JP2885142B2 - Vacuum processing apparatus and method for detecting atmospheric contamination in vacuum processing apparatus - Google Patents

Vacuum processing apparatus and method for detecting atmospheric contamination in vacuum processing apparatus

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Publication number
JP2885142B2
JP2885142B2 JP7208899A JP20889995A JP2885142B2 JP 2885142 B2 JP2885142 B2 JP 2885142B2 JP 7208899 A JP7208899 A JP 7208899A JP 20889995 A JP20889995 A JP 20889995A JP 2885142 B2 JP2885142 B2 JP 2885142B2
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JP
Japan
Prior art keywords
gas
shutoff valve
vacuum processing
automatic shutoff
mass flow
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 - Lifetime
Application number
JP7208899A
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Japanese (ja)
Other versions
JPH0955369A (en
Inventor
浩 松村
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.)
NEC Corp
Original Assignee
Nippon Electric Co Ltd
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Filing date
Publication date
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Priority to JP7208899A priority Critical patent/JP2885142B2/en
Publication of JPH0955369A publication Critical patent/JPH0955369A/en
Application granted granted Critical
Publication of JP2885142B2 publication Critical patent/JP2885142B2/en
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Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は半導体装置の製造工
程に用いられるドライエッチング装置等の真空処理装置
及び真空処理装置への大気混入の検知方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vacuum processing apparatus such as a dry etching apparatus used in a manufacturing process of a semiconductor device, and a method for detecting atmospheric contamination in the vacuum processing apparatus.

【0002】[0002]

【従来の技術】従来の真空処理装置は、図5に示すよう
に、真空処理を行う真空処理室6と、例えば危険ガスが
貯蔵されているガスシリンダ9と、このガスシリンダ9
に順次接続された一次側ガス配管15Aと、ガス質量流
量制御器16と二次側ガス配管13Aと、ガスシリンダ
収納容器8とガス配管収納容器14と、これらの収納容
器に接続されたガス漏洩検知器11と、この検知器11
と連動する自動遮断弁12とから主に構成されている。
このような真空処理装置は、例えば特開昭61−189
641号公報に記載されている。
2. Description of the Related Art As shown in FIG. 5, a conventional vacuum processing apparatus includes a vacuum processing chamber 6 for performing vacuum processing, a gas cylinder 9 for storing, for example, a dangerous gas, and a gas cylinder 9 for storing the dangerous gas.
, A gas mass flow controller 16, a secondary gas pipe 13A, a gas cylinder storage container 8, a gas pipe storage container 14, and a gas leak connected to these storage containers. Detector 11 and this detector 11
And an automatic shut-off valve 12 interlocked with the automatic shut-off valve 12.
Such a vacuum processing apparatus is disclosed in, for example, JP-A-61-189.
No. 641.

【0003】次に、この真空処理装置をドライエッチン
グ装置とした場合についてその動作を説明する。ガスシ
リンダ9から供給されるガスは、一次側ガス配管15A
を通り、ガス質量流量制御器16によりガス流量を一定
に制御されて二次側ガス配管13Aを通り真空処理室6
に導入され、所要の処理圧力に保たれながら高周波電力
により励起されてプラズマ化し、被処理物のエッチング
を行う、ガスシリンダ9はガスシリンダ収納容器8に又
一次側ガス配管15Aはガス配管収納容器14にそれぞ
れ収納され、ガス漏洩検知器11によりガスシリンダ収
納容器8及びガス配管収納容器14内で発生するガス漏
洩の有無をモニタする。ガス漏洩検知器11がガス漏洩
を検知したとき、ガス漏洩警報信号を発して自動遮断弁
12を閉じガスシリンダ9からの危険ガスの供給を停止
することにより、ガスシリンダ収納容器8及び、ガス配
管収納容器14からのガス漏洩を抑え人体への危険性を
回避する。
[0003] Next, the operation of the case where the vacuum processing apparatus is a dry etching apparatus will be described. The gas supplied from the gas cylinder 9 is a primary gas pipe 15A.
, The gas flow rate is controlled to be constant by the gas mass flow controller 16, and the gas flows through the
The gas cylinder 9 is in a gas cylinder storage container 8 and the primary gas pipe 15A is in a gas pipe storage container. The gas leakage detector 11 monitors the presence or absence of gas leakage occurring in the gas cylinder storage container 8 and the gas pipe storage container 14. When the gas leak detector 11 detects a gas leak, it issues a gas leak alarm signal and closes the automatic shutoff valve 12 to stop the supply of dangerous gas from the gas cylinder 9, so that the gas cylinder storage container 8 and the gas pipe Gas leakage from the storage container 14 is suppressed to avoid danger to the human body.

