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JP2006040990A - Reduced pressure heat treatment apparatus and method of restoration to normal pressure of the apparatus - Google Patents

Reduced pressure heat treatment apparatus and method of restoration to normal pressure of the apparatus Download PDF

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JP2006040990A
JP2006040990A JP2004215179A JP2004215179A JP2006040990A JP 2006040990 A JP2006040990 A JP 2006040990A JP 2004215179 A JP2004215179 A JP 2004215179A JP 2004215179 A JP2004215179 A JP 2004215179A JP 2006040990 A JP2006040990 A JP 2006040990A
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pressure
processing container
value
heat treatment
flow rate
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Takeshi Kobayashi
健 小林
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Tokyo Electron Ltd
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<P>PROBLEM TO BE SOLVED: To provide a reduced-pressure heat treatment apparatus which can restore a processing container to normal pressure stably and rapidly without making the inside of the processing container into a pressurized state and can shorten a TAT, and to provide a method of restoration to normal pressure. <P>SOLUTION: The reduced-pressure heat treatment apparatus 1 is so structured that, after a workpiece is stored in the processing container 2 and then heat-treated in a prescribed low pressure atmosphere, an inert gas is introduced into the processing container 2 by means of a flow controller 9 to restore the inside of the processing container 2 to normal pressure. The apparatus 1 includes a pressure sensor 18 for detecting pressure inside the processing container 2; and a controlling unit 19 which controls the flow controller 19 so that the inert gas may be introduced in such a flow rate as to keep the inside of the processing container 2 from becoming a pressurized state, when restoring the inside of the processing container 2 to normal pressure by introducing the inert gas into the container 2 after heat treatment. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、減圧熱処理装置及びその常圧復帰方法に関する。   The present invention relates to a reduced pressure heat treatment apparatus and a method for returning to normal pressure.

半導体装置の製造においては、被処理体例えば半導体ウエハに例えば酸化、拡散、CVD、アニール等の各種の熱処理を施す工程があり、これらの工程を所定の減圧(真空)雰囲気下で実行するための装置として減圧熱処理装置が用いられている。この減圧熱処理装置は、ウエハを収容して所定の減圧雰囲気下で熱処理するための処理容器を備え、この処理容器には処理容器内を所定の減圧に排気可能な排気系と、処理容器内に処理ガスや不活性ガスを導入するガス導入系とが接続されている。このような減圧熱処理装置(例えばCVD装置)においては、熱処理後(プロセス完了後)に、処理容器内から常圧(大気圧)側にウエハを搬出(アンロード)するために、処理容器内を常圧ないし微減圧で排気しながら処理容器内に不活性ガス例えば窒素ガス(N)を流量制御器を介して導入し、処理容器内を不活性ガスで置換しながら高真空から常圧(大気圧)に復帰させることが行われている(例えば、特開平7-227534号公報、特開2001−146975公報参照)。 In the manufacture of a semiconductor device, there are processes for subjecting an object to be processed, such as a semiconductor wafer, to various heat treatments such as oxidation, diffusion, CVD, annealing, etc., and for performing these processes in a predetermined reduced pressure (vacuum) atmosphere. A vacuum heat treatment apparatus is used as the apparatus. The reduced pressure heat treatment apparatus includes a processing container for accommodating a wafer and heat-treating in a predetermined reduced pressure atmosphere. The processing container includes an exhaust system capable of evacuating the processing container to a predetermined reduced pressure, and a processing container. A gas introduction system for introducing processing gas and inert gas is connected. In such a reduced-pressure heat treatment apparatus (for example, a CVD apparatus), after the heat treatment (after completion of the process), in order to unload the wafer from the treatment container to the normal pressure (atmospheric pressure) side, An inert gas such as nitrogen gas (N 2 ) is introduced into the processing vessel through a flow controller while evacuating at normal pressure or slightly reduced pressure, and the inside of the processing vessel is replaced with inert gas from high vacuum to normal pressure ( (For example, refer to JP-A-7-227534 and JP-A-2001-146975).

