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JP3406040B2 - Processing device and processing method - Google Patents
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JP3406040B2 - Processing device and processing method - Google Patents

Processing device and processing method

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Publication number
JP3406040B2
JP3406040B2 JP34786693A JP34786693A JP3406040B2 JP 3406040 B2 JP3406040 B2 JP 3406040B2 JP 34786693 A JP34786693 A JP 34786693A JP 34786693 A JP34786693 A JP 34786693A JP 3406040 B2 JP3406040 B2 JP 3406040B2
Authority
JP
Japan
Prior art keywords
adjusting mechanism
pressure adjusting
exhaust
waste liquid
processing
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 - Fee Related
Application number
JP34786693A
Other languages
Japanese (ja)
Other versions
JPH07183242A (en
Inventor
俊二 川上
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tokyo Electron Ltd
Original Assignee
Tokyo Electron Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tokyo Electron Ltd filed Critical Tokyo Electron Ltd
Priority to JP34786693A priority Critical patent/JP3406040B2/en
Publication of JPH07183242A publication Critical patent/JPH07183242A/en
Application granted granted Critical
Publication of JP3406040B2 publication Critical patent/JP3406040B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は熱処理装置の排気処理装
置及び排気処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust treatment apparatus and an exhaust treatment method for a heat treatment apparatus.

【0002】[0002]

【従来の技術】従来、一般に半導体ウェハ等の熱処理プ
ロセスラインは、プロセスチューブを備えた熱処理炉を
多数設置し、これらの炉の排気系ダクトを共通にして工
場の排気ダクトに接続して製造ラインを構成している。
熱処理装置のプロセス排気能力は装置設置場所である工
場の排気能力に左右され、複数枚の半導体ウェハを均一
に熱処理するために一定であることが望まれている。し
かしながら、プロセスチューブである反応管内の圧力
が、プロセス実行中に変動することが多々発生してい
た。
2. Description of the Related Art Conventionally, a heat treatment process line for semiconductor wafers or the like is generally a production line in which a large number of heat treatment furnaces equipped with process tubes are installed and the exhaust system ducts of these furnaces are commonly connected to the exhaust ducts of a factory. Are configured.
The process exhaust capacity of the heat treatment apparatus depends on the exhaust capacity of the factory where the apparatus is installed, and is desired to be constant in order to uniformly heat treat a plurality of semiconductor wafers. However, the pressure in the reaction tube, which is the process tube, often changes during the process execution.

【0003】この反応管内の圧力の変動により生ずる排
気管内の圧力の変動を防止するため、排気管途中に設け
た圧力調整機構によって、自動的に内圧を調節して装置
内を均一に排気する技術としては、特開平3−2192
00号公報に記載された技術がある。
In order to prevent the fluctuation of the pressure in the exhaust pipe caused by the fluctuation of the pressure in the reaction pipe, a technique of automatically adjusting the internal pressure by a pressure adjusting mechanism provided in the middle of the exhaust pipe to uniformly exhaust the inside of the apparatus. Japanese Patent Laid-Open No. 3-2192
There is a technique described in Japanese Patent Publication No. 00.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、前述の
排気技術では装置の構成上、すなわち排気管の途中に設
けられた膨大状の凹部と、この凹部の内側縁に弾性部材
から成るOリングと、Oリングの上部に中心部が凹状に
形成された円形の可動弁が自重でOリングを押しつけ、
大気との気密状態を設定しているフロート式圧力調整機
構では、熱処理後の排気ガスがプロセスチューブに接続
された排気管路を流れ、下流に行くに従い、排気ガスの
温度が下がる。この降温現象によって結露した廃液によ
り、圧力調整機構が動作不良を起こし、所望の排気比を
一定に保持する事ができないため、半導体ウェハを均一
に熱処理できない。また熱処理後の排気ガスが反応管外
の排気管を流れる間に、温度が高温のまま結露しない場
合は、装置の構成上HCl等有毒ガスの大気中への逆拡
散する可能性もある、等の改善点を有する。
However, in the above-mentioned exhaust technology, an enormous concave portion provided in the structure of the apparatus, that is, in the middle of the exhaust pipe, and an O-ring made of an elastic member at the inner edge of the concave portion are provided. A circular movable valve with a concave central part on top of the O-ring presses the O-ring under its own weight,
In the float type pressure adjusting mechanism that sets the airtight state with the atmosphere, the exhaust gas after the heat treatment flows through the exhaust pipe line connected to the process tube, and the temperature of the exhaust gas decreases as it goes downstream. The waste liquid condensed due to this temperature decrease phenomenon causes the pressure adjusting mechanism to malfunction, and the desired exhaust ratio cannot be kept constant, so that the semiconductor wafer cannot be uniformly heat-treated. Also, when the exhaust gas after the heat treatment flows through the exhaust pipe outside the reaction tube, if the temperature remains high and does not cause condensation, there is a possibility that toxic gases such as HCl may back-diffuse into the atmosphere. Has the improvements.

