JPS5823926B2 - heat treatment equipment - Google Patents
heat treatment equipmentInfo
- Publication number
- JPS5823926B2 JPS5823926B2 JP52136084A JP13608477A JPS5823926B2 JP S5823926 B2 JPS5823926 B2 JP S5823926B2 JP 52136084 A JP52136084 A JP 52136084A JP 13608477 A JP13608477 A JP 13608477A JP S5823926 B2 JPS5823926 B2 JP S5823926B2
- Authority
- JP
- Japan
- Prior art keywords
- tube
- furnace
- heat treatment
- outside air
- pipe
- 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
Description
【発明の詳細な説明】
この発明は熱処理装置、特に開管形拡散炉などの熱処理
装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat treatment apparatus, particularly to a heat treatment apparatus such as an open tube diffusion furnace.
半導体装置などの製造に使用する開管形拡散炉の従来例
を第1図に示しである。FIG. 1 shows a conventional example of an open tube diffusion furnace used for manufacturing semiconductor devices and the like.
この第1図において、1は石英ガラス管などからなるプ
ロセス管2はこのプロセス管1の外周囲に配設された磁
性管などによる均熱管、3はこの均熱管2の外周囲に同
様に配設された高周波コイルなどによるヒータであり、
熱処理に際して使用されるガスは、プロセス管1の一端
側インジエクタ11から管内に導入され、他端側管口部
12より排気されるようになっている。In FIG. 1, 1 is a process tube 2 made of a quartz glass tube or the like, and 3 is a soaking tube made of a magnetic tube or the like placed around the outside of the process tube 1. It is a heater using a high frequency coil etc.
Gas used in the heat treatment is introduced into the process tube 1 from an injector 11 at one end thereof, and is exhausted from a tube port 12 at the other end.
しかしてこのような拡散炉においては、管口部12の断
面積が大きい程、符号4で示した外気の廻り込み部分が
、内部に入り込むことになる。However, in such a diffusion furnace, the larger the cross-sectional area of the pipe opening 12, the more the outside air enters into the interior, as indicated by the reference numeral 4.
そしてこの外気の廻り込みによって、例えばシリコンウ
ェハを水蒸気雰囲気で酸化する場合には、シリコンウェ
ハの炉内位置、ウェハ上の位置により、酸化膜厚が大き
く異なるなどの悪影響を生ずる。When a silicon wafer is oxidized in a steam atmosphere, for example, this circulation of outside air causes an adverse effect such as a large difference in oxide film thickness depending on the position of the silicon wafer in the furnace and the position on the wafer.
こ\で前記第1図A−A部の炉断面内でのガスの動きは
、第2図に矢印で示したとおりであり、このようなガス
の流れは、高温の均熱部を経て加熱されたガスが低温領
域に入ると、管壁に近い部分で冷却され、このために管
壁に沿う下降流が生ずるものと考えられ、この作用に伴
って前記した外気が管内低部側により一層入り込み易く
なるのである。The movement of gas within the furnace cross section in section A-A in Figure 1 is as shown by the arrow in Figure 2, and this flow of gas passes through the high-temperature soaking section and is heated. When the gas enters the low-temperature region, it is thought to be cooled near the pipe wall, causing a downward flow along the pipe wall, and as a result of this action, the above-mentioned outside air flows further toward the lower part of the pipe. It makes it easier to get into it.
そしてこのような管口部から管内への外気の廻り込みを
阻止するために従来は、実効的に管口部の開口面積を小
さくするエンドキャップを用いたす、外気遮蔽のための
バッフル板を用いる方法が、第3図に示したように採用
されている。In order to prevent outside air from entering the pipe from the pipe opening, conventional methods have used end caps that effectively reduce the opening area of the pipe opening, and baffle plates for shielding outside air. A method is adopted as shown in FIG.