特開平7-227534号公報JP-A-7-227534 特開2001−146975公報JP 2001-146975 A

ところで、前記常圧復帰に要する時間を短縮させてTAT(Turn Around Time)の短縮化を図るために、処理容器内に常温の不活性ガスを大流量で導入する試みがなされている。しかしながら、処理容器は熱容量が大きく冷めにくいだけでなく、次の処理に備えて高温に保たれることが多いため、処理容器内に常温の不活性ガスを大流量で流入させると、気体の急激な熱膨張により処理容器内が加圧状態になってしまい、シール面からのリーク等の不具合を発生する可能性があった。   By the way, an attempt has been made to introduce an inert gas at a normal temperature into a processing vessel at a large flow rate in order to shorten the time required for the return to normal pressure to shorten TAT (Turn Around Time). However, since the processing container not only has a large heat capacity and is difficult to cool, but is often kept at a high temperature in preparation for the next processing, if a normal temperature inert gas flows into the processing container at a large flow rate, the gas rapidly Due to the thermal expansion, the inside of the processing container is in a pressurized state, which may cause a problem such as leakage from the sealing surface.

本発明は、上記事情を考慮してなされたものであり、処理容器内を加圧状態にすることなく安定して迅速に常圧復帰させることができ、TATの短縮化が図れる減圧熱処理装置及びその常圧復帰方法を提供することを目的とする。   The present invention has been made in view of the above circumstances, and a reduced pressure heat treatment apparatus that can return to normal pressure stably and quickly without bringing the inside of the processing vessel into a pressurized state, and can reduce TAT. An object of the present invention is to provide a method for restoring the normal pressure.

本発明のうち、請求項1に係る発明は、処理容器内に被処理体を収容して所定の減圧雰囲気下で熱処理した後、処理容器内に流量制御器により不活性ガスを導入して処理容器内を常圧に復帰させる減圧熱処理装置の常圧復帰方法であって、前記処理容器内の圧力を検出し、該圧力が加圧状態にならないように流量制御器により不活性ガスの導入流量を制御することを特徴とする。   Among the present inventions, the invention according to claim 1 is a process in which an object to be processed is accommodated in a processing container and heat-treated in a predetermined reduced-pressure atmosphere, and then an inert gas is introduced into the processing container by a flow controller. A normal pressure recovery method of a reduced pressure heat treatment apparatus for returning the inside of a container to normal pressure, wherein the pressure in the processing container is detected, and a flow rate controller introduces an inert gas flow rate so that the pressure does not become a pressurized state. It is characterized by controlling.

請求項2に係る発明は、処理容器内に被処理体を収容して所定の減圧雰囲気下で熱処理した後、処理容器内に流量制御器により不活性ガスを導入して処理容器内を常圧に復帰させるようにした減圧熱処理装置であって、前記処理容器内の圧力を検出する圧力センサと、熱処理後に処理容器内に不活性ガスを導入して処理容器内を常圧に復帰させるときに処理容器内の圧力が加圧状態にならない不活性ガスの導入流量になるように前記流量制御器を制御する制御部とを備えたことを特徴とする。   In the invention according to claim 2, after the object to be processed is accommodated in the processing container and heat-treated in a predetermined reduced pressure atmosphere, an inert gas is introduced into the processing container by a flow rate controller, and the inside of the processing container is kept at normal pressure. And a pressure sensor for detecting the pressure in the processing container, and for introducing an inert gas into the processing container after the heat treatment to return the processing container to normal pressure. And a control unit that controls the flow rate controller so that the pressure in the processing vessel becomes an introduction flow rate of an inert gas that does not enter a pressurized state.

請求項3に係る発明は、請求項2記載の減圧熱処理装置において、前記制御部が、目標圧力値と検出圧力値を比較し、検出圧力値が目標圧力値に達しているときは現在の制御流量値をそのまま制御流量値とし、検出圧力値が目標圧力値に達していないときはその圧力差分より計算した値を制御流量値として出力するオートチューニング機能を備えていることを特徴とする。   The invention according to claim 3 is the reduced pressure heat treatment apparatus according to claim 2, wherein the control unit compares the target pressure value with the detected pressure value, and when the detected pressure value reaches the target pressure value, the current control is performed. The flow rate value is used as it is as a control flow rate value, and when the detected pressure value does not reach the target pressure value, an auto-tuning function that outputs a value calculated from the pressure difference as the control flow rate value is provided.

請求項1に係る発明によれば、処理容器内に被処理体を収容して所定の減圧雰囲気下で熱処理した後、処理容器内に流量制御器により不活性ガスを導入して処理容器内を常圧に復帰させる減圧熱処理装置の常圧復帰方法であって、前記処理容器内の圧力を検出し、該圧力が加圧状態にならないように流量制御器により不活性ガスの導入流量を制御するため、処理容器内を加圧状態にすることなく安定して迅速に常圧復帰させることができ、TATの短縮化が図れる。   According to the first aspect of the present invention, the object to be processed is accommodated in the processing container and heat-treated in a predetermined reduced-pressure atmosphere, and then an inert gas is introduced into the processing container by the flow rate controller. A method for returning to normal pressure by a reduced-pressure heat treatment apparatus that returns to normal pressure, wherein the pressure in the processing vessel is detected, and the flow rate of the inert gas is controlled by a flow rate controller so that the pressure does not become a pressurized state. Therefore, it is possible to return to normal pressure stably and quickly without bringing the inside of the processing container into a pressurized state, and TAT can be shortened.

