JPH0441174Y2 - - Google Patents
Info
- Publication number
- JPH0441174Y2 JPH0441174Y2 JP6168987U JP6168987U JPH0441174Y2 JP H0441174 Y2 JPH0441174 Y2 JP H0441174Y2 JP 6168987 U JP6168987 U JP 6168987U JP 6168987 U JP6168987 U JP 6168987U JP H0441174 Y2 JPH0441174 Y2 JP H0441174Y2
- Authority
- JP
- Japan
- Prior art keywords
- reaction tube
- exhaust pipe
- internal reaction
- raw material
- wafers
- 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
- 238000006243 chemical reaction Methods 0.000 claims description 57
- 235000012431 wafers Nutrition 0.000 claims description 20
- 239000002994 raw material Substances 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 8
- 238000000034 method Methods 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000000376 reactant Substances 0.000 description 3
- 229910004298 SiO 2 Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 229910021420 polycrystalline silicon Inorganic materials 0.000 description 2
- 229920005591 polysilicon Polymers 0.000 description 2
- 238000011109 contamination Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Chemical Vapour Deposition (AREA)
Description
【考案の詳細な説明】
〔産業上の利用分野〕
本考案はウエーハの表面にCVD膜を均一に生
成する減圧縦型CVD装置に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a reduced pressure vertical CVD apparatus that uniformly forms a CVD film on the surface of a wafer.
第4図は従来の減圧縦型CVD装置の一例を示
す簡略断面図で、1は発熱体、2はこの発熱体1
の内側に垂設された外部反応管、3はこの外部反
応管2の内側に垂設された内部反応管、7は反応
室キヤツプ部である。9はこの反応室キヤツプ部
7を上下動させるエレベータで、当該キヤツプ部
7を上下動させることによりキヤツプ部7上に載
置したボート10を内部反応管3より出入できる
ようになつている。11はボート10に保持した
多数のウエーハである。12は内部反応管3の下
方より原料ガスを供給する供給管であり、5aは
この供給管12の途中に介挿されたガスコントロ
ールシステムである。4は内、外部反応管3,2
間の下部より排気する排気管であり、6は排気用
の真空ポンプである。
Figure 4 is a simplified cross-sectional view showing an example of a conventional reduced pressure vertical CVD device, where 1 is a heating element, and 2 is this heating element 1.
3 is an internal reaction tube vertically installed inside the external reaction tube 2, and 7 is a reaction chamber cap. Reference numeral 9 denotes an elevator that moves the reaction chamber cap section 7 up and down, and by moving the cap section 7 up and down, the boat 10 placed on the cap section 7 can be taken in and out of the internal reaction tube 3. 11 is a large number of wafers held in the boat 10. 12 is a supply pipe for supplying raw material gas from below the internal reaction tube 3, and 5a is a gas control system inserted in the middle of this supply pipe 12. 4 is inner and outer reaction tubes 3 and 2
It is an exhaust pipe that exhausts air from the lower part between them, and 6 is a vacuum pump for exhaust.
このような従来装置において、エレベータ9に
よりキヤツプ部7を上動させ、キヤツプ部7に載
置したボート10を内部反応管(ホツトウオール
反応室)3内に導入すると、内、外部反応管3,
2の下方においてキヤツプ部7で密閉される。こ
の状態で真空ポンプ6を駆動すると、内部反応管
3内のガスは内、外部反応管3,2間を通り、排
気管4を経て排気され、内部反応管3内は真空状
態になる。 In such a conventional apparatus, when the cap part 7 is moved upward by the elevator 9 and the boat 10 placed on the cap part 7 is introduced into the internal reaction tube (hot wall reaction chamber) 3, the inner and outer reaction tubes 3,
The lower part of the cap 2 is sealed with a cap part 7. When the vacuum pump 6 is driven in this state, the gas in the internal reaction tube 3 passes between the inner and outer reaction tubes 3 and 2, and is exhausted via the exhaust pipe 4, so that the inside of the internal reaction tube 3 becomes in a vacuum state.
そして原料ガスをガスコントロールシステム5
a及び供給管12を経て内部反応管3の下部より
供給すると、原料ガスは矢印で示す経路を通つて
真空ポンプ6により排気される。その過程におい
てボート10に支持された多数のウエーハ11の
表面に気相中で化学反応したCVD膜が生成され
ることになる。 Then, the raw material gas is controlled by the gas control system 5.
