JPS61248519A - Chemical vapor deposition apparatus - Google Patents
Chemical vapor deposition apparatusInfo
- Publication number
- JPS61248519A JPS61248519A JP9010885A JP9010885A JPS61248519A JP S61248519 A JPS61248519 A JP S61248519A JP 9010885 A JP9010885 A JP 9010885A JP 9010885 A JP9010885 A JP 9010885A JP S61248519 A JPS61248519 A JP S61248519A
- Authority
- JP
- Japan
- Prior art keywords
- shower
- substrate
- gas
- processed
- feed
- 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.)
- Pending
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/02—Manufacture or treatment of semiconductor devices or of parts thereof
- H01L21/02104—Forming layers
- H01L21/02365—Forming inorganic semiconducting materials on a substrate
- H01L21/02518—Deposited layers
- H01L21/02521—Materials
- H01L21/02524—Group 14 semiconducting materials
- H01L21/02532—Silicon, silicon germanium, germanium
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/02—Manufacture or treatment of semiconductor devices or of parts thereof
- H01L21/02104—Forming layers
- H01L21/02365—Forming inorganic semiconducting materials on a substrate
- H01L21/02612—Formation types
- H01L21/02617—Deposition types
- H01L21/0262—Reduction or decomposition of gaseous compounds, e.g. CVD
Abstract
Description
【発明の詳細な説明】
〔概要〕
チャンバ内に反応ガスを供給するシャワーの形状を円筒
形として容量を増すと共に、冷却管を備えてシャワー内
の反応を防止した化学気相成長装置。DETAILED DESCRIPTION OF THE INVENTION [Summary] A chemical vapor deposition apparatus in which a shower for supplying a reaction gas into a chamber has a cylindrical shape to increase capacity, and a cooling pipe is provided to prevent reactions within the shower.
本発明は反応ガスの濃度分布を良くすると共にシャワー
内反応を防止したシャワーを備えた化学気相成長装置に
関する。The present invention relates to a chemical vapor deposition apparatus equipped with a shower that improves the concentration distribution of reaction gas and prevents reactions within the shower.
化学気相成長(Chemical Vapor Dep
osition以下略してCVD)法は気相反応を利用
して所望の薄膜を基板上に形成するもので、半導体のエ
ピタキシャル成長を始めとし、半導体層、絶縁層、導体
層の成長など半導体素子の製造工程に広く使用されてい
る。Chemical Vapor Depth
The CVD method (abbreviated hereafter as CVD) is a method of forming a desired thin film on a substrate using a gas phase reaction, and is used in the manufacturing process of semiconductor devices, including the epitaxial growth of semiconductors, as well as the growth of semiconductor layers, insulating layers, and conductor layers. widely used.
すなわち半導体基板としてシリコン(Si)を用いる場
合を例とすると、エピタキシャル成長は塩化シリコン(
SiC1m )或いはジクロールシラン(Si112
C12)と112との混合物を1000〜1200℃の
高温で還元することにより行われており、またポリシリ
コン(ポリSt)の成長は600℃以上の比較的低温で
SiHaと112との熱分解反応により行われている。In other words, taking as an example the case where silicon (Si) is used as a semiconductor substrate, epitaxial growth is performed using silicon chloride (Si).
SiC1m ) or dichlorosilane (Si112
The growth of polysilicon (polySt) is carried out by reducing a mixture of C12) and 112 at a high temperature of 1000 to 1200°C, and the growth of polysilicon (polySt) is achieved by a thermal decomposition reaction between SiHa and 112 at a relatively low temperature of 600°C or higher. It is carried out by
また酸化シリコン(SiO2)のような絶縁物はSin
4と亜酸化窒素(No)とH2との混合ガスを700
℃以上の温度で分解することより形成しており、また導
体層は弗化タングステン(WF s )や塩化タングス
テン(WCIg )などを400℃以上の温度で熱分解
することにより基板上に薄層を形成し、これを写真食刻
技術(ホトリソグラフィ)により選択エツチングして各
種のパターンをつくり、半導体素子を形成している。Also, insulators such as silicon oxide (SiO2) are
4, nitrous oxide (No), and H2 mixed gas at 700
The conductor layer is formed by thermally decomposing tungsten fluoride (WFs) or tungsten chloride (WCIg) at a temperature of 400°C or higher to form a thin layer on the substrate. This is then selectively etched using photolithography to create various patterns to form semiconductor elements.