請求項2に係る発明によれば、処理容器内に被処理体を収容して所定の減圧雰囲気下で熱処理した後、処理容器内に流量制御器により不活性ガスを導入して処理容器内を常圧に復帰させるようにした減圧熱処理装置であって、前記処理容器内の圧力を検出する圧力センサと、熱処理後に処理容器内に不活性ガスを導入して処理容器内を常圧に復帰させるときに処理容器内の圧力が加圧状態にならない不活性ガスの導入流量になるよう前記流量制御器を制御する制御部とを備えているため、処理容器内を加圧状態にすることなく安定して迅速に常圧復帰させることができ、TATの短縮化が図れる。   According to the invention of claim 2, after the object to be processed is accommodated in the processing container and heat-treated in a predetermined reduced pressure atmosphere, an inert gas is introduced into the processing container by the flow rate controller, and the inside of the processing container is filled. A reduced-pressure heat treatment apparatus configured to return to normal pressure, a pressure sensor that detects the pressure in the processing container, and an inert gas introduced into the processing container after the heat treatment to return the processing container to normal pressure Since there is a controller that controls the flow rate controller so that the pressure inside the processing vessel is an inert gas introduction flow rate that does not become a pressurized state, the processing vessel is stable without being pressurized. Thus, normal pressure can be quickly restored, and TAT can be shortened.

請求項3に係る発明によれば、前記制御部が目標圧力値と検出圧力値を比較し、検出圧力値が目標圧力値に達しているときは現在の制御流量値をそのまま制御流量値とし、検出圧力値が目標圧力値に達していないときはその圧力差分より計算した値を制御流量値として出力するオートチューニング機能を備えているため、処理容器の容積や、一次側からの不活性ガスの流入量に応じて短時間で最適値を求めることができ、処理容器内を迅速に常圧復帰させることができる。   According to the invention of claim 3, the control unit compares the target pressure value with the detected pressure value, and when the detected pressure value has reached the target pressure value, the current control flow value is used as it is as the control flow value, When the detected pressure value does not reach the target pressure value, it has an auto-tuning function that outputs the value calculated from the pressure difference as the control flow rate value, so the volume of the processing vessel and the inert gas from the primary side The optimum value can be obtained in a short time according to the inflow amount, and the inside of the processing container can be quickly returned to normal pressure.

以下に、本発明を実施するための最良の形態について、添付図面を基に詳述する。図1は本発明の実施の形態である減圧熱処理装置を概略的に示す図、図2は流量制御システムを説明するブロック図、図3は常圧復帰する場合の流量制御を説明するフローチャート図である
これらの図において、1は減圧熱処理装置として例示した縦型熱処理装置で、この縦型熱処理装置1は被処理体例えば半導体ウエハを収容して所定の減圧雰囲気下で熱処理するための熱処理炉を構成する例えば石英製の処理容器(反応管ともいう)2を備えている。処理容器2は例えば下端が炉口として開口された縦長円筒状に形成されている。処理容器2の周囲にはウエハを所定の温度例えば800〜1200℃程度に加熱するための加熱手段であるヒーター3が設けられている。
The best mode for carrying out the present invention will be described below in detail with reference to the accompanying drawings. FIG. 1 is a diagram schematically illustrating a reduced pressure heat treatment apparatus according to an embodiment of the present invention, FIG. 2 is a block diagram illustrating a flow rate control system, and FIG. 3 is a flowchart diagram illustrating flow rate control when normal pressure is restored. In these drawings, reference numeral 1 denotes a vertical heat treatment apparatus exemplified as a reduced pressure heat treatment apparatus. This vertical heat treatment apparatus 1 includes a heat treatment furnace for accommodating an object to be processed, for example, a semiconductor wafer, and performing heat treatment in a predetermined reduced pressure atmosphere. A processing vessel (also referred to as a reaction tube) 2 made of, for example, quartz is provided. For example, the processing container 2 is formed in a vertically long cylindrical shape having a lower end opened as a furnace port. Around the processing container 2, a heater 3 is provided as a heating means for heating the wafer to a predetermined temperature, for example, about 800 to 1200 ° C.