【0005】本発明は、この様な事情のもとに成された
ものであり、その目的は熱処理後の排気ガスが反応管外
の排気管を流れるに従い、温度が下がる事によって結露
した廃液が排気管内に発生しても、液溜め部にて廃液を
集中捕獲して外部に排出するので、圧力調整機構の正常
動作を可能とし、また熱処理後の排気ガスが反応管外の
排気管を流れる間に、温度が高温のまま結露しない場合
は、HCl等有毒ガスの大気中への逆拡散を防止し、被
処理体を均一に熱処理することのできる処理装置、及び
処理方法を提供する事にある。
The present invention has been made under the circumstances as described above, and its purpose is to remove waste liquid condensed due to a decrease in temperature as the exhaust gas after heat treatment flows through the exhaust pipe outside the reaction tube. Even if it occurs in the exhaust pipe, the waste liquid is concentrated and discharged to the outside in the liquid reservoir, so that the pressure adjustment mechanism can operate normally, and the exhaust gas after heat treatment flows through the exhaust pipe outside the reaction tube. In the meantime, when the temperature remains high and does not cause dew condensation, it is possible to prevent back diffusion of toxic gas such as HCl into the atmosphere, and to provide a processing apparatus and a processing method capable of uniformly heat-treating an object. is there.

【0006】[0006]

【課題を解決するための手段】請求項1の発明は、被処
理体を収容して熱処理をする反応管と、この反応管に接
続された排気管の途中に少なくとも一つ設けられた液溜
め部と、この液溜め部から廃液排出系を介して接続され
た廃液排出部と、圧力調整機構とを設けた処理装置にお
いて、前記圧力調整機構の周囲を密閉して、この圧力調
整機構が動作する範囲内で雰囲気を強制排気させるため
の排気手段、とから構成されたことを特徴とする。
According to a first aspect of the present invention, there is provided a reaction tube for accommodating an object to be treated and performing heat treatment, and at least one liquid reservoir provided in the middle of an exhaust pipe connected to the reaction tube. In a processing device provided with a portion, a waste liquid discharge portion connected from the liquid storage portion via a waste liquid discharge system, and a pressure adjusting mechanism, the pressure adjusting mechanism operates by sealing the periphery of the pressure adjusting mechanism. And an exhaust means for forcibly exhausting the atmosphere within the range.

【0007】請求項2の発明は、被処理体を熱処理をす
る反応管と、この反応管に設けられた排気系に少なくと
も一つ設けられた液溜め部と、圧力調整機構とを設けた
処理装置の処理方法において、前記圧力調整機構の周囲
を密閉して、この圧力調整機構が動作する範囲内で雰囲
気を強制排気させることを特徴とする。
According to a second aspect of the present invention, there is provided a treatment tube provided with a reaction tube for heat-treating an object, a liquid reservoir provided in at least one exhaust system provided in the reaction tube, and a pressure adjusting mechanism. In the processing method of the apparatus, the periphery of the pressure adjusting mechanism is hermetically closed, and the atmosphere is forcibly exhausted within the range in which the pressure adjusting mechanism operates.

【0008】[0008]

【作用】本発明において、熱処理後の排気ガスが反応管
外の排気管を流れるに従い、温度が下がる事によって結
露した廃液が排気管内に発生しても、液溜め部にて廃液
を集中捕獲して、廃液排出管を介して接続された廃液排
出部から外部に排出するので、廃液が圧力調整機構には
流れ込まず、圧力調整機構の正常動作を可能とし、また
熱処理後の排気ガスが反応管外の排気管を流れる間に、
温度が高温のままで完全に結露しない場合は、圧力調整
機構の正常動作を保ちつつ、HCl等有毒ガスの大気中
への逆拡散を防止する。
In the present invention, as the exhaust gas after the heat treatment flows through the exhaust pipe outside the reaction tube, the temperature of the exhaust gas decreases, and even if a condensed liquid is generated in the exhaust pipe, the waste liquid is trapped in a concentrated manner in the liquid reservoir. The waste liquid is discharged to the outside from the waste liquid discharge part connected via the waste liquid discharge pipe, so that the waste liquid does not flow into the pressure adjustment mechanism and the pressure adjustment mechanism can operate normally. While flowing through the outside exhaust pipe,
When the temperature remains high and does not completely dew, the normal operation of the pressure adjusting mechanism is maintained and the back diffusion of toxic gas such as HCl into the atmosphere is prevented.

【0009】[0009]

【実施例】以下本発明の実施例について具体的に説明す
る。図1は本発明を縦型常圧水蒸気酸化熱処理装置に適
用した一実施例を示す説明図である。耐熱材料、例えば
石英からなる垂直方向に長く底面に蓋部を有する反応
管、例えば縦型のプロセスチューブ10の一端部にプロ
セスガス導入管12が連結され、他端部に排出管13が
設けられている。
EXAMPLES Examples of the present invention will be specifically described below. FIG. 1 is an explanatory view showing an embodiment in which the present invention is applied to a vertical atmospheric steam oxidation heat treatment apparatus. A reaction tube made of a heat-resistant material, such as quartz, which is long in the vertical direction and has a lid on the bottom surface, for example, a vertical process tube 10, has a process gas introduction pipe 12 connected to one end thereof and a discharge pipe 13 provided at the other end thereof. ing.