【0004】[0004]

【発明が解決しようとする課題】この従来の真空処理装
置では、ガス漏洩検知器を用いてガスシリンダ収納容器
及びガス配管収納容器からのガス漏洩のみを検知してい
るために、大気圧よりも低圧になっているガス質量流量
制御器の二次側ガス配管への大気成分の混入については
検知できない。その結果、所定のガス種及びガス流量が
得られず処理不良を生じさせ半導体装置の歩留りを低下
させるという問題があった。
In this conventional vacuum processing apparatus, since only gas leakage from the gas cylinder storage container and the gas pipe storage container is detected using the gas leakage detector, the pressure is lower than the atmospheric pressure. Atmospheric components cannot be detected in the secondary gas pipe of the low-pressure gas mass flow controller. As a result, there is a problem that a predetermined gas type and a gas flow rate cannot be obtained, processing defects occur, and the yield of semiconductor devices decreases.

【0005】本発明の目的は、ガス配管で生じる大気混
入を検知し、被処理物の処理不良を防止できる真空処理
装置及び真空処理装置への大気混入の検知方法を提供す
ることにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a vacuum processing apparatus and a method for detecting air mixing in a vacuum processing apparatus, which can detect air entrapment generated in a gas pipe and prevent processing defects of an object to be processed.

【0006】[0006]

【課題を解決するための手段】第1の発明の真空処理装
置は、ガスシリンダに順次接続された一次側自動遮断弁
と質量流量制御器と二次側自動遮断弁とからなる複数組
のガスラインと、前記ガスラインの各前記二次側自動遮
断弁に一端が接続され他端が一系統にまとめられたガス
配管と、このガス配管に接続された最終自動遮断弁と、
この最終自動遮断弁に接続された質量流量計と、この質
量流量計に接続された真空処理室と、前記質量流量計に
接続され複数組の前記ガスラインを流れる処理ガスの総
設定流量の値を記憶しこの設定値と前記質量流量計の測
定値とを比較し測定値が設定値より大きい場合は警報を
発生すると共に前記一次側自動遮断弁と前記二次側自動
遮断弁を閉る為の信号を送出する検知制御手段とを含む
ことを特徴とするものであり、又この検知制御手段は、
一次側自動遮断弁又は二次側自動遮断弁又は最終自動遮
断弁を閉じて、真空処理室を真空引きした時に、質量流
量計に設定値以上のガスが流れた場合警報を発生する機
能を合せ持つものである。
According to a first aspect of the present invention, there is provided a vacuum processing apparatus comprising a plurality of sets of gas comprising a primary automatic shutoff valve, a mass flow controller, and a secondary automatic shutoff valve which are sequentially connected to a gas cylinder. Line, a gas pipe having one end connected to each of the secondary-side automatic shut-off valves of the gas line and the other end integrated into one system, and a final automatic shut-off valve connected to the gas pipe,
A mass flow meter connected to the final automatic shut-off valve, a vacuum processing chamber connected to the mass flow meter, and a value of a total set flow rate of the processing gas flowing through a plurality of sets of the gas lines connected to the mass flow meter. The set value is compared with the measured value of the mass flow meter. If the measured value is larger than the set value, an alarm is generated and the primary automatic shutoff valve and the secondary automatic shutoff valve are closed. And a detection control means for transmitting a signal of
When the primary automatic shut-off valve, secondary automatic shut-off valve or final automatic shut-off valve is closed and the vacuum processing chamber is evacuated, an alarm is generated when gas exceeding the set value flows to the mass flow meter. Have.

【0007】第2の発明の真空処理装置への大気混入の
検査方法は、第1の発明の真空処理装置を用い、各ライ
ンの自動遮断弁の少くとも1つを閉めて真空処理室を真
空引きし、この時質量流量計に流れるガス量を所定値と
比較し、多い場合は警報を発生させるものである。
According to a second aspect of the present invention, there is provided a method for inspecting air in a vacuum processing apparatus using the vacuum processing apparatus according to the first invention, wherein at least one of the automatic shutoff valves of each line is closed to evacuate the vacuum processing chamber. At this time, the amount of gas flowing through the mass flow meter is compared with a predetermined value, and if it is large, an alarm is generated.

【0008】[0008]

【発明の実施の形態】次に本発明について図面を参照し
て説明する。図1は本発明の第1の実施の形態を説明す
る為の真空処理装置の構成図である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Next, the present invention will be described with reference to the drawings. FIG. 1 is a configuration diagram of a vacuum processing apparatus for explaining a first embodiment of the present invention.