When the raw material gas is supplied from the lower part of the internal reaction tube 3 through the supply pipe 12 and the feed pipe 12, the raw material gas is exhausted by the vacuum pump 6 through the path shown by the arrow. In this process, CVD films are produced on the surfaces of a large number of wafers 11 supported by the boat 10 by chemical reaction in the gas phase.
しかしながら上記従来装置にあつては、多量の
ウエーハ11を処理しようとした場合、単純に考
えると、ボート10の高さはもとより発熱体1、
内外部反応管3,2の高さも高くしなければなら
ず、設置室を天井の高い室にしなければならない
し、また高さが高くなると、ボート10の下方位
置(ガス流入側)にあるウエーハの表面に生成さ
れる膜の厚さと上方位置(ガス流出側)にあるウ
エーハの表面に生成される膜の厚さに差が生じ、
多量のウエーハの表面に均一性よくCVD膜を生
成することができなくなるばかりでなく、原料ガ
スが外部反応管2の内面に沿つて流れるので、外
部反応管2の内面に反応物が多量に付着し、フレ
ークが増大し、洗浄頻度が高くなるという問題点
があつた。
However, in the conventional apparatus described above, when trying to process a large number of wafers 11, simply considering the height of the boat 10, the height of the heating element 1,
The height of the inner and outer reaction tubes 3 and 2 must also be increased, and the installation room must be a room with a high ceiling. There is a difference between the thickness of the film formed on the surface of the wafer and the thickness of the film formed on the surface of the wafer located above (the gas outflow side).
Not only will it be impossible to uniformly generate a CVD film on the surface of a large number of wafers, but also a large amount of reactants will adhere to the inner surface of the outer reaction tube 2 because the raw material gas flows along the inner surface of the outer reaction tube 2. However, there were problems in that flakes increased and cleaning frequency increased.
本考案装置は上記の問題点を解決するため、第
1図〜第3図に示すように発熱体1の内側に外部
反応管2を垂設し、この外部反応管2の中心部に
排気管4を垂直に配設し、この排気管4を中心に
して複数個の内部反応管3を垂設せしめ、排気管
4に嵌め込んだ反応室キヤツプ部7上に、各内部
反応管3内に挿入される多数のウエーハ11を支
持した複数個のボート10を載置し、各内部反応
管3の下方より原料ガスを供給すると共に、中心
部の排気管4の下方より排気するように構成した
ものである。
In order to solve the above-mentioned problems, the device of the present invention has an external reaction tube 2 vertically installed inside a heating element 1 as shown in FIGS. A plurality of internal reaction tubes 3 are arranged vertically around the exhaust pipe 4, and a plurality of internal reaction tubes 3 are placed vertically on the reaction chamber cap part 7 fitted into the exhaust pipe 4. A plurality of boats 10 supporting a large number of wafers 11 to be inserted were placed thereon, and raw material gas was supplied from below each internal reaction tube 3, and exhaust was exhausted from below an exhaust pipe 4 in the center. It is something.
原料ガスは複数個の内部反応管3の下方より供
給され、各内部反応管3内に挿入されたボート1
0を経て中心部の排気管4の上端より下方へ流
れ、排気管4の下方より排気される。その過程に
おいて複数個のボート10に支持された多数のウ
エーハ11の表面に気相中で化学反応したCVD
膜が生成される。
Raw material gas is supplied from below a plurality of internal reaction tubes 3, and a boat 1 inserted into each internal reaction tube 3
0, flows downward from the upper end of the exhaust pipe 4 in the center, and is exhausted from the lower part of the exhaust pipe 4. During this process, CVD chemically reacted in the gas phase on the surfaces of a large number of wafers 11 supported by a plurality of boats 10.
A film is produced.
以下図面に基づいて本考案の実施例を説明す
る。
Embodiments of the present invention will be described below based on the drawings.
第1図は本考案装置の一実施例を示す簡略断面
図、第2図は第1図の−線断面図、第3図は
本考案における反応管キヤツプ部に複数個のボー
トを載置した状態を示す簡略斜視図である。 Fig. 1 is a simplified cross-sectional view showing one embodiment of the device of the present invention, Fig. 2 is a cross-sectional view taken along the - line in Fig. 1, and Fig. 3 is a diagram showing a plurality of boats mounted on the reaction tube cap of the present invention. It is a simplified perspective view showing a state.