【0010】上記プロセスチューブ10の側壁外周囲に
はこのプロセスチューブ10と同軸的に筒状ヒータ、例
えば抵抗加熱ヒータ16が設けられ、プロセスチューブ
10を所定の熱処理温度、例えば800℃〜1200℃
の範囲で適宜制御設定可能である。被処理体として、例
えば複数枚の半導体ウェハ17は耐熱性材料、例えば石
英製ウェハボート18に収容され、この石英製ウェハボ
ート18は載置台19に設置され、上記プロセスチュー
ブ10内の予め定められた位置、すなわち均熱領域に収
納されるように構成されている。
A cylindrical heater, such as a resistance heater 16, is provided coaxially with the process tube 10 on the outer periphery of the side wall of the process tube 10. The process tube 10 has a predetermined heat treatment temperature, for example, 800 ° C. to 1200 ° C.
The control can be set appropriately within the range. As the objects to be processed, for example, a plurality of semiconductor wafers 17 are accommodated in a heat-resistant material, for example, a wafer boat 18 made of quartz, and the wafer boat 18 made of quartz is installed on a mounting table 19 and is predetermined in the process tube 10. It is configured to be stored in a different position, that is, in a soaking area.

【0011】上記載置台19は蓋体20上に設置され、
この蓋体20は昇降機構31により上記複数枚の半導体
ウェハ17を収納した状態で上下方向にに移動する事が
でき、半導体ウェハ17を収納した上記ウェハボート1
8を上記プロセスチューブ10に対しての搬入搬出を行
えるように構成されている。
The mounting table 19 described above is installed on the lid 20.
The lid 20 can be moved in the vertical direction in a state where the plurality of semiconductor wafers 17 are accommodated by the elevating mechanism 31, and the wafer boat 1 in which the semiconductor wafers 17 are accommodated.
8 is configured so that it can be carried in and out of the process tube 10.

【0012】前記プロセスガス導入管12には、処理ガ
ス例えば水蒸気発生源32から水蒸気を、マスフローコ
ントローラ34からHClガスを供給できるよう構成さ
れている。
The process gas introduction pipe 12 is constructed so that a processing gas, for example, steam from a steam generation source 32 and HCl gas from a mass flow controller 34 can be supplied.

【0013】前記排出管13は、結合バルブを介して水
平に配置された第2の排気管21が結合され、この第2
の排気管21には、主筒を垂直に配置した第1の排気管
22が結合されており、この第1の排気管22には配管
途中に液溜管23が設けられている。この液溜管23
は、排気の結露した廃液を集中捕獲して外部に排出する
と供に、高温のまま気化したままの排気の一部を、スカ
ベンジャー部25へ還流させることを目的とし、還流管
23の先端には、圧力調整機構40が設けられている。
この圧力調整機構40は、排気流の圧力を予め設定され
た圧力に自動的に設定するためのものである。
A second exhaust pipe 21 arranged horizontally is connected to the discharge pipe 13 via a connecting valve.
A first exhaust pipe 22 in which a main cylinder is vertically arranged is coupled to the exhaust pipe 21, and a liquid reservoir 23 is provided in the middle of the first exhaust pipe 22. This liquid reservoir 23
Is intended to recirculate a part of the exhaust gas that remains vaporized at a high temperature to the scavenger section 25 while collecting the condensed waste liquid of the exhaust gas and discharging it to the outside. A pressure adjusting mechanism 40 is provided.
The pressure adjusting mechanism 40 is for automatically setting the pressure of the exhaust flow to a preset pressure.

【0014】上記スカベンジャー部25では、前記プロ
セスチューブ10及び前記圧力調整機構40から、漏れ
出たHClガス等有毒ガスを、吸引管26を設けて、図
示しない強制排気機構、例えば真空ポンプ(図示せず)
等により排出するよう構成されている。
In the scavenger section 25, a toxic gas such as HCl gas leaked from the process tube 10 and the pressure adjusting mechanism 40 is provided with a suction pipe 26, and a forced exhaust mechanism (not shown) such as a vacuum pump (not shown) is provided. No)
And so on.

【0015】次に図2を参照して、圧力調整機構40の
構成の一例を具体的に説明する。前記第1の排気管22
の途中から例えば下方に曲げられた支流管41の端部に
膨大状の凹部43が設けられ、この凹部43の内側縁に
弾性部材から成るOリング44が配設されている。この
Oリング44の上部には中心部が凹状に形成された円形
の可動弁45が、例えば自重でOリング44を押しつ
け、圧力調整機構40と大気との気密状態を設定してい
る。
Next, an example of the structure of the pressure adjusting mechanism 40 will be specifically described with reference to FIG. The first exhaust pipe 22
An enlarging concave portion 43 is provided at an end portion of the tributary pipe 41 bent downward from the middle thereof, and an O-ring 44 made of an elastic member is arranged at an inner edge of the concave portion 43. A circular movable valve 45 having a concave central portion is pressed on the upper portion of the O-ring 44, for example, by pressing the O-ring 44 by its own weight to set an airtight state between the pressure adjusting mechanism 40 and the atmosphere.