すなわち、この第3図において、5は管口部12を閉じ
るエンドキャップ、6は管内に挿入されるバッフル板、
7は被処理物の搬入、搬出を行なうボート、8はこのボ
ート7の引出し棒である。That is, in this FIG. 3, 5 is an end cap that closes the pipe opening 12, 6 is a baffle plate inserted into the pipe,
Reference numeral 7 designates a boat for loading and unloading objects to be treated, and 8 designates a pull-out rod of this boat 7.
しかし乍らエンドキャップ5を用いる場合は、プロセス
管1の管口部12に対して充分な密着を再現性よく得る
ことができず、またバッフル板6を用いる場合は、プロ
セス管1の内径にバッフル板6の直径を一杯に合わせ、
特に管内底部側とバッフル板下部側との間隙を小さくす
る必要があるが、大口径のプロセス管はど熱処理中に自
重による変形を受は易いことから、実際上この間隙を小
さくできず、外気の廻り込みを防ぎ得ないものであった
。However, when using the end cap 5, it is not possible to obtain sufficient adhesion to the pipe opening 12 of the process tube 1 with good reproducibility, and when using the baffle plate 6, the inner diameter of the process tube 1 Adjust the diameter of the baffle plate 6 to its full extent,
In particular, it is necessary to reduce the gap between the inner bottom side of the tube and the lower side of the baffle plate, but since large-diameter process tubes are easily deformed by their own weight during heat treatment, this gap cannot be reduced in practice, and outside air It was impossible to prevent this from happening.
この発明は前記した従来の開管形炉での対流作用に伴な
って、管口部炉内に生ずる外気引き込み作用を阻止する
ため、前記対流作用を妨げる案内部材を管口部炉内に設
けたものである。In order to prevent the outside air drawing action that occurs in the pipe mouth furnace due to the convection action in the conventional open tube furnace described above, the present invention provides a guide member in the pipe mouth furnace that prevents the convection action. It is something that
以下この発明を開管形拡散炉に適用した実施例につき、
第4図ないし第6図を参照して詳細に説明する。The following is an example of applying this invention to an open tube diffusion furnace.
This will be explained in detail with reference to FIGS. 4 to 6.
第4図および第5図は一実施例を示しており、これら各
図において前記第1図ないし第3図と同一符号は同一ま
たは相当部分を示している。4 and 5 show one embodiment, and in each of these figures, the same reference numerals as in FIGS. 1 to 3 indicate the same or corresponding parts.
この実施例による開管形拡散炉では、プロセス管1の管
口部12炉内に、所定長さに亘って石英ガラス板などの
案内板10aを、炉長方向に向は層状に挿入させてなる
案内部材10を設けたものである。In the open-tube diffusion furnace according to this embodiment, a guide plate 10a such as a quartz glass plate is inserted into the tube opening 12 of the process tube 1 over a predetermined length in a layered manner in the furnace length direction. A guide member 10 is provided.
従ってこのように案内部材10を設けであるため、管口
部12での前記第2図に示した対流が妨げられること5
なり、上昇流によって生じていた圧力差が小さくなるこ
とから、外気の廻り込みが抑制されるものであり、また
この案内部材10をボート7の直後にまで延長させるこ
とで、このボート7を引出す工程でも外気の廻り込みを
少なくし得られ、前記エンドキャップ5およびバッフル
板6に優る作用効果を得ることができるのである。Therefore, since the guide member 10 is provided in this way, the convection shown in FIG. 2 at the pipe opening 12 is hindered.
This reduces the pressure difference caused by the upward flow, which suppresses the intrusion of outside air.Furthermore, by extending the guide member 10 to just behind the boat 7, the boat 7 can be pulled out. It is possible to reduce the circulation of outside air during the process, and it is possible to obtain functions and effects superior to those of the end cap 5 and the baffle plate 6.