第1図において1は発熱体、2はこの発熱体1
の内側に垂設された外部反応管、4はこの外部反
応管2の中心部に垂直に配設された排気管であ
る。この排気管4は金属製である場合、不純物汚
染をウエーハに引き起こすので、これを回避する
ため石英製円筒管8でカバーされている。排気管
4は真空ポンプ(図示せず)に連結されている。 In Figure 1, 1 is a heating element, 2 is this heating element 1
An external reaction tube 4 is vertically installed inside the external reaction tube 2, and 4 is an exhaust pipe installed vertically at the center of the external reaction tube 2. If this exhaust pipe 4 is made of metal, it will cause impurity contamination on the wafer, so to avoid this, it is covered with a cylindrical pipe 8 made of quartz. The exhaust pipe 4 is connected to a vacuum pump (not shown).
複数個のこの例では3個の内部反応管(第2図
参照)が排気管4を中心にして垂設されている。
排気管4に嵌め込んだ反応室キヤツプ部7上に
は、第3図示のように各内部反応管3内に挿入さ
れる多数のウエーハ11を支持した3個のボート
10が載置されている。反応室キヤツプ部7はエ
レベータ9により上下動される。 In this example, a plurality of internal reaction tubes, three in number (see FIG. 2), are installed vertically around the exhaust pipe 4.
As shown in the third diagram, three boats 10 supporting a large number of wafers 11 to be inserted into each internal reaction tube 3 are placed on the reaction chamber cap part 7 fitted into the exhaust pipe 4. . The reaction chamber cap 7 is moved up and down by an elevator 9.
各内部反応管3の下部は供給管12に接続さ
れ、原料ガスはガスコントロールシステム5によ
り各内部反応管3内に均一に供給されるようにな
つている。 The lower part of each internal reaction tube 3 is connected to a supply pipe 12, and the raw material gas is uniformly supplied into each internal reaction tube 3 by a gas control system 5.
上記の構成において、エレベータ9により反応
室キヤツプ部7を上動させ、キヤツプ部7に載置
した3個のボート10を各内部反応管3内に導入
すると、各内、外部反応管3,2の下方において
キヤツプ部7で密閉される。この状態で真空ポン
プ(図示せず)を駆動すると内、外部反応管3,
2間のガスは、排気管4の上方より下方へ向かつ
て排気され、内、外部反応管3,2内は真空状態
になる。 In the above configuration, when the reaction chamber cap part 7 is moved upward by the elevator 9 and the three boats 10 placed on the cap part 7 are introduced into each internal reaction tube 3, each of the inner and outer reaction tubes 3, 2 It is sealed with a cap part 7 below. When the vacuum pump (not shown) is operated in this state, the inner and outer reaction tubes 3,
The gas between the reaction tubes 2 and 2 is exhausted from the upper side of the exhaust pipe 4 to the lower side, and the insides of the inner and outer reaction tubes 3 and 2 are brought into a vacuum state.
原料ガスを本管13に導入すると、原料ガスは
ガスコントロールシステム5により各内部反応管
3内に供給管12を経て均一に供給され、この供
給された原料ガスは矢印で示すように多数のウエ
ーハ11を支持した3個のボート10と各内部反
応管3の内周との間を経由し、中心部の排気管4
の上方より下方に向かつて排気される。 When the raw material gas is introduced into the main pipe 13, the raw material gas is uniformly supplied into each internal reaction tube 3 through the supply pipe 12 by the gas control system 5, and this supplied raw material gas is supplied to a large number of wafers as shown by the arrows. 11 and the inner periphery of each internal reaction tube 3.
Air is exhausted from above to below.
この排気過程において3個のボート10に支持
された多数のウエーハ11の表面に気相中で化学
反応したCVD膜が生成される。このCVD膜、特
に、SiO2,PSG、ドープトポリシリコンの膜の
厚さの均一性は内部反応管3とウエーハ11間の
ギヤツプに左右されるが、当該ギヤツプを適切に
することによりSiO2,PSG、ドープトポリシリ
コン等のCVD膜においても均一な膜厚のものが
生成できる。 During this evacuation process, CVD films are produced on the surfaces of a large number of wafers 11 supported by three boats 10 by chemical reaction in the gas phase. The uniformity of the thickness of this CVD film, particularly of SiO 2 , PSG, and doped polysilicon films, depends on the gap between the internal reaction tube 3 and the wafer 11, but by making the gap appropriate, SiO 2 , PSG, doped polysilicon, etc. can also be produced with uniform thickness.