【0016】上記第1の排気管22と上記第2の排気管
21の接続点より例えば下方、及び液溜管23の例えば
下方には廃液排出部、例えば廃液排出機構50が接続配
置されている。強制吸引機構、例えば真空ポンプ等を設
ければ上方でも良い。この廃液排出機構50は図3に示
すように、図1の上記第1の排気管22及び液溜管23
から延長して位置する廃液排出管51を廃液容器、例え
ば廃液溜め部52の内側に挿入配置し、この廃液溜め部
52の上部には穴部54を少なくとも1個以上設け、廃
液55が上部穴部54から溢れ出る様に構成され、廃液
溜め部52の周囲は外側ケース56で密閉されて構成さ
れている。この溢水構造により共通廃液管63との直結
を回避し、排気流の乱れを防止している。
A waste liquid discharge part, for example, a waste liquid discharge mechanism 50 is connected and arranged, for example, below the connection point between the first exhaust pipe 22 and the second exhaust pipe 21 and below the liquid reservoir pipe 23, for example. . If a forced suction mechanism such as a vacuum pump is provided, it may be above. As shown in FIG. 3, the waste liquid discharge mechanism 50 includes the first exhaust pipe 22 and the liquid storage pipe 23 shown in FIG.
A waste liquid discharge pipe 51 extending from the inside of the waste liquid container, for example, a waste liquid reservoir 52, is inserted and disposed, and at least one hole 54 is provided in the upper portion of the waste liquid reservoir 52. It is configured so as to overflow from the portion 54, and the periphery of the waste liquid storage portion 52 is configured to be sealed by an outer case 56. With this overflow structure, direct connection with the common waste liquid pipe 63 is avoided and turbulence of the exhaust flow is prevented.

【0017】このようにして一系統の熱処理装置が構成
されている。このような熱処理装置が、半導体製造工場
では複数系統並列に配置され、これらの排気系及び廃液
排出系は、最終的には一系統に集合される。
In this way, a single-system heat treatment apparatus is constructed. Such a heat treatment apparatus is arranged in parallel in a plurality of systems in a semiconductor manufacturing factory, and the exhaust system and the waste liquid discharge system are finally assembled into one system.

【0018】即ち、複数のプロセスチューブ10の排気
駆動を、共通排気管61に設置した排気能力の大きな1
つの排気ファン62により排気されるように構成されて
いる。この排気ファン62については例えば真空ポンプ
で構成しても良い。
That is, the exhaust drive of a plurality of process tubes 10 is installed in the common exhaust pipe 61 and the exhaust capacity is large.
The two exhaust fans 62 are configured to exhaust the air. The exhaust fan 62 may be configured by a vacuum pump, for example.

【0019】また、複数のプロセスチューブ10の熱処
理後の排気ガスが、排気管路を流れるに従い温度が下が
る事によって結露した廃液は、廃液排出機構50から共
通廃液排出管63を介して排出されるよう構成されてい
る。
Further, the exhaust liquid after the heat treatment of the plurality of process tubes 10 is condensed by the temperature of the exhaust gas being lowered as it flows through the exhaust pipe line, and the waste liquid is discharged from the waste liquid discharge mechanism 50 through the common waste liquid discharge pipe 63. Is configured.

【0020】尚、高温ガスやHCl等の腐食性ガスと接
触する前記プロセスガス導入管12、排出管13、第2
の排気管21、第1の排気管22、液溜管23、吸引管
26、圧力調整機構40、廃液排出機構50、廃液排出
管51、及び共通廃液排出管63の部分は、非金属、例
えば石英やフッ素樹脂等の耐熱耐食性部材から構成され
ている。
The process gas introduction pipe 12, the discharge pipe 13, and the second pipe which come into contact with a high temperature gas and a corrosive gas such as HCl.
The exhaust pipe 21, the first exhaust pipe 22, the liquid collecting pipe 23, the suction pipe 26, the pressure adjusting mechanism 40, the waste liquid discharging mechanism 50, the waste liquid discharging pipe 51, and the common waste liquid discharging pipe 63 are non-metal, for example, It is composed of a heat and corrosion resistant member such as quartz or fluororesin.

【0021】このように多数の常圧熱処理装置の排気系
が一系統に統一されるため、排気量の総量は一定にする
必要がある。従って、この排気量を一定にする手段とし
て、上記圧力調整機構40、及び廃液排出機構50が各
系の排気管路に設けられている。
As described above, since the exhaust system of many atmospheric pressure heat treatment apparatuses is unified into one system, it is necessary to keep the total exhaust amount constant. Therefore, the pressure adjusting mechanism 40 and the waste liquid discharging mechanism 50 are provided in the exhaust pipe line of each system as means for keeping the exhaust amount constant.

【0022】次に前述実施例の作用について述べる。複
数のプロセスチューブ10の内、1つのプロセスチュー
ブ10に処理ガスが供給されており、他のプロセスチュ
ーブ10には処理ガスが供給されず蓋体20が閉じられ
ている状態では、排気ファン62の排気能力に対して流
れる処理ガスの流量が少ないため、第1の排気管22の
中の圧力は比較的大きく負圧状態となる。
Next, the operation of the above embodiment will be described. In a state where the processing gas is supplied to one of the plurality of process tubes 10 and the processing gas is not supplied to the other process tubes 10 and the lid 20 is closed, the exhaust fan 62 is Since the flow rate of the processing gas flowing with respect to the exhaust capacity is small, the pressure in the first exhaust pipe 22 becomes relatively large and becomes a negative pressure state.