処理容器2の下方には、処理容器2の開口端である炉口を塞ぐ蓋体4が図示しない昇降機構により開閉可能すなわち昇降可能に設けられている。蓋体4の上部には多数枚のウエハを上下方向に所定間隔で多段に保持する例えば石英製のボート(図示省略)が設けられている。前記昇降機構によって、処理容器2に対するボートの搬入(ロード)、搬出(アンロード)及び蓋体4の開閉が行われるようになっている。   Below the processing container 2, a lid body 4 that closes the furnace port, which is the open end of the processing container 2, is provided so that it can be opened and closed by an elevator mechanism (not shown). An upper part of the lid 4 is provided with, for example, a quartz boat (not shown) that holds a large number of wafers in multiple stages at predetermined intervals in the vertical direction. By the elevating mechanism, the boat is carried in (loaded) and carried out (unloaded) from the processing container 2 and the lid 4 is opened and closed.

前記縦型熱処理装置1は、内部が清浄な雰囲気とされた筐体(図示省略)を備え、この筐体内の後部上方に前記処理容器2が設置されている。筐体内における処理容器2の下方はローディグエリア(作業領域)とされ、このローディングエリアには処理容器2内から搬出されたボートと運搬容器であるカセットとの間でウエハの移し替え(移載)を行うための移載機構が設けられている。   The vertical heat treatment apparatus 1 includes a casing (not shown) whose inside is a clean atmosphere, and the processing container 2 is installed above the rear part in the casing. Below the processing container 2 in the housing is a loading area (working area). In this loading area, wafers are transferred (transferred) between the boat unloaded from the processing container 2 and the cassette as the transport container. ) Is provided.

前記処理容器2には、処理容器2内に処理ガスや不活性ガス(例えばN)を導入するガス導入系としてのガス導入管5と、処理容器2内を減圧排気可能な排気系(主排気系)としての主排気管6とが接続されている。図示例では、処理容器2の下側部(例えばフランジ部)にガス導入管5を接続するガス導入口7が設けられ、処理容器2の頂部に主排気管6を接続する排気口8が設けられている。なお、処理容器2としては、上端が閉塞されており、下端の開口端に、ガス導入管を接続するガス導入口と、主排気管を接続する排気口とを有する円筒状のマニホールドが接続されたものであっても良い。 The processing container 2 includes a gas introduction pipe 5 as a gas introduction system for introducing a processing gas and an inert gas (for example, N 2 ) into the processing container 2, and an exhaust system (mainly capable of evacuating the processing container 2 under reduced pressure). A main exhaust pipe 6 as an exhaust system) is connected. In the illustrated example, a gas introduction port 7 for connecting the gas introduction pipe 5 is provided at the lower side (for example, flange portion) of the processing container 2, and an exhaust port 8 for connecting the main exhaust pipe 6 is provided at the top of the processing container 2. It has been. The processing vessel 2 is closed at the upper end, and a cylindrical manifold having a gas introduction port for connecting the gas introduction pipe and an exhaust port for connecting the main exhaust pipe is connected to the opening end of the lower end. It may be.

前記ガス導入口7及びガス導入管5は、例えばガス種に対応する数だけ設けられている。また、ガス導入管5にはガス流量を調節するための流量制御器(Mass Flow Controller、略してMFCともいう。)9が設けられ、この流量制御器9よりも上流には開閉弁10が設けられている。前記主排気管6の下流には、処理容器2内を例えば1×10−5Torr程度まで減圧排気可能な真空ポンプ11が設けられている。 The number of the gas introduction ports 7 and the gas introduction pipes 5 is provided in a number corresponding to, for example, the gas type. The gas introduction pipe 5 is provided with a flow rate controller (Mass Flow Controller, also referred to as MFC for short) 9 for adjusting the gas flow rate, and an on-off valve 10 is provided upstream of the flow rate controller 9. It has been. A vacuum pump 11 capable of evacuating the inside of the processing vessel 2 to about 1 × 10 −5 Torr, for example, is provided downstream of the main exhaust pipe 6.