ここでCVD成長の特徴は反応ガスとして各種のガスお
よび混合ガスを使用し得ること、またステップ・カバー
レッジよく膜形成できることであるが成長速度を成るべ
く太き(して且つ均一な膜厚に成長させることが必要で
ある。The characteristics of CVD growth are that various gases and mixed gases can be used as reaction gases, and that films can be formed with good step coverage. It is necessary to grow it.
第2図は従来のCVD装置の構成を示すもので、排気系
に接続したチャンバ1の中には反応ガスを噴出するシャ
ブー2が上部にあり、これに対向して設けられているサ
セプタ3の上には被処理基板4が載置されている。Fig. 2 shows the configuration of a conventional CVD apparatus. Inside a chamber 1 connected to an exhaust system, there is a shabu 2 at the top for spouting a reaction gas, and a susceptor 3 is installed opposite to the shabu 2. A substrate 4 to be processed is placed thereon.
ここで、サセプタ3は内部に加熱源5を備えて構成され
ており、ヒータに通電してサセプタを加熱することによ
り、被処理基板4を所望の温度に保持できるようになっ
ている。Here, the susceptor 3 is configured to include a heating source 5 therein, and by heating the susceptor by supplying electricity to the heater, the substrate 4 to be processed can be maintained at a desired temperature.
また、このサセプタ3が設けられている装置基板には排
気ダクト6が設けられており、メカニカルブースタや回
転ポンプなどからなる排気系に接続している。Further, an exhaust duct 6 is provided on the device board on which the susceptor 3 is provided, and is connected to an exhaust system consisting of a mechanical booster, a rotary pump, and the like.
以下シリコン(Si)からなる被処理基板4の上にアル
ミニウム(AI)の薄層を形成する場合についてCVD
法を説明すると次ぎのようになる。The following describes the case of forming a thin layer of aluminum (AI) on the substrate 4 to be processed made of silicon (Si) using CVD.
The law is explained as follows.
排気系を動作させてチャンバ1の中を排気した状態でシ
ャワー2より反応ガスをチャンバ1の中に供給し、0.
3〜0.5Torr程度の真空度に保持する。While the exhaust system is operated to exhaust the inside of the chamber 1, a reaction gas is supplied into the chamber 1 from the shower 2, and 0.
The degree of vacuum is maintained at about 3 to 0.5 Torr.
ここでシャワー2の導入管7には図示を省略しであるが
、これにソースガス配管、キャリアガス配管9介解促進
ガス配管などがそれぞれ流量計を備えて設けられており
、正確に流量を調節して混合ガスが作られている。Although not shown, the inlet pipe 7 of the shower 2 is equipped with a source gas pipe, a carrier gas pipe 9, an catalytic gas pipe, and the like, each equipped with a flow meter to accurately measure the flow rate. A mixed gas is created by adjusting the
この例の場合、ソースガスとしてはトリイソブーチルア
ルミニウム(Al (CH2Cl(CHコ)2)コ〕を
、キャリアガスとしてはアルゴン(Ar)を、また分解
促進ガスとして水素(++ z )を用いて反応ガスが
構成されている。In this example, triisobutylaluminum (Al(CH2Cl(CH))2) is used as the source gas, argon (Ar) is used as the carrier gas, and hydrogen (++z) is used as the decomposition promoting gas. The reaction gas is composed of
これらのガスは混合された状態で導入管7を通ってシャ
ワー2に達し、この下面に設けである数多くの噴出孔8
より被処理基板4に向けて噴出している。These gases reach the shower 2 through the introduction pipe 7 in a mixed state, and a number of jet holes 8 are provided on the lower surface of the shower 2.