【0023】その結果、可動弁45の重さより可動弁4
5に加わる差圧の力が大きくなり、可動弁45は大きく
浮き上がり凹部43を介してスカベンジャー部25内雰
囲気が第1の排気管22へ流入し、内圧は予め定めれた
圧力に常に保たれる。
As a result, the movable valve 4 is weighed more than the movable valve 45.
The force of the differential pressure applied to 5 is increased, the movable valve 45 is largely lifted, and the atmosphere in the scavenger portion 25 flows into the first exhaust pipe 22 through the concave portion 43, and the internal pressure is always maintained at a predetermined pressure. .

【0024】その際スカベンジャー部25から吸引管2
6を介して強制排気される場合、その排気能力は排気フ
ァン62の排気能力を下回る必要がある。また、圧力調
整機構40から有毒な排気ガスが逆拡散したとしても、
密閉されたスカベンジャー部25内なので、工場作業員
の安全は確保される。
At this time, the scavenger portion 25 to the suction pipe 2
When forcedly exhausted via 6, the exhaust capacity must be lower than the exhaust capacity of the exhaust fan 62. Further, even if the toxic exhaust gas diffuses back from the pressure adjusting mechanism 40,
Since it is inside the closed scavenger section 25, the safety of factory workers is ensured.

【0025】更に、他のプロセスチューブ10に半導体
ウェハ17を搬入するため蓋体20を開けた状態では、
プロセスチューブ10から多量の大気が第1の排気管2
2に流れ込み、内圧は上昇する。
Further, in a state where the lid 20 is opened to carry the semiconductor wafer 17 into another process tube 10,
A large amount of atmospheric air is discharged from the process tube 10 to the first exhaust pipe 2
It flows into 2, and the internal pressure rises.

【0026】この時、今まで大きく開いていた圧力調整
機構40の可動弁45の開度が狭くなり、所望の圧力が
得られる状態で安定する。このように圧力調整機構40
の可動弁45の開度が第1の排気管22内の圧力に応じ
て変化し、常に所望の圧力が保たれるように作動する。
プロセス状態を変えるためプロセスチューブ10に流す
ガスの流量を変化させた場合も、上記と同様に圧力調整
機構40の可動弁45が作動し、常に所望の圧力に保持
する。
At this time, the opening degree of the movable valve 45 of the pressure adjusting mechanism 40, which has been wide open up to now, becomes narrow, and the desired pressure is stabilized. In this way, the pressure adjusting mechanism 40
The opening degree of the movable valve 45 changes according to the pressure in the first exhaust pipe 22, and operates so that a desired pressure is always maintained.
Even when the flow rate of the gas flowing through the process tube 10 is changed in order to change the process state, the movable valve 45 of the pressure adjusting mechanism 40 operates in the same manner as described above, and the desired pressure is always maintained.

【0027】また、廃液については抵抗加熱ヒータ16
によりプロセスチューブ10内の均熱領域を、酸化処理
温度例えば1000℃の温度に設定し、処理ガスとして
水蒸気とHClガスをプロセスチューブ10内に収納さ
れている被処理体、例えば半導体ウェハ17に供給す
る。そしてプロセスチューブ10内を通過して排気され
第1の排気管22の内壁で水蒸気が冷やされ、HClを
含んだ廃液はこの第1の排気管22の内壁に沿って落下
し、または液溜管23にて集中捕獲され、廃液管51を
通り廃液排出機構50の廃液溜め部52から溢れだし、
共通廃液排出管63に排出する。
For the waste liquid, the resistance heater 16 is used.
By setting the soaking region in the process tube 10 to an oxidation treatment temperature, for example, a temperature of 1000 ° C., steam and HCl gas as a treatment gas are supplied to the object to be treated, for example, the semiconductor wafer 17 accommodated in the process tube 10. To do. Then, after passing through the inside of the process tube 10 and being exhausted, the water vapor is cooled on the inner wall of the first exhaust pipe 22, the waste liquid containing HCl falls along the inner wall of the first exhaust pipe 22, or the liquid collecting pipe. 23 is intensively captured, passes through the waste liquid pipe 51, and overflows from the waste liquid reservoir 52 of the waste liquid discharge mechanism 50.
Discharge to the common waste liquid discharge pipe 63.

【0028】以下に前述実施例の効果について説明す
る。本発明によれば、熱処理後の排気ガスがプロセスチ
ューブ10外の排気管路を流れるに従い、温度が下がる
事によって結露した廃液が排気管路内に発生しても、廃
液排出管51を介して排出することができる。また、廃
液が圧力調整機構40には流れ込まず外部に漏れ出る事
を防止し、可動弁45の正常動作を可能とする。
The effects of the above embodiment will be described below. According to the present invention, as the exhaust gas after the heat treatment flows through the exhaust pipe line outside the process tube 10, the temperature of the exhaust gas decreases, so that even if a waste liquid is formed in the exhaust pipe line due to dew condensation, the waste liquid is discharged through the waste liquid discharge pipe 51. Can be discharged. Further, the waste liquid is prevented from leaking to the outside without flowing into the pressure adjusting mechanism 40, which enables the movable valve 45 to operate normally.

