JPH03106018A - Pressure-reduced chemical vapor growth device - Google Patents
Pressure-reduced chemical vapor growth deviceInfo
- Publication number
- JPH03106018A JPH03106018A JP24553089A JP24553089A JPH03106018A JP H03106018 A JPH03106018 A JP H03106018A JP 24553089 A JP24553089 A JP 24553089A JP 24553089 A JP24553089 A JP 24553089A JP H03106018 A JPH03106018 A JP H03106018A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- inert gas
- wafer
- wafers
- air
- 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.)
- Granted
Links
- 239000000126 substance Substances 0.000 title description 3
- 239000011261 inert gas Substances 0.000 claims abstract description 39
- 235000012431 wafers Nutrition 0.000 claims abstract description 33
- 230000007246 mechanism Effects 0.000 claims abstract description 5
- 238000005229 chemical vapour deposition Methods 0.000 claims description 6
- 238000007664 blowing Methods 0.000 claims description 5
- 239000004065 semiconductor Substances 0.000 claims description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 7
- 239000001301 oxygen Substances 0.000 abstract description 7
- 229910052760 oxygen Inorganic materials 0.000 abstract description 7
- 238000006467 substitution reaction Methods 0.000 abstract 2
- 238000000034 method Methods 0.000 abstract 1
- 230000035515 penetration Effects 0.000 abstract 1
- 239000012495 reaction gas Substances 0.000 description 6
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910021420 polycrystalline silicon Inorganic materials 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 239000012808 vapor phase Substances 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010573 double replacement reaction Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000004518 low pressure chemical vapour deposition Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、減圧化学気相成長装置、特に昇温状態且つ炉
内を大気開放状態にてウェノ1−を入炉し、その後炉内
を減圧して或膜を行う減圧化学気相戒長装置に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a reduced-pressure chemical vapor deposition apparatus, in particular, to a reduced pressure chemical vapor deposition apparatus, in which a weno 1 is placed in the furnace at a raised temperature and the inside of the furnace is opened to the atmosphere, and then the inside of the furnace is opened to the atmosphere. This invention relates to a reduced pressure chemical vapor phase control device that performs a certain membrane treatment under reduced pressure.
第2図に従来の減圧化学気相成長装置の断面図を示す。 FIG. 2 shows a cross-sectional view of a conventional reduced pressure chemical vapor deposition apparatus.
同図において、炉芯管1内にキャップ3を付犀したウェ
ハー装填治具5に、被加工の多数の半導体ウェハー6を
セットし、炉口部から入炉し、炉口をキャップ3で密閉
し、キャップ3に設けてある反応ガス導入管4から反応
ガスを導入し、ウェハー6の表面に前記反応ガスの化学
反応により所望の被膜を戊長させる。また、ウェハ一人
炉時には、炉口の反対側の炉後端側に設けている不活性
ガス導入管のバルブ8を開いて、炉後端側から炉口側へ
の不活性ガスの流れをつくって炉内への大気の浸入を防
止している。なお、図において、2は炉内を高温にする
ための加熱ヒータ、7は炉内圧力制御用バルブ、10は
排気部である。In the figure, a large number of semiconductor wafers 6 to be processed are set in a wafer loading jig 5 with a cap 3 attached to the furnace core tube 1, and the furnace is loaded from the furnace mouth, and the furnace mouth is sealed with the cap 3. Then, a reaction gas is introduced from a reaction gas introduction pipe 4 provided in the cap 3, and a desired film is elongated on the surface of the wafer 6 by a chemical reaction of the reaction gas. In addition, when using a single wafer furnace, open the valve 8 of the inert gas introduction pipe installed at the rear end of the furnace opposite to the furnace mouth to create a flow of inert gas from the rear end of the furnace to the furnace mouth. This prevents air from entering the furnace. In the figure, 2 is a heater for raising the temperature inside the furnace, 7 is a valve for controlling the pressure inside the furnace, and 10 is an exhaust part.
上述した従来の減圧化学気相成長装置では、入炉が或膜
時に近い高温状態で行われ、且つ大気開放状態で行われ
る為、大気中の酸素が炉内に侵入し、ウェハー表面が入
炉時に徐々に酸化される。In the conventional low-pressure chemical vapor deposition apparatus described above, charging is performed at a high temperature close to that of a certain film temperature and in an open atmosphere, so oxygen from the atmosphere enters the furnace and the wafer surface is heated. sometimes gradually oxidized.