It is ejected more toward the substrate 4 to be processed.
然しなから、シャワー2と被処理基板4の間隔は30〜
40龍程度と僅かであり、一方被処理基板4はこの実施
例の場合、300℃に保持されているためシャワー2の
温度が上昇しており、シャワーの内部で分解反応が起こ
りやすい。However, the distance between the shower 2 and the substrate 4 to be processed is 30~
On the other hand, since the substrate 4 to be processed is maintained at 300° C. in this embodiment, the temperature of the shower 2 has increased, and a decomposition reaction is likely to occur inside the shower.
また混合ガスは導入管7より狭い容積からなるシャワー
2に供給されるため、これがシャワー内に広がった後、
数多く設けられている細孔から均等な流速で噴出するの
は容易ではなく、噴出孔8の設定位置や孔径などが大き
く影響するために条件の設定は容易ではなかった。Also, since the mixed gas is supplied to the shower 2 which has a smaller volume than the introduction pipe 7, after it spreads inside the shower,
It is not easy to eject water at a uniform flow rate from a large number of pores, and it is not easy to set the conditions because the position of the ejection holes 8, the hole diameter, etc. have a large effect.
一方、量産効果を増すために被処理基板4は大きさが4
インチ径から5インチ径に、また5インチ径から6イン
チへと大形化し、また反応ガスの流速が増加するに従っ
て、被処理基板4上の均一なCVD成長が困難になり、
被処理基板の中央部が厚< CVD成長が起ると共に未
反応生成物の残留が生じやすく、この改良が要望されて
いた。On the other hand, in order to increase the mass production effect, the size of the substrate 4 to be processed is 4.
As the size increases from an inch diameter to a 5 inch diameter, and from a 5 inch diameter to a 6 inch diameter, and as the flow rate of the reaction gas increases, uniform CVD growth on the substrate 4 to be processed becomes difficult.
When the thickness of the substrate in the center of the substrate is less than that, CVD growth occurs and unreacted products tend to remain, and an improvement has been desired.
以上説明したように被処理基板上にCVD成長装置を用
いて半導体層、絶縁層、導体層などを形成する場合に、
被処理基板の大きさが増し、また反応ガスの供給量を多
くするに従ってCVD成長が不均一になることが問題で
あり、またシャワー内で反応してソースガスの凝縮が起
こりやすいことも問題である。As explained above, when forming a semiconductor layer, an insulating layer, a conductor layer, etc. on a substrate to be processed using a CVD growth apparatus,
The problem is that CVD growth becomes non-uniform as the size of the substrate to be processed increases and the amount of reactant gas supplied increases.Another problem is that the source gas tends to condense due to reactions in the shower. be.
上記の問題は排気系に接続したチャンバ内に反応ガスを
噴出するシャワーと該シャワーに対向し、加熱源を備え
たサセプタとがあり、該サセプタ上に被処理基板を載置
して加熱せしめ、前記反応ガスを熱分解して被処理基板
上に分解生成物を成長せしめる装置において、シャワー
が円筒形状をとり内容積を増すと共に全面に冷却管を備
えて設けられていることを特徴とする化学気相成長装置
により解決することができる。The above problem involves a shower that spouts a reaction gas into a chamber connected to an exhaust system, and a susceptor that faces the shower and is equipped with a heating source, and a substrate to be processed is placed on the susceptor and heated. In the apparatus for thermally decomposing the reaction gas to grow decomposition products on the substrate to be processed, the shower has a cylindrical shape to increase the internal volume and is provided with cooling pipes on the entire surface. This problem can be solved using a vapor phase growth apparatus.