【0009】図1において真空処理装置は、一次側ガス
配管15によりガスシリンダ9に順次接続された一次側
自動遮断弁1と質量流量制御器2と二次側自動遮断弁3
からなる複数組のガスライン(ガス−1〜ガス−N)
と、この各ガスラインの二次側自動遮断弁3に一端が接
続され他端が一系統にまとめられた二次側ガス配管13
と、この二次側ガス配管13に順次接続された最終自動
遮断弁4と質量流量計5と真空処理室6と、この質量流
量計5に接続され複数組のガスラインを流れる処理ガス
の総設定流量の値を記憶しこの設定値と質量流量計の測
定値とを比較し測定値が設定値より大きい場合はブザー
や表示等で警報を発生すると共に、一次側遮断弁1と質
量流量制御器2と二次側自動遮断弁3を閉じる為の信号
を送出する検知制御部7とから主に構成されている。こ
の検知制御部はメモリー、比較回路、CPU等から構成
されており、一次側自動遮断弁1又は二次側自動遮断弁
3又は最終自動遮断弁4を閉じて真空処理室6を真空引
きした時に、質量流量計5に設定値以上のガスが流れた
場合警報を発生する機能をも合せ持っている。尚、図1
において8はガスシリンダ収納容器,10は減圧弁,1
1はガス漏洩検知器,12は自動遮断弁である。
In FIG. 1, the vacuum processing apparatus includes a primary automatic gas shutoff valve 1, a mass flow controller 2, and a secondary automatic shutoff valve 3, which are sequentially connected to a gas cylinder 9 by a primary gas pipe 15.
Sets of gas lines (gas-1 to gas-N)
And a secondary gas pipe 13 having one end connected to the secondary automatic shutoff valve 3 of each gas line and the other end integrated into one system.
And a final automatic shut-off valve 4, a mass flow meter 5, and a vacuum processing chamber 6, which are sequentially connected to the secondary gas pipe 13, and a total of processing gases connected to the mass flow meter 5 and flowing through a plurality of sets of gas lines. The set flow rate value is stored and the set value is compared with the measured value of the mass flow meter. If the measured value is larger than the set value, an alarm is generated by a buzzer, display, etc., and the primary side shutoff valve 1 and the mass flow control It mainly comprises a detector 2 and a detection controller 7 for sending a signal for closing the secondary-side automatic shutoff valve 3. This detection control unit is composed of a memory, a comparison circuit, a CPU, and the like. Also, it has a function of generating an alarm when gas exceeding a set value flows through the mass flow meter 5. FIG.
, 8 is a gas cylinder storage container, 10 is a pressure reducing valve, 1
1 is a gas leak detector and 12 is an automatic shutoff valve.

【0010】次にこのように構成された真空処理装置の
動作について説明する。図2は本発明の第2の実施の形
態の大気混入の検知方法を説明する為の動作フローチャ
ートである。以下図1と併用して説明する。
Next, the operation of the vacuum processing apparatus configured as described above will be described. FIG. 2 is an operation flowchart for explaining a method for detecting atmospheric contamination according to the second embodiment of the present invention. This will be described below in conjunction with FIG.