そこで、この酸化を防ぐために、炉芯管密閉用のキャッ
プ3を脱去し開口すると同時に、不活性ガス導入用バル
ブ8を開けて、炉後端側から不活性ガスを導入している
が、炉口の開口面積が非常に大きいため、大気の侵入を
十分には防ぎ切れなかった。また入炉の際ウェハー面は
炉芯管軸方向に対し、垂直またはほぼ垂直に近い状態に
あり、炉後端側から導入する不活性ガスの流れ方向をさ
えぎる状態となり、炉内壁付近はある程度不活性ガスに
て置換されるが、各ウェハー間については大気が停留し
たままの状態で炉内に持込まれ、やはりウェハー表面が
酸化されてしまうという欠点がある。Therefore, in order to prevent this oxidation, the cap 3 for sealing the furnace core tube is removed and opened, and at the same time, the inert gas introduction valve 8 is opened to introduce inert gas from the rear end of the furnace. Because the opening area of the furnace mouth was extremely large, it was not possible to sufficiently prevent air from entering. In addition, when entering the furnace, the wafer surface is perpendicular or nearly perpendicular to the axis of the furnace core tube, blocking the flow direction of the inert gas introduced from the rear end of the furnace, and the area near the furnace inner wall is somewhat unstable. Although the atmosphere is replaced with an active gas, there is a drawback that the air remains between each wafer and is brought into the furnace, resulting in oxidation of the wafer surface.
本発明の減圧化学気相成長装置は、炉芯管開口部付近に
不活性ガス吹き出し部と排気部を不活性ガスの流れが各
ウェハー面とほぼ平行となるように対に設けて、炉口直
前にて各ウェハー間の停留大気を不活性ガスにて置換す
るようにしてい.る。In the reduced pressure chemical vapor deposition apparatus of the present invention, an inert gas blowout part and an exhaust part are provided in pairs near the opening of the furnace core tube so that the flow of the inert gas is approximately parallel to each wafer surface. Immediately before this, the stagnant atmosphere between each wafer is replaced with inert gas. Ru.
更に、このようにしても不活性ガス吹き出しの際に同時
に大気を巻き込み、各ウェハー間に微量の大気が停留し
てしまうので、炉内の炉口付近においても不活性ガスの
吹き出し部と排気部を設けた二重の不活性ガス置換構造
としている。そのため、従来見逃されていた各ウェハー
間に停留する酸素も完全に不活性ガスで置換される。Furthermore, even if you do this, air will be drawn in at the same time when the inert gas is blown out, and a small amount of air will remain between each wafer. It has a double inert gas replacement structure with a Therefore, the oxygen remaining between each wafer, which was overlooked in the past, is also completely replaced with inert gas.
次に、本発明について図面を参照して説明する。 Next, the present invention will be explained with reference to the drawings.
第1図は本発明の一実施例の断面図である。第1図にお
いて、炉芯管1は、ヒータ2により加熱され、ウェハー
6の入炉時は、キャップ3がウェハー装填治具5と共に
上方に移動し、炉芯管開口端を密閉する。モして膜成長
時には反応ガス導入部4から反応ガスを導入し、炉内圧
力は、炉内圧力制御用バルブ7により調整する。ここで
ウェハ一人炉(上昇)時には、炉内圧力制御用バルブ7
は閉じており、炉内への大気侵入を防ぐための不活性ガ
ス導入用バルブ8が開き不活性ガスが矢印に沿って炉内
を開口端に向かって流れていく。FIG. 1 is a sectional view of an embodiment of the present invention. In FIG. 1, a furnace core tube 1 is heated by a heater 2, and when a wafer 6 is placed in the furnace, a cap 3 moves upward together with a wafer loading jig 5 to seal the open end of the furnace core tube. During film growth, a reaction gas is introduced from the reaction gas inlet 4, and the furnace pressure is adjusted by the furnace pressure control valve 7. Here, when one wafer is in the furnace (ascending), the furnace pressure control valve 7
is closed, and an inert gas introduction valve 8 for preventing atmospheric air from entering the furnace opens, and the inert gas flows inside the furnace toward the open end along the arrow.
また同時に、炉外不活性ガス吹き出し部9から不活性ガ
スを入炉中のウェハーに向けて吹き出し、その延長線上
に設置された炉外排気部10から排気し、炉口付近の大
気を若干巻き込みながらも各ウェハー間の大気を不活性
ガスにある程度置換する。さらに炉内不活性ガス吹き出
し部11から同様に不活性ガスを吹き出し、その延長線
上に設置された炉内排気部12で排気して各ウェハー間
に僅かに停留した大気を不活性ガスにより置換する二重
の置換機構を設けている。At the same time, inert gas is blown out from the outside inert gas blowing section 9 toward the wafers being placed in the furnace, and is exhausted from the outside exhaust section 10 installed on the extension line of the inert gas, which slightly entrains the atmosphere near the furnace mouth. However, the atmosphere between each wafer is replaced to some extent with an inert gas. Furthermore, inert gas is blown out in the same way from the inert gas blowing section 11 in the furnace, and the inert gas is evacuated at the in-furnace exhaust section 12 installed on the extension line of the inert gas, and the atmosphere slightly stagnant between each wafer is replaced with the inert gas. A double replacement mechanism is provided.
