulator and isolator |
| JPS63164426A (en) * | 1986-12-26 | 1988-07-07 | Fujitsu Ltd | Vapor phase epitaxy method |
| JPH027419A (en) * | 1988-06-24 | 1990-01-11 | Toshiba Mach Co Ltd | Vapor growth apparatus |
| US5781693A (en) * | 1996-07-24 | 1998-07-14 | Applied Materials, Inc. | Gas introduction showerhead for an RTP chamber with upper and lower transparent plates and gas flow therebetween |
-
1976
- 1976-08-06 JP JP9319776A patent/JPS6054919B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5319181A (en) | 1978-02-22 |
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