本発明はシャワーの容積を増すことによって反応ガスの
混合を良くすると共に導入管からの流速を緩和し、また
シャワーに冷却管を設けて温度上昇を抑制することによ
りシャワー内反応を無くするものである。The present invention improves mixing of reaction gases by increasing the volume of the shower, moderates the flow velocity from the introduction pipe, and eliminates reactions within the shower by providing a cooling pipe in the shower to suppress temperature rise. be.
すなわち、従来シャワーの下面に設けである噴出孔8か
ら均等な流量で反応ガスを噴出させるため、噴出孔8の
位置と大きさを調整していたが、本発明は第1図に示す
ようにシャワー9の容積を拡大し、これにより導入管7
より供給される反応ガスの流速を緩和し、この流速がそ
のまま噴出孔8に影響するのを防ぐようにしたものであ
る。That is, in order to eject the reaction gas at an even flow rate from the ejection holes 8 provided on the bottom surface of the shower, the position and size of the ejection holes 8 were conventionally adjusted. By expanding the volume of the shower 9, the introduction pipe 7
The flow rate of the reactant gas supplied is moderated to prevent this flow rate from directly affecting the ejection holes 8.
また分解促進ガスのようにソースガスと反応し易いガス
は従来の導入管7とは別にシャワー9の中に供給するこ
とにより、導入管7内で凝縮反応などが起こるのを防ぎ
、またシャワー9に冷却管10を備えて冷却することに
よりシャワー9内での分解を無くするものである。Furthermore, gases that easily react with the source gas, such as decomposition-promoting gases, are supplied into the shower 9 separately from the conventional introduction pipe 7 to prevent condensation reactions from occurring within the introduction pipe 7. By providing a cooling pipe 10 for cooling, decomposition within the shower 9 can be eliminated.
第1図は本発明を実施したCVD装置の構造を示すもの
で、シャワー9の構造を除き、従来と変わらない。FIG. 1 shows the structure of a CVD apparatus embodying the present invention, which is the same as the conventional one except for the structure of the shower 9.
すなわち、本発明に係るシャワー9は周囲に冷却管10
を備えて円筒状に設けてあり、また分解促進ガス配管1
1は導入管7と別個に設け、シャワー9の内部において
ソースガスおよびキャリアガスと混合するよう構成しで
ある。That is, the shower 9 according to the present invention has a cooling pipe 10 around it.
It is provided in a cylindrical shape with a decomposition promoting gas pipe 1.
1 is provided separately from the introduction pipe 7 and configured to mix with the source gas and carrier gas inside the shower 9.
またシャワー9には冷却管10を表面に沿って設けて水
冷し、被処理基板4とサセプタ3からの輻 ゛射熱によ
る温度上昇を抑えている。In addition, a cooling pipe 10 is provided along the surface of the shower 9 for water cooling, thereby suppressing a temperature rise due to radiant heat from the substrate 4 to be processed and the susceptor 3.
このようにして直径6インチのシャワーを用いて直径4
インチのSiウェハからなる被処理基板4の上にA1を
CVD成長させた結果、膜厚の変動は5%以内であり、
また分析の結果も被処理基板の中央部に従来のように未
分解物が認められることもなかった。In this way you can use a 6 inch diameter shower to create a 4 inch diameter shower.
As a result of growing A1 by CVD on the substrate 4 to be processed consisting of an inch-sized Si wafer, the variation in film thickness was within 5%,
Also, the analysis results showed that no undecomposed substances were found in the center of the substrate to be processed, unlike in the conventional case.
以上記したように従来のCVD装置では被処理基板の面
積が増し、また反応ガスの供給量を増すに従って、均一
成長が困難になっていたが、本発明の実施により、均一
化が可能になり、半厚体素子の収率を向上することがで
きる。As mentioned above, with conventional CVD equipment, as the area of the substrate to be processed increases and the amount of reactant gas supplied increases, it becomes difficult to achieve uniform growth, but by implementing the present invention, uniform growth is now possible. , the yield of semi-thick body elements can be improved.