【0029】従って、熱処理の中でもウェット酸化処理
のように多量の水蒸気を流し、どの様に廃液が多くなっ
ても廃液によって第1の排気管22や第2の排気管21
は塞がれることはなく、半導体ウェハ17間のバラツキ
のない所望の処理を行うことができる。
Therefore, even in the heat treatment, a large amount of water vapor is caused to flow as in the wet oxidation treatment, and no matter how much the waste liquid becomes, the waste liquid causes the first exhaust pipe 22 and the second exhaust pipe 21.
Is not blocked, and desired processing can be performed without variations between the semiconductor wafers 17.

【0030】また本発明によれば、熱処理後の排気ガス
が反応管外の排気管を流れる間に、温度が高温のまま結
露しない場合でも、HCl等有毒ガスの大気中への逆拡
散を防止する。従って、工場作業者の安全を確保し、か
つプロセスチューブ10内を流れるプロセスガスの均一
排気が可能となり、もって装置内のガス流に乱れが生じ
なくなり、半導体ウェハ17の面内面間均一性を良好に
処理する事ができる。
Further, according to the present invention, while the exhaust gas after the heat treatment flows through the exhaust pipe outside the reaction pipe, even if the temperature is high and there is no dew condensation, back diffusion of toxic gas such as HCl into the atmosphere is prevented. To do. Therefore, the safety of the factory worker can be ensured, and the process gas flowing in the process tube 10 can be uniformly exhausted, so that the gas flow in the apparatus is not disturbed and the in-plane uniformity of the surface of the semiconductor wafer 17 is good. Can be processed.

【0031】更に、HCl等の腐食性ガスを流しても廃
液排出機構50は非金属の耐蝕性部材で構成されている
ため、腐食は起こらない。
Further, even if a corrosive gas such as HCl is flowed, the waste liquid discharge mechanism 50 is composed of a non-metal corrosion resistant member, so that no corrosion occurs.

【0032】次に本発明の他の実施例について説明す
る。図4に示すように、排出管13は結合バルブを介し
て水平に配置された第2の排気管21が結合され、この
第2の排気管21には、主筒を垂直に配置した第1の排
気管22が結合されている。この第1の排気管22は配
管途中に分岐して設けられた支流管41に液溜め部、例
えば鍵形あるいはU字形に湾曲された液溜管23が設け
られている。この液溜管23を経て下方に曲げられた支
流管41の端部に圧力調整機構40が設けられている。
Next, another embodiment of the present invention will be described. As shown in FIG. 4, the exhaust pipe 13 is connected to a second exhaust pipe 21 which is horizontally arranged via a coupling valve, and the second exhaust pipe 21 has a first cylinder in which a main cylinder is vertically arranged. Exhaust pipe 22 is connected. The first exhaust pipe 22 is provided with a liquid collecting portion, for example, a liquid collecting pipe 23 curved in a key shape or a U shape, in a branch pipe 41 provided in a branch in the middle of the pipe. A pressure adjusting mechanism 40 is provided at an end of a branch pipe 41 that is bent downward through the liquid reservoir 23.

【0033】更に上記圧力調整機構40の周囲を、覆い
65で密閉し、バルブ66を介して共通排気管61に接
続されている。そしてこのバルブ66により、前記覆い
65内の雰囲気は、共通排気管61よりも陽圧に設定さ
れている。
Further, the circumference of the pressure adjusting mechanism 40 is sealed with a cover 65 and is connected to a common exhaust pipe 61 via a valve 66. With this valve 66, the atmosphere in the cover 65 is set to a positive pressure higher than that in the common exhaust pipe 61.

【0034】また排気流路に冷却部を設け、この冷却部
で強制的に排気ガスを液化し、この液化部に液溜め部を
設ければ、この場合も液溜め部は一か所でよい。尚、図
4においてその他の部分は前述第一実施例と同じである
ので、同一部分には同一符号を付して、その説明は省略
する。
Further, if a cooling unit is provided in the exhaust passage, the exhaust gas is forcibly liquefied by this cooling unit, and a liquid reservoir is provided in this liquefaction unit, the liquid reservoir may be provided in one place in this case as well. . Since the other parts in FIG. 4 are the same as those of the first embodiment, the same parts are designated by the same reference numerals and the description thereof will be omitted.

【0035】本実施例の作用について説明すると、前述
第一実施例と同じく、圧力調整機構40の可動弁45の
開度が第1の排気管22内の圧力に応じて変化し、常に
所望の圧力が保たれるように作動し、プロセス状態を変
えるためプロセスチューブ10に流すガスの流量を変化
させた場合も、上記と同様に圧力調整機構40の可動弁
45が作動し、常に所望の圧力に保たれる。また、廃液
についても液溜管23から廃液排出管51を通り、廃液
排出機構50の液溜め部55から溢れだし、共通廃液排
出管63に排出される。また、圧力調整機構40からH
Cl等の有毒な排気ガスが工場内に漏れる事もない。
The operation of this embodiment will be described. As in the first embodiment, the opening degree of the movable valve 45 of the pressure adjusting mechanism 40 changes according to the pressure in the first exhaust pipe 22 and is always desired. Even when the flow rate of the gas flowing through the process tube 10 is changed so as to maintain the pressure and change the process state, the movable valve 45 of the pressure adjusting mechanism 40 is operated similarly to the above, and the desired pressure is constantly maintained. Kept in. The waste liquid also passes from the liquid storage pipe 23 through the waste liquid discharge pipe 51, overflows from the liquid reservoir 55 of the waste liquid discharge mechanism 50, and is discharged to the common waste liquid discharge pipe 63. Also, from the pressure adjusting mechanism 40 to H
No toxic exhaust gas such as Cl will leak into the factory.