主排気管6における真空ポンプ11よりも上流には排気圧力を調節するための主排気弁12が設けられ、この主排気弁12の前後を連通するように設けられた細径で排気流量の小さい副排気系としてのバイパス管13には排気圧力を調節するための副排気弁14が設けられている。主排気弁12の開操作による主排気減圧工程では例えば1×10−5Torr程度までの減圧が可能であり、副排気弁14の開操作による副排気減圧工程では例えば10Torr程度までの減圧が可能である。 A main exhaust valve 12 for adjusting the exhaust pressure is provided upstream of the vacuum pump 11 in the main exhaust pipe 6, and has a small diameter and a small exhaust flow rate so as to communicate with the front and rear of the main exhaust valve 12. A bypass pipe 13 serving as a secondary exhaust system is provided with a secondary exhaust valve 14 for adjusting the exhaust pressure. In the main exhaust pressure reducing step by opening the main exhaust valve 12, the pressure can be reduced to about 1 × 10 −5 Torr, and in the sub exhaust pressure reducing step by opening the sub exhaust valve 14, the pressure can be reduced to, for example, about 10 Torr. It is.

また、前記主排気管6における主排気弁12よりも上流には、処理容器2内を常圧ないし微減圧で排気するために工場排気系に接続された常圧排気系としての常圧排気管15が分岐接続されている。この常圧排気管15には常圧排気弁(ベントバルブ)16と、常圧排気管15側から主排気管6側への逆流を防止するための逆止弁17とが順に設けられている。処理容器2内の圧力を検出するために、処理容器2内と同じ減圧領域である主排気管6には圧力センサ18が設けられている。   Further, upstream of the main exhaust valve 12 in the main exhaust pipe 6, a normal pressure exhaust pipe 15 as a normal pressure exhaust system connected to a factory exhaust system in order to exhaust the inside of the processing vessel 2 at normal pressure or slightly reduced pressure. Is branched. The normal pressure exhaust pipe 15 is provided with a normal pressure exhaust valve (vent valve) 16 and a check valve 17 for preventing a back flow from the normal pressure exhaust pipe 15 side to the main exhaust pipe 6 side. In order to detect the pressure in the processing container 2, a pressure sensor 18 is provided in the main exhaust pipe 6, which is the same decompression region as in the processing container 2.

前記主排気弁12、副排気弁14、開閉弁16は制御部(コントローラ)19によって開閉制御されるようになっている。処理容器2内を所定の圧力まで真空引きする場合には、先ず開閉弁10、主排気弁12及び常圧排気弁16を閉じ、副排気弁14を開けて小流量のスロー排気による予備真空引きを行い、次いで副排気弁12を閉じ、主排気弁12を開いて所定の真空度になるまで本真空引きを行い、この真空度を維持しつつ所定の処理ガスを所定の流量で処理容器内に導入することにより所定の熱処理例えばCVD処理を行う。熱処理が終了したら、主開閉弁12を閉じる。   The main exhaust valve 12, the sub exhaust valve 14, and the opening / closing valve 16 are controlled to be opened / closed by a control unit (controller) 19. When evacuating the inside of the processing container 2 to a predetermined pressure, first, the on-off valve 10, the main exhaust valve 12 and the normal pressure exhaust valve 16 are closed, and the auxiliary exhaust valve 14 is opened to perform preliminary evacuation by slow exhaust at a low flow rate. Next, the sub exhaust valve 12 is closed, the main exhaust valve 12 is opened, and the main vacuum is drawn until a predetermined degree of vacuum is reached, and a predetermined processing gas is supplied into the processing container at a predetermined flow rate while maintaining the degree of vacuum. A predetermined heat treatment, for example, a CVD process is performed by introducing into the above. When the heat treatment is finished, the main on-off valve 12 is closed.

熱処理後(プロセス終了後)、処理容器2内に不活性ガス例えばNを導入して常圧に復帰させるときに、圧力センサ18で検出される圧力が加圧状態(例えば大気圧:760Torrを超える状態)にならない不活性ガスの導入流量になるよう前記流量制御器9を制御部(コントローラ)19によって制御するように構成されている。この場合、常圧排気弁16又は副排気弁14を開いておき、常圧排気又は低減圧排気を行い、処理容器2内に残存する処理ガスを掃気して処理容器2内を不活性ガス例えばNでパージする。 After heat treatment (after completion of the process), when an inert gas such as N 2 is introduced into the processing vessel 2 to return to normal pressure, the pressure detected by the pressure sensor 18 is in a pressurized state (for example, atmospheric pressure: 760 Torr). The flow rate controller 9 is controlled by a control unit (controller) 19 so that the flow rate of the inert gas is not increased. In this case, the normal pressure exhaust valve 16 or the sub exhaust valve 14 is opened, normal pressure exhaust or reduced pressure exhaust is performed, the processing gas remaining in the processing container 2 is scavenged, and the inside of the processing container 2 is inert gas, for example, Purge with N 2 .