【0011】まず図2のステップ1(S−1と記す、続
くステップも同様にS−(n)と記す)において、全ラ
インに流すガスのN2 流量換算係数CF,設定流量Q
set 及び許容誤差dを検知制御部7に入力する。そして
ガスシリンダ9より減圧弁10により減圧されたガスを
各ラインに供給する。次にS−2において、各ラインの
一時側自動遮断弁(V1st )1を開き、ガス毎に校正さ
れた質量流量制御器2で設定流量Qset に制御させ、二
次側自動遮断弁(V2nd )3を開き、更に最終自動遮断
弁(VF )4を開くことにより、ガスはN2 ガスにて校
正された質量流量計5へ導入される。次にS−3におい
て、このとき質量流量計5での観測値QTが検知制御部
7に送られる。検知制御部7は、全ガスをN2 流量換算
した総和に対して許容誤差d以下か否かの判断を行い、
許容誤差d以下の場合には真空処理室6においてS−4
のプラズマ処理を行い、例えばAl膜のドライエッチン
グを行う。また許容誤差dを超える場合には、検知制御
部7はS−6において「異常流量検出」すなわち大気混
入検知の警報を発する。どちらの処理を行ってもS−5
において全一次側自動遮断弁1、全質量流量計2、全二
次側自動遮断弁3および最終自動遮断弁4を閉じ終了す
る。
First, in step 1 of FIG. 2 (referred to as S-1 and subsequent steps also referred to as S- (n)), the N 2 flow rate conversion coefficient CF and the set flow rate Q
The set and the allowable error d are input to the detection control unit 7. The gas decompressed by the pressure reducing valve 10 from the gas cylinder 9 is supplied to each line. Next, in S-2, the temporary-side automatic shutoff valve (V 1st ) 1 of each line is opened, and the mass flow controller 2 calibrated for each gas controls the set flow rate Qset to set the secondary-side automatic shutoff valve (V 1st ). By opening V 2nd ) 3 and further opening the final automatic shut-off valve (V F ) 4, the gas is introduced into the mass flow meter 5 calibrated with N 2 gas. Next, in S-3, the observed value Q T of a mass flow meter 5 this time is sent to the detection control unit 7. The detection control unit 7 determines whether or not the total sum of all the gases converted into the N 2 flow rate is equal to or less than an allowable error d,
If the error is equal to or smaller than the allowable error d, the vacuum processing chamber 6 performs S-4.
Is performed, for example, dry etching of an Al film is performed. If the error d exceeds the allowable error d, the detection controller 7 issues an "abnormal flow rate detection" alarm in S-6, that is, a warning of detection of air contamination. Whichever processing is performed, S-5
At, all the primary-side automatic shut-off valves 1, all the mass flow meters 2, all the secondary-side automatic shut-off valves 3, and the final automatic shut-off valve 4 are closed and finished.

【0012】次に具体的に説明する。ここで、ガス−1
=Cl2 ,ガス−2=BCl3 ,ガス−3=N2 で設定
流量がそれぞれ50、200、20sccm、N2 換算
係数がそれぞれ0.86、0.40、1.0とS−1で
入力された場合、ガス配管系が正常なとき真空処理室6
へ導入される混合ガスのN2 換算流量は Σ(QSET (n)CF(n))=50×0.86+20
0×0.40+20×1.0=143.0sccm である。
Next, a specific description will be given. Here, gas-1
= Cl 2 , gas-2 = BCl 3 , gas-3 = N 2 , set flow rates are 50, 200, 20 sccm, respectively, and N 2 conversion coefficients are 0.86, 0.40, 1.0, and S-1, respectively. When input, the vacuum processing chamber 6 when the gas piping system is normal
N 2 -converted flow rate of the mixed gas introduced into へ is (Q SET (n) CF (n)) = 50 × 0.86 + 20
0 × 0.40 + 20 × 1.0 = 143.0 sccm.

【0013】このとき、質量流量制御器2から質量流量
計5までのガス配管に、5sccmの空気が混入した場
合、空気のN2 換算係数が1.10であることから質量
流量計5で観測されるQT は QT =143+5×1.10=148.5sccm と観測される。このときの許容誤差d=2%とS−1で
予め設定している場合S−3で|ΔQ|=|〔(14
8.5−143)/143〕|×100=3.8>2
(%)となり、S−6で「異常流量検出」警報を発して
終了となる。
At this time, when 5 sccm of air is mixed in the gas pipe from the mass flow controller 2 to the mass flow meter 5, the N 2 conversion coefficient of the air is 1.10, so that the mass flow meter 5 The observed Q T is observed as Q T = 143 + 5 × 1.10 = 148.5 sccm. In this case, when the allowable error d = 2% and S-1 are set in advance, | ΔQ | = | [(14
8.5-143) / 143] | × 100 = 3.8> 2
(%), An "abnormal flow rate detection" alarm is issued in S-6, and the process ends.

【0014】また、あるガスの質量流量制御器2が設定
した流量通りに制御できない場合、例えばCl2 ガスが
設定流量50sccmに対して55sccmと誤制御さ
れたとき、質量流量計5でQT は55×0.86+20
0×0.40+20×1.0=147.3sccmを観
測するから、誤差ΔQはS−3で |ΔQ|=|〔(147.3+143)/143〕|×
100=3.0>2(%) となり、S−6で「異常流量検出」警報を発して停止と
なる。
If the mass flow controller 2 cannot control the gas at the set flow rate, for example, if the Cl 2 gas is erroneously controlled to 55 sccm with respect to the set flow rate of 50 sccm, the mass flow meter 5 sets Q T to 55 × 0.86 + 20
Since 0 × 0.40 + 20 × 1.0 = 147.3 sccm is observed, the error ΔQ is S−3, and | ΔQ | = | [(147.3 + 143) / 143] | ×
100 = 3.0> 2 (%), and an abnormal flow rate detection alarm is issued in S-6 to stop.