【0036】本実施例では、第一実施例に比較して、従
来より工場内に設置してある装置においても、排気系の
一部追加改造を実施することにより、処理ウェハ間のバ
ラツキのない等の、所望の処理を行うことができる。
In this embodiment, compared with the first embodiment, even in the apparatus conventionally installed in the factory, by partially modifying the exhaust system, there is no variation between processed wafers. Desired processing such as can be performed.

【0037】尚、本発明は前述実施例に限定されるもの
ではなく、本発明の要旨の範囲内で種々の変形実施が可
能である。
The present invention is not limited to the above-mentioned embodiments, and various modifications can be made within the scope of the gist of the present invention.

【0038】本発明は必ずしも複数のプロセスチューブ
に対して排気駆動源を共通化したものに適用するものに
限らず、第1の排気管22が単一のプロセスチューブ1
0専用に設けられている場合においても、プロセス状態
を変えるため処理ガスの流量を変えたり、電源電圧変動
等により排気ファン25の性能が変わったりする事があ
り、均一排気を行うために本発明は有用である。
The present invention is not necessarily applied to a plurality of process tubes having a common exhaust drive source, and the first exhaust pipe 22 is a single process tube 1.
Even if it is provided exclusively for 0, the flow rate of the processing gas may be changed to change the process state, or the performance of the exhaust fan 25 may be changed due to fluctuations in the power supply voltage and the like. Is useful.

【0039】また、所望の圧力で圧力調整機構40の可
動弁45の重さを調整できるようにするか、可動弁45
をスプリングで押すか又は引っ張ることも本発明を実施
する上で有用である。
The weight of the movable valve 45 of the pressure adjusting mechanism 40 can be adjusted at a desired pressure, or the movable valve 45 can be adjusted.
It is also useful in practicing the invention to push or pull the spring.

【0040】更に、本発明は酸化炉や拡散炉等の熱処理
炉に限らず、常圧CVD装置やその他常圧処理装置に応
用してもよいことは当然である。また、縦型装置に限ら
ず横型熱処理炉等の横型装置に適用できるのは当然のこ
とである。
Furthermore, the present invention is not limited to a heat treatment furnace such as an oxidation furnace or a diffusion furnace, and it goes without saying that it may be applied to an atmospheric pressure CVD apparatus or other atmospheric pressure processing apparatus. Further, it goes without saying that the invention can be applied not only to the vertical apparatus but also to horizontal apparatuses such as a horizontal heat treatment furnace.

【0041】更にまた、本発明はバッチ処理に限らず、
枚葉処理でも同様な効果の得られることは説明するまで
もないことである。
Furthermore, the present invention is not limited to batch processing,
It goes without saying that the same effect can be obtained by the single-wafer processing.

【0042】[0042]

【発明の効果】本発明によれば、熱処理後の排気ガスが
反応管外の排気管を流れるに従い、温度が下がる事によ
って結露した廃液が排気管内に発生しても、廃液排出管
を介して接続された廃液排出部から外部に排出するの
で、廃液が圧力調整機構には流れ込まず、圧力調整機構
の正常動作を可能とし、また熱処理後の排気ガスが反応
管外の排気管を流れる間に、温度が高温のままで完全に
結露しない場合は、圧力調整機構の正常動作を保ちつ
つ、HCl等有毒ガスの大気中への逆拡散を防止する。
従って、安全にかつ、処理ウェハ間のバラツキのない所
望の均一な熱処理を行うことができる。
According to the present invention, as the exhaust gas after the heat treatment flows through the exhaust pipe outside the reaction tube, the temperature of the exhaust gas decreases, so that even if a waste liquid is formed in the exhaust pipe due to dew condensation, the waste liquid is exhausted through the exhaust pipe. Since the waste liquid is discharged to the outside from the connected waste liquid discharge part, the waste liquid does not flow into the pressure adjusting mechanism and enables the pressure adjusting mechanism to operate normally, and while the exhaust gas after heat treatment flows through the exhaust pipe outside the reaction tube. When the temperature remains high and does not completely dew, the normal operation of the pressure adjusting mechanism is maintained and the back diffusion of toxic gas such as HCl into the atmosphere is prevented.
Therefore, the desired uniform heat treatment can be performed safely and without variations between the processed wafers.

【図面の簡単な説明】[Brief description of drawings]

【図1】縦型熱処理装置に適用した本発明の一実施例を
示す説明図である。
FIG. 1 is an explanatory diagram showing an embodiment of the present invention applied to a vertical heat treatment apparatus.

【図2】図1の圧力調整機構を示す説明図である。FIG. 2 is an explanatory view showing a pressure adjusting mechanism of FIG.

【図3】図1の廃液排出機構を示す説明図である。FIG. 3 is an explanatory view showing the waste liquid discharge mechanism of FIG. 1.

【図4】縦型熱処理装置に適用した本発明の他の実施例
を示す説明図である。
FIG. 4 is an explanatory view showing another embodiment of the present invention applied to a vertical heat treatment apparatus.