処理容器2内に不活性ガスを導入する場合、TATの短縮化のために、大流量例えば500〜1000リットル/分で導入することが好ましい。また、処理容器2の容積や、一次側からの不活性ガス例えばNの流入量に応じて短時間で最適値を求め、処理容器2内を迅速に常圧復帰させるために、前記制御部19は、設定値である目標圧力値(例えば大気圧:760Torr)と検出値である現在圧力値を比較し、現在圧力値が目標圧力値に達しているときは現在の制御流量値をそのまま制御流量値とし、現在圧力値が目標圧力値に達していないときはその圧力差分より計算した値を制御流量値として出力するオートチューニング機能を備えていることが好ましい。このオートチューニングの手法としては、いわゆるリミットサイクル法やPID法が用いられる。 When the inert gas is introduced into the processing container 2, it is preferably introduced at a large flow rate, for example, 500 to 1000 liters / minute in order to shorten TAT. In addition, in order to obtain the optimum value in a short time according to the volume of the processing container 2 and the inflow amount of the inert gas such as N 2 from the primary side, the control unit 19 compares a target pressure value (for example, atmospheric pressure: 760 Torr) that is a set value with a current pressure value that is a detected value, and when the current pressure value has reached the target pressure value, the current control flow value is directly controlled. It is preferable to have an auto-tuning function that outputs a value calculated from the pressure difference as a control flow value when the current pressure value does not reach the target pressure value. As this auto-tuning method, a so-called limit cycle method or PID method is used.

減圧状態から常圧(大気圧)状態に戻すときに減圧領域である処理容器2内に不活性ガス例えばN2を導入して圧力を制御する圧力制御方法ないし圧力制御システムにおいては、制御部19において、図3に示すように、圧力制御処理を開始する(S1)と、目標圧力値の取得(S2)、制御流量値の取得(S3)、現在圧力値の取得(S4)を順に行った後、現在圧力値が目標圧力値に達したか否かを比較し(S5)、達した場合は現在の制御流量値をそのまま制御流量値とし(S6)、達しない場合はその圧力差分より計算した値を制御流量値とし(S7)、最適な制御流量値を出力して(S8)、流量制御器9を制御するようになっている。なお、現在圧力値が目標圧力値(例えば大気圧)に達した場合には、処理容器2内が常圧に復帰しているので、開閉弁10、常圧排気弁16、副排気弁14を閉じて常圧復帰工程を終了し、蓋体4を降下してボートを搬出すれば良い。   In the pressure control method or pressure control system for controlling the pressure by introducing an inert gas such as N 2 into the processing vessel 2 which is the decompression region when returning from the decompressed state to the normal pressure (atmospheric pressure) state, As shown in FIG. 3, after the pressure control process is started (S1), the target pressure value is acquired (S2), the control flow value is acquired (S3), and the current pressure value is acquired (S4) in this order. Then, it is compared whether or not the current pressure value has reached the target pressure value (S5). If the current pressure value has been reached, the current control flow value is used as the control flow value as it is (S6). The value is set as a control flow rate value (S7), and an optimal control flow rate value is output (S8) to control the flow rate controller 9. Note that when the current pressure value reaches a target pressure value (for example, atmospheric pressure), the inside of the processing vessel 2 has returned to normal pressure, so the on-off valve 10, the normal pressure exhaust valve 16, and the sub exhaust valve 14 are turned on. The normal pressure return process is closed to close, and the lid 4 is lowered to carry out the boat.

前記制御部19は、図2に示すように比較演算を行う中央処理装置(CPU)20を有し、この中央処理装置20には目標圧力値の設定等の各種設定値及び現在値の入出力を行う例えばタッチパネル式の入出力表示装置であるMMI(Man Machine Interface)21が接続されている。中央処理装置20には圧力センサ18からの出力値である現在圧力値と流量制御器9からの出力値である現在流量値がA/D変換されて取り込まれ(入力され)、中央処理装置20で比較演算処理されて算出された制御流量値がD/A変換されて流量制御器9に出力されるようになっている。   As shown in FIG. 2, the control unit 19 has a central processing unit (CPU) 20 that performs a comparison operation. The central processing unit 20 inputs and outputs various set values such as a target pressure value and current values. For example, an MMI (Man Machine Interface) 21 which is a touch panel type input / output display device is connected. The central processing unit 20 captures (inputs) the current pressure value, which is the output value from the pressure sensor 18, and the current flow value, which is the output value from the flow rate controller 9, after A / D conversion. Thus, the control flow rate value calculated by the comparison calculation process is D / A converted and output to the flow rate controller 9.