また第6図はこの発明の他の実施例を示しており、この
第6図からも明らかなように、前記案内部材10として
は、同様な材質による案内管10bの複数本を、炉長方
向に向は重積するように挿入させでもよく、同様な作用
効果を得られるのである。FIG. 6 shows another embodiment of the present invention, and as is clear from FIG. 6, the guide member 10 includes a plurality of guide tubes 10b made of the same material in the furnace length direction. The same effect can be obtained by inserting them in a stacked manner.
以上詳述したようにこの発明によるときは、管口部炉内
に対流作用を妨げるための案内部材を設けるだけの極め
て簡単な手段により、管口部に生じていた外気の廻り込
みを充分に阻止することができるものであり、従来のよ
うにエンドギヤラスバッフル板にみられるような欠点を
改善できるほか、この発明での案内部材をボートローダ
と併用させることにより完全自動化システムを導入し得
て、■バッチ当りの処理量を増加でき、均一な拡散、酸
化処理などを容易に実行できるなどの特長を有するもの
である。As described in detail above, according to the present invention, the circulation of outside air occurring at the pipe mouth can be sufficiently prevented by simply providing a guide member for preventing convection in the pipe mouth furnace. In addition to improving the defects seen in conventional end gear lath baffle plates, a fully automated system can be introduced by using the guide member of this invention in combination with a boat loader. (2) The amount of processing per batch can be increased, and uniform diffusion, oxidation treatment, etc. can be easily performed.
第1図は通常の開管形拡散炉の構成を示す概要図、第2
図は同上A−A′線部でのガスの流れを示す説明図、第
3図は外気の廻り込みを抑制するための従来の手段を適
用した開管形拡散炉の構成を示す概要図、第4図はこの
発明を開管形拡散炉に適用した場合の一実施例による構
成を示す概要図、第5図は同上要部の斜視図、第6図は
同上能の実施例を示す斜視図である。
1・・・・・・プロセス管、2・・・・・・均熱管、3
・・・・・・ヒータ、7・・・・・・ボート、8・・・
・・・引出し棒、10・・・・・・案内部材、10a・
・・・・・案内板、10b・・・・・・案内管。Figure 1 is a schematic diagram showing the configuration of a normal open-tube diffusion furnace;
The figure is an explanatory diagram showing the gas flow along line A-A' as above, and Figure 3 is a schematic diagram showing the configuration of an open-tube diffusion furnace to which conventional means for suppressing the circulation of outside air is applied. Fig. 4 is a schematic diagram showing the configuration of an embodiment of the invention when applied to an open-tube diffusion furnace, Fig. 5 is a perspective view of the main parts of the same, and Fig. 6 is a perspective view showing an embodiment of the same. It is a diagram. 1... Process tube, 2... Soaking tube, 3
... Heater, 7 ... Boat, 8 ...
... Pull-out rod, 10 ... Guide member, 10a.
...Guidance board, 10b...Guidance tube.
Claims (1)
前口部炉内の対流作用を妨げる複数の案内部材を炉長方
向に向は層状に設けたことを特徴とする熱処理装置。1. A heat treatment apparatus in an open-tube furnace, characterized in that a plurality of guide members are provided in the tube opening opening to the outside in a layered manner in the furnace length direction to prevent convection in the front opening of the furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52136084A JPS5823926B2 (en) | 1977-11-11 | 1977-11-11 | heat treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52136084A JPS5823926B2 (en) | 1977-11-11 | 1977-11-11 | heat treatment equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5469061A JPS5469061A (en) | 1979-06-02 |
| JPS5823926B2 true JPS5823926B2 (en) | 1983-05-18 |
Family
ID=15166866
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP52136084A Expired JPS5823926B2 (en) | 1977-11-11 | 1977-11-11 | heat treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5823926B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5422870B2 (en) * | 1974-03-12 | 1979-08-09 |
-
1977
- 1977-11-11 JP JP52136084A patent/JPS5823926B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5469061A (en) | 1979-06-02 |
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