【符号の説明】[Explanation of symbols]

10 プロセスチューブ 17 半導体ウェハ 18 ウェハボート 21 第2の排気管 22 第1の排気管 23 液溜管 25 スカベンジャー部 26 吸引管 40 圧力調整機構 50 廃液排出機構 51 廃液排出管 52 廃液溜め部 55 廃液 65 覆い 66 バルブ 10 process tubes 17 Semiconductor wafer 18 wafer boat 21 Second exhaust pipe 22 First exhaust pipe 23 Liquid Reservoir 25 Scavenger Club 26 Suction tube 40 Pressure adjustment mechanism 50 Waste liquid discharge mechanism 51 Waste liquid discharge pipe 52 Waste liquid reservoir 55 Waste liquid 65 Cover 66 valves

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) H01L 21/22 H01L 21/324 H01L 21/205 ─────────────────────────────────────────────────── ─── Continuation of the front page (58) Fields surveyed (Int.Cl. 7 , DB name) H01L 21/22 H01L 21/324 H01L 21/205

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 被処理体を収容して熱処理をする反応管
と、この反応管に接続された排気管の途中に少なくとも
一つ設けられた液溜め部と、この液溜め部から廃液排出
管を介して接続された廃液排出部と、圧力調整機構とを
設けた処理装置において、 前記圧力調整機構の周囲を密閉して、この圧力調整機構
が動作する範囲内で雰囲気を強制排気させるための排気
手段、とから構成されたことを特徴とする処理装置。
1. A reaction tube for accommodating an object to be treated and performing heat treatment, a liquid reservoir provided at least one in the middle of an exhaust pipe connected to the reaction tube, and a waste liquid discharge pipe from the liquid reservoir. In a processing device provided with a waste liquid discharge part connected via a pressure adjusting mechanism, for sealing the periphery of the pressure adjusting mechanism, for forcibly exhausting the atmosphere within the range in which the pressure adjusting mechanism operates. A processing apparatus comprising: an exhaust unit.
【請求項2】 被処理体を熱処理をする反応管と、この
反応管に設けられた排気系に少なくとも一つ設けられた
液溜め部と、圧力調整機構とを設けた処理装置の処理方
法において、 前記圧力調整機構の周囲を密閉して、この圧力調整機構
が動作する範囲内で雰囲気を強制排気させることを特徴
とする処理方法。
2. A processing method of a processing apparatus, comprising: a reaction tube for heat-treating an object to be processed; a liquid reservoir provided in at least one exhaust system provided in the reaction tube; and a pressure adjusting mechanism. A processing method characterized in that the periphery of the pressure adjusting mechanism is hermetically closed and the atmosphere is forcibly exhausted within a range in which the pressure adjusting mechanism operates.
【請求項3】 被処理体を処理する処理部と、この処理
部に接続された排気系の途中に少なくとも一つ設けられ
た液溜め部と、この液溜め部から廃液排出管を介して接
続された廃液排出部と、圧力調整機構とを設けた処理装
置において、 前記圧力調整機構の周囲を密閉して、この圧力調整機構
が動作する範囲内で雰囲気を強制排気させるための排気
手段、とから構成されたことを特徴とする処理装置。
3. A processing section for processing an object to be processed, a liquid storage section provided at least one in the middle of an exhaust system connected to the processing section, and connected from the liquid storage section via a waste liquid discharge pipe. In the processing device provided with the waste liquid discharging section and the pressure adjusting mechanism, the exhaust means for sealing the periphery of the pressure adjusting mechanism and forcibly exhausting the atmosphere within the range in which the pressure adjusting mechanism operates, and A processing device comprising:
【請求項4】 被処理体を処理をする処理部と、この処
理部に設けられた排気系に少なくとも一つ設けられた液
溜め部と、圧力調整機構とを設けた処理装置の処理方法
において、 前記圧力調整機構の周囲を密閉して、この圧力調整機構
が動作する範囲内で雰囲気を強制排気させることを特徴
とする処理方法。
4. A processing method of a processing apparatus comprising a processing section for processing an object to be processed, a liquid storage section provided in at least one exhaust system provided in the processing section, and a pressure adjusting mechanism. A processing method characterized in that the periphery of the pressure adjusting mechanism is hermetically closed and the atmosphere is forcibly exhausted within a range in which the pressure adjusting mechanism operates.
JP34786693A 1993-12-24 1993-12-24 Processing device and processing method Expired - Fee Related JP3406040B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34786693A JP3406040B2 (en) 1993-12-24 1993-12-24 Processing device and processing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34786693A JP3406040B2 (en) 1993-12-24 1993-12-24 Processing device and processing method

Publications (2)

Publication Number Publication Date
JPH07183242A JPH07183242A (en) 1995-07-21
JP3406040B2 true JP3406040B2 (en) 2003-05-12

Family

ID=18393133

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34786693A Expired - Fee Related JP3406040B2 (en) 1993-12-24 1993-12-24 Processing device and processing method

Country Status (1)

Country Link
JP (1) JP3406040B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006245492A (en) * 2005-03-07 2006-09-14 Gasonics:Kk Equipment and method for heat treating substrate
JP5054599B2 (en) * 2008-04-17 2012-10-24 エスペック株式会社 Condensation suppression device and environmental test device equipped with the same

Also Published As

Publication number Publication date
JPH07183242A (en) 1995-07-21

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