以上構成からなる縦型熱処理装置1の常圧復帰方法によれば、処理容器2内にウエハを収容して所定の減圧雰囲気下で熱処理した後、処理容器2内に流量制御器9により不活性ガスを導入して処理容器2内を常圧に復帰させる減圧熱処理装置1の常圧復帰方法であって、前記処理容器2内の圧力を検出し、該圧力が加圧状態にならないように流量制御器9により不活性ガスの導入流量を制御するため、処理容器2内を加圧状態にすることなく安定して迅速に常圧復帰させることができ、TATの短縮化が図れる。   According to the normal pressure recovery method of the vertical heat treatment apparatus 1 having the above-described configuration, the wafer is accommodated in the processing vessel 2 and heat-treated in a predetermined reduced pressure atmosphere, and then the processing vessel 2 is inactivated by the flow rate controller 9. A method for restoring normal pressure of the reduced pressure heat treatment apparatus 1 for introducing a gas to restore the inside of the processing vessel 2 to normal pressure, wherein the pressure in the processing vessel 2 is detected and the flow rate is set so that the pressure does not become a pressurized state. Since the introduction flow rate of the inert gas is controlled by the controller 9, the process vessel 2 can be stably and quickly returned to normal pressure without being in a pressurized state, and TAT can be shortened.

また、縦型熱処理装置1によれば、処理容器2内にウエハを収容して所定の減圧雰囲気下で熱処理した後、処理容器2内に流量制御器9により不活性ガスを導入して処理容器2内を常圧に復帰させるようにした減圧熱処理装置1であって、前記処理容器2内の圧力を検出する圧力センサ28と、熱処理後に処理容器2内に不活性ガスを導入して処理容器2内を常圧に復帰させるときに処理容器2内の圧力が加圧状態にならない不活性ガスの導入流量になるように前記流量制御器9を制御する制御部19とを備えているため、処理容器2内を加圧状態にすることなく安定して迅速に常圧復帰させることができ、TATの短縮化が図れる。   Further, according to the vertical heat treatment apparatus 1, a wafer is accommodated in the processing container 2 and heat-treated in a predetermined reduced pressure atmosphere, and then an inert gas is introduced into the processing container 2 by the flow rate controller 9. 2 is a reduced pressure heat treatment apparatus 1 for returning the inside to normal pressure, and a pressure sensor 28 for detecting the pressure in the processing vessel 2 and an inert gas introduced into the processing vessel 2 after the heat treatment. 2 is provided with a control unit 19 that controls the flow rate controller 9 so that the pressure in the processing vessel 2 becomes a pressurized flow rate of an inert gas that does not enter a pressurized state when the inside is returned to normal pressure. Without bringing the inside of the processing container 2 into a pressurized state, the normal pressure can be stably and promptly restored, and TAT can be shortened.

更に、前記制御部19が目標圧力値と検出圧力値を比較し、検出圧力値が目標圧力値に達しているときは現在の制御流量値をそのまま制御流量値とし、検出圧力値が目標圧力値に達していないときはその圧力差分より計算した値を制御流量値として出力するオートチューニング機能を備えているため、処理容器2の容積や、一次側からの不活性ガスの流入量に応じて短時間で最適値を求めることができ、処理容器2内を迅速に常圧復帰させることができる。   Further, the control unit 19 compares the target pressure value with the detected pressure value, and when the detected pressure value has reached the target pressure value, the current control flow value is used as the control flow value, and the detected pressure value is the target pressure value. Since it has an auto-tuning function that outputs a value calculated from the pressure difference as a control flow rate value when the pressure does not reach, the flow rate is short depending on the volume of the processing vessel 2 and the inflow amount of the inert gas from the primary side. The optimum value can be obtained over time, and the inside of the processing container 2 can be quickly returned to normal pressure.

以上、本発明の実施の形態ないし実施例を図面により詳述してきたが、本発明は前記実施の形態ないし実施例に限定されるものではなく、本発明の要旨を逸脱しない範囲での種々の設計変更等が可能である。不活性ガスとしては、アルゴンガスやヘリウムガスであっても良い。減圧熱処理装置としては、横型熱処理装置であっても良く、また、バッチ式に限らず、枚様式であっても良い。   As mentioned above, although embodiment thru | or example of this invention has been explained in full detail with drawing, this invention is not limited to the said embodiment thru | or example, Various in the range which does not deviate from the summary of this invention. Design changes can be made. The inert gas may be argon gas or helium gas. The vacuum heat treatment apparatus may be a horizontal heat treatment apparatus, and is not limited to a batch type, but may be a sheet type.