第1図は本発明に係るCVD装置の断面図、第2図は従
来のCVD装置の断面図、
である。
図において、
1はチャンバ、 2.9はシャワー、3はサ
セプタ、 4は被処理基板、5は加熱源、
7は導入管、8は噴出孔、 10は
冷却管、11は分解促進ガス配管、
である。FIG. 1 is a sectional view of a CVD apparatus according to the present invention, and FIG. 2 is a sectional view of a conventional CVD apparatus. In the figure, 1 is a chamber, 2.9 is a shower, 3 is a susceptor, 4 is a substrate to be processed, 5 is a heat source,
7 is an introduction pipe, 8 is an ejection hole, 10 is a cooling pipe, and 11 is a decomposition promoting gas pipe.
Claims (1)
するシャワー(9)と該シャワー(9)に対向して加熱
源(5)を備えたサセプタ(3)とがあり、該サセプタ
(3)上に被処理基板(4)を載置して加熱せしめ、前
記反応ガスを熱分解して被処理基板(4)上に分解生成
物を成長せしめる成長装置において、前記シャワー(9
)に冷却管(10)を設けたことを特徴とする化学気相
成長装置。In the chamber (1) connected to the exhaust system, there is a shower (9) for spouting a reaction gas, and a susceptor (3) equipped with a heating source (5) facing the shower (9). In the growth apparatus, the substrate to be processed (4) is placed on the substrate to be processed (4) and heated, and the reaction gas is thermally decomposed to grow a decomposition product on the substrate to be processed (4).
) is provided with a cooling pipe (10).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9010885A JPS61248519A (en) | 1985-04-26 | 1985-04-26 | Chemical vapor deposition apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9010885A JPS61248519A (en) | 1985-04-26 | 1985-04-26 | Chemical vapor deposition apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61248519A true JPS61248519A (en) | 1986-11-05 |
Family
ID=13989322
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9010885A Pending JPS61248519A (en) | 1985-04-26 | 1985-04-26 | Chemical vapor deposition apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61248519A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63174319A (en) * | 1987-01-14 | 1988-07-18 | Hitachi Ltd | Manufacture of semiconductor device |
JPH0917749A (en) * | 1996-08-02 | 1997-01-17 | Hitachi Ltd | Thin-film formation apparatus |
JP2017092140A (en) * | 2015-11-05 | 2017-05-25 | 株式会社ニューフレアテクノロジー | Shower plate, vapor phase deposition apparatus, and vapor phase deposition method |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6071596A (en) * | 1983-09-27 | 1985-04-23 | Matsushita Electric Ind Co Ltd | Vapor-phase growth apparatus |
-
1985
- 1985-04-26 JP JP9010885A patent/JPS61248519A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6071596A (en) * | 1983-09-27 | 1985-04-23 | Matsushita Electric Ind Co Ltd | Vapor-phase growth apparatus |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63174319A (en) * | 1987-01-14 | 1988-07-18 | Hitachi Ltd | Manufacture of semiconductor device |
JPH0917749A (en) * | 1996-08-02 | 1997-01-17 | Hitachi Ltd | Thin-film formation apparatus |
JP2017092140A (en) * | 2015-11-05 | 2017-05-25 | 株式会社ニューフレアテクノロジー | Shower plate, vapor phase deposition apparatus, and vapor phase deposition method |
US10407772B2 (en) | 2015-11-05 | 2019-09-10 | Nuflare Technology, Inc. | Shower head, vapor phase growth apparatus, and vapor phase growth method |
US10550473B2 (en) | 2015-11-05 | 2020-02-04 | Nuflare Technology, Inc. | Shower head, vapor phase growth apparatus, and vapor phase growth method |
US11047047B2 (en) | 2015-11-05 | 2021-06-29 | Nuflare Technology, Inc. | Shower head, vapor phase growth apparatus, and vapor phase growth method |
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