また、本考案においては、横方向に大きくなる
が、縦方向には大きくならない(高くならない)
ので、設置室を天井の高い室にする必要はない
し、かつ各ボート10の下方位置(ガス流入側)
にあるウエーハの表面に生成される膜の厚さと上
方位置(ガス流出側)にあるウエーハの表面に生
成される膜の厚さに差が生じることはなく、多量
のウエーハの表面には均一性よくCVD膜を生成
することができる。 In addition, in this invention, although it becomes larger in the horizontal direction, it does not become larger (does not become taller) in the vertical direction.
Therefore, there is no need for the installation room to be a room with a high ceiling, and it is located below each boat 10 (gas inflow side).
There is no difference in the thickness of the film formed on the surface of the wafer located at the upper position (gas outflow side) and the thickness of the film formed on the surface of the wafer located at the upper position (gas outlet side), and there is no uniformity on the surface of a large number of wafers. Can produce CVD films well.
更に原料ガスが各内部反応管3の内面に沿つて
流れ、中心部の排気管4より排気されるので、外
部反応管2の内面に付着する反応物を低減し、フ
レークを少なく、洗浄頻度を低減することができ
る。 Furthermore, since the raw material gas flows along the inner surface of each internal reaction tube 3 and is exhausted from the central exhaust pipe 4, the amount of reactants adhering to the inner surface of the outer reaction tube 2 is reduced, flakes are reduced, and cleaning frequency is reduced. can be reduced.
即ち、本考案によれば、多量のウエーハ11の
表面に均一性よくCVD膜を生成することができ
るばかりでなく、外部反応管の内面に付着する反
応物を低減でき、フレークを少なく、洗浄頻度を
低減することができる。
That is, according to the present invention, not only can a CVD film be formed with good uniformity on the surface of a large number of wafers 11, but also the amount of reactants adhering to the inner surface of the external reaction tube can be reduced, flakes can be reduced, and cleaning frequency can be reduced. can be reduced.
第1図は本考案装置の一実施例を示す簡略断面
図、第2図は第1図の−線断面図、第3図は
本考案における反応管キヤツプ部に複数個のボー
トを載置した状態を示す簡略斜視図、第4図は従
来の減圧縦型CVD装置の一例を示す簡略断面図
である。
1……発熱体、2……外部反応管、3……内部
反応管、4……排気管、7……反応室キヤツプ
部、10……ボート、11……ウエーハ。
Fig. 1 is a simplified cross-sectional view showing one embodiment of the device of the present invention, Fig. 2 is a cross-sectional view taken along the - line in Fig. 1, and Fig. 3 is a diagram showing a plurality of boats mounted on the reaction tube cap of the present invention. FIG. 4 is a simplified perspective view showing the state, and FIG. 4 is a simplified sectional view showing an example of a conventional reduced pressure vertical CVD apparatus. DESCRIPTION OF SYMBOLS 1... Heating element, 2... External reaction tube, 3... Internal reaction tube, 4... Exhaust pipe, 7... Reaction chamber cap part, 10... Boat, 11... Wafer.
Claims (1)
外部反応管2の中心部に排気管4を垂直に配設
し、この排気管4を中心にして複数個の内部反応
管3を垂設せしめ、排気管4に嵌め込んだ反応室
キヤツプ部7上に、各内部反応管3内に挿入され
る多数のウエーハ11を支持した複数個のボート
10を載置し、各内部反応管3の下方より原料ガ
スを供給すると共に、中心部の排気管4の下方よ
り排気するように構成した減圧縦型CVD装置。 An external reaction tube 2 is installed vertically inside the heating element 1, an exhaust pipe 4 is installed vertically in the center of the external reaction tube 2, and a plurality of internal reaction tubes 3 are arranged around the exhaust pipe 4. A plurality of boats 10 supporting a large number of wafers 11 to be inserted into each internal reaction tube 3 are placed on the reaction chamber cap part 7 which is vertically installed and fitted into the exhaust pipe 4. A reduced-pressure vertical CVD device configured to supply raw material gas from below 3 and exhaust from below an exhaust pipe 4 in the center.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6168987U JPH0441174Y2 (en) | 1987-04-22 | 1987-04-22 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6168987U JPH0441174Y2 (en) | 1987-04-22 | 1987-04-22 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63170465U JPS63170465U (en) | 1988-11-07 |
| JPH0441174Y2 true JPH0441174Y2 (en) | 1992-09-28 |
Family
ID=30895263
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6168987U Expired JPH0441174Y2 (en) | 1987-04-22 | 1987-04-22 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0441174Y2 (en) |
-
1987
- 1987-04-22 JP JP6168987U patent/JPH0441174Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63170465U (en) | 1988-11-07 |
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