本発明の実施の形態である減圧熱処理装置を概略的に示す図である。1 is a diagram schematically showing a reduced pressure heat treatment apparatus according to an embodiment of the present invention. 流量制御システムを説明するブロック図である。It is a block diagram explaining a flow control system. 常圧復帰する場合の流量制御を説明するフローチャート図である。It is a flowchart explaining the flow control in the case of returning to normal pressure.

符号の説明Explanation of symbols

1 縦型熱処理装置(減圧熱処理装置)
2 処理容器
5 ガス導入管(ガス導入系)
6 主排気管(排気系)
9 流量制御器
18 圧力センサ
19 制御部
1 Vertical heat treatment equipment (reduced pressure heat treatment equipment)
2 Processing vessel 5 Gas introduction pipe (gas introduction system)
6 Main exhaust pipe (exhaust system)
9 Flow controller 18 Pressure sensor 19 Control unit

Claims (3)

処理容器内に被処理体を収容して所定の減圧雰囲気下で熱処理した後、処理容器内に流量制御器により不活性ガスを導入して処理容器内を常圧に復帰させる減圧熱処理装置の常圧復帰方法であって、前記処理容器内の圧力を検出し、該圧力が加圧状態にならないように流量制御器により不活性ガスの導入流量を制御することを特徴とする減圧熱処理装置の常圧復帰方法。   After the object to be processed is stored in the processing container and heat-treated in a predetermined reduced-pressure atmosphere, an inert gas is introduced into the processing container by a flow controller to return the processing container to normal pressure. The pressure recovery method is characterized in that the pressure in the processing vessel is detected, and the flow rate of the inert gas is controlled by a flow rate controller so that the pressure does not enter a pressurized state. Pressure recovery method. 処理容器内に被処理体を収容して所定の減圧雰囲気下で熱処理した後、処理容器内に流量制御器により不活性ガスを導入して処理容器内を常圧に復帰させるようにした減圧熱処理装置であって、前記処理容器内の圧力を検出する圧力センサと、熱処理後に処理容器内に不活性ガスを導入して処理容器内を常圧に復帰させるときに処理容器内の圧力が加圧状態にならない不活性ガスの導入流量になるように前記流量制御器を制御する制御部とを備えたことを特徴とする減圧熱処理装置。   Low-pressure heat treatment in which an object to be processed is stored in a processing container and heat-treated in a predetermined reduced-pressure atmosphere, and then an inert gas is introduced into the processing container by a flow controller so that the inside of the processing container is returned to normal pressure. A pressure sensor for detecting the pressure in the processing container, and the pressure in the processing container is increased when an inert gas is introduced into the processing container after the heat treatment to return the processing container to normal pressure. A reduced-pressure heat treatment apparatus comprising: a control unit that controls the flow rate controller so that the flow rate of the inert gas that does not enter a state is reached. 前記制御部は、目標圧力値と検出圧力値を比較し、検出圧力値が目標圧力値に達しているときは現在の制御流量値をそのまま流量制御値とし、検出圧力値が目標圧力値に達していないときはその圧力差分より計算した値を制御流量値として出力するオートチューニング機能を備えていることを特徴とする請求項2記載の減圧熱処理装置。
The control unit compares the target pressure value with the detected pressure value, and when the detected pressure value has reached the target pressure value, the current control flow value is used as the flow control value as it is, and the detected pressure value reaches the target pressure value. 3. A reduced pressure heat treatment apparatus according to claim 2, further comprising an auto-tuning function for outputting a value calculated from the pressure difference as a control flow rate value when not.
JP2004215179A 2004-07-23 2004-07-23 Reduced pressure heat treatment apparatus and method of restoration to normal pressure of the apparatus Pending JP2006040990A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009534867A (en) * 2006-04-24 2009-09-24 アクセリス テクノロジーズ, インコーポレイテッド Load lock control
CN109559966A (en) * 2017-09-27 2019-04-02 北京北方华创微电子装备有限公司 Accelerate the cleaning method that processing chamber is answered a pager's call

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009534867A (en) * 2006-04-24 2009-09-24 アクセリス テクノロジーズ, インコーポレイテッド Load lock control
CN109559966A (en) * 2017-09-27 2019-04-02 北京北方华创微电子装备有限公司 Accelerate the cleaning method that processing chamber is answered a pager's call

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