以上説明したように本発明は、炉後端側から不活性ガス
を導入し、炉口直前部分と炉内の炉口付近とに二重に不
活性ガス置換機構を有することにより、ウェハ一人炉時
の炉内への酸素持ち込み量を大幅に抑えることが可能と
なり、更に各ウェハー間の停留大気(特に酸素)も同様
に抑えられるため、入炉時のウェハー表面の酸化が十分
抑えられるという効果がある。従って、例えばシリコン
ウェハー上に多結晶シリコンを戒長させて、両者の導通
をとる場合、入炉時の酸素の侵入により二酸化ケイ素が
シリコンウェハー表面と多結晶シリコンの間に形成され
、その間の導通を妨げてしまうという問題が解決できる
。As explained above, the present invention introduces an inert gas from the rear end of the furnace and has a dual inert gas exchange mechanism in the area just before the furnace mouth and in the vicinity of the furnace mouth. It is possible to significantly reduce the amount of oxygen brought into the furnace at the time of processing, and the amount of air (especially oxygen) stagnant between each wafer is also suppressed, which has the effect of sufficiently suppressing oxidation of the wafer surface when entering the furnace. There is. Therefore, for example, when polycrystalline silicon is placed on a silicon wafer to establish electrical conduction between the two, silicon dioxide is formed between the silicon wafer surface and polycrystalline silicon due to the intrusion of oxygen during the furnace, and the electrical conduction between the two is established. This can solve the problem of preventing
第1図は本発明の一実施例の断面図、第2図は従来の減
圧化学気相戊長装置の断面図である。
1・・・・・・炉芯管、2・・・・・・ヒータ、3・・
・・・・キャップ、4・・・・・・反応ガス導入部、5
・・・・・・ウェハー装填治具、6・・・・・・ウェハ
ー 7・・・・・・炉内圧カ制御用バルブ、8・・・・
・・不活性ガス導入用バルブ、9・・・・・・炉外不活
性ガス吹き出し部、1o・・・・・・炉外排気部、11
・・・・・・炉内不活性ガス吹き出し部、12・・・・
・・炉内排気部。FIG. 1 is a sectional view of an embodiment of the present invention, and FIG. 2 is a sectional view of a conventional reduced pressure chemical vapor phase elongation apparatus. 1... Furnace core tube, 2... Heater, 3...
... Cap, 4 ... Reaction gas introduction part, 5
...Wafer loading jig, 6...Wafer 7...Furnace pressure control valve, 8...
... Valve for inert gas introduction, 9 ... Inert gas blowing part outside the furnace, 1o ... Exhaust part outside the furnace, 11
...Furnace inert gas blowing section, 12...
...Furnace exhaust section.
Claims (1)
具にセットされて前記炉芯管に入炉される多数の半導体
ウェハー間の停留大気を不活性ガスにて置換するための
2重の不活性ガス吹出し、排気機構が前記炉芯管炉口近
傍に設けられていることを特徴とする減圧化学気相成長
装置。In a reduced pressure chemical vapor deposition apparatus using a furnace core tube, a double layer is used to replace the stagnant atmosphere between a large number of semiconductor wafers set in a loading jig and entered into the furnace core tube with inert gas. A reduced pressure chemical vapor deposition apparatus, characterized in that an inert gas blowing and exhaust mechanism is provided near the furnace mouth of the furnace core tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24553089A JPH0821551B2 (en) | 1989-09-20 | 1989-09-20 | Low pressure chemical vapor deposition equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24553089A JPH0821551B2 (en) | 1989-09-20 | 1989-09-20 | Low pressure chemical vapor deposition equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03106018A true JPH03106018A (en) | 1991-05-02 |
| JPH0821551B2 JPH0821551B2 (en) | 1996-03-04 |
Family
ID=17135063
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24553089A Expired - Lifetime JPH0821551B2 (en) | 1989-09-20 | 1989-09-20 | Low pressure chemical vapor deposition equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0821551B2 (en) |
-
1989
- 1989-09-20 JP JP24553089A patent/JPH0821551B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0821551B2 (en) | 1996-03-04 |
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