【0015】次に本発明の第3の実施の形態としてライ
ンの途中における大気混入の検知方法について説明す
る。図3は本発明の第3の実施の形態を説明する為の動
作フローチャートである。
Next, as a third embodiment of the present invention, a method of detecting air entrapment in the middle of a line will be described. FIG. 3 is an operation flowchart for explaining the third embodiment of the present invention.

【0016】まず図3のS−11において、全一次側自
動遮断弁1,全質量流量制御器2,全二次側自動遮断弁
3および最終自動遮断弁4を閉じた状態で、最終自動遮
断弁4から真空処理室6内までを充分真空排気し、S−
12でこのときの質量流量計5の観測値QT が設定値、
たとえば0sccmより大きい場合にはS−17で「最
終自動遮断弁4から質量流量計5の間での大気漏洩検
知」警報を発し終了する。S−12で質量流量計5の観
測値QT が0sccmの場合は、S−13で最終自動遮
断弁4を開けた状態で充分真空排気し、S−14でこの
ときの質量流量計5の観測値QT が0sccmより大き
い場合にはS−18で「二次側自動遮断弁3から最終自
動遮断弁4の間での大気漏洩検知」警報を発し終了す
る。
First, in step S-11 in FIG. 3, the final automatic shutoff is performed with all the primary automatic shutoff valves 1, all mass flow controllers 2, all secondary automatic shutoff valves 3 and final automatic shutoff valve 4 closed. The space from the valve 4 to the inside of the vacuum processing chamber 6 is sufficiently evacuated, and S-
At 12, the observed value Q T of the mass flow meter 5 at this time is the set value,
For example, if it is greater than 0 sccm, a warning is issued in S-17, "Detection of atmospheric leakage between final automatic shutoff valve 4 and mass flow meter 5", and the process ends. If the observed value Q T of the mass flow meter 5 at S-12 is 0 sccm, sufficiently evacuated while opening the final automatic shut-off valve 4 in S-13, S-14 at a mass flow meter 5 at this time observations Q T is the case 0sccm larger ends an alarm "air leakage detection in between the secondary side automatic shut-off valve 3 in the final automatic shut-off valve 4" in S-18.

【0017】S−14で質量流量計5の観測値QT が0
sccmの場合は、S−15で全ての質量流量制御器2
と二次側自動遮断弁3を開けた状態で充分真空排気し、
S−16でこのときの質量流量計5の観測値QT が0s
ccmより大きい場合にはS−19で「一次側自動遮断
弁1と二次側自動遮断弁3の間で大気漏洩検知」警報を
発し、S−20で一度全ての質量流量制御器2と二次側
自動遮断弁3を閉じる。そして、S−22でまずガス−
1の質量流量制御器2と二次側自動遮断弁3を開き充分
真空排気し、S−23でこのとき質量流量計5の観測値
T が0sccmより大きい場合にはS−25で「ガス
−1の一次側自動遮断弁1と二次側自動遮断弁3の間で
大気漏洩検知」警報を発する。
In S-14, the observed value Q T of the mass flow meter 5 is 0.
In the case of sccm, all mass flow controllers 2 are set in S-15.
And with the secondary side automatic shut-off valve 3 opened, evacuate sufficiently,
S-16 at a mass flow meter 5 observations Q T at this time 0s
If it is larger than ccm, an alarm "detection of atmospheric leakage between the primary automatic shutoff valve 1 and the secondary automatic shutoff valve 3" is issued in S-19, and all mass flow controllers 2 and 2 are once communicated in S-20. The secondary automatic shutoff valve 3 is closed. Then, first in S-22, gas-
Sufficiently evacuated Open 1 mass flow controller 2 and the secondary-side automatic shut-off valve 3, if the observed value Q T at this time the mass flow meter 5 at S-23 is larger than 0sccm "gas S-25 -1 detection of atmospheric leakage between the primary automatic shutoff valve 1 and the secondary automatic shutoff valve 3 is issued.

【0018】S−23で質量流量計5の観測値QT が0
sccmの場合は、ガス−2から順番にガス−Nまで同
様の動作を行う(S−20〜S−24)ことにより、ど
のガスの一次側自動遮断弁1と二次側自動遮断弁3の間
で大気漏洩が発生しているのかを検知しS−25で警報
を発する。
In S-23, the observed value Q T of the mass flow meter 5 is 0.
In the case of sccm, the same operation is sequentially performed from gas-2 to gas-N (S-20 to S-24), so that the primary-side automatic shutoff valve 1 and the secondary-side automatic shutoff valve 3 of any gas are set. It detects whether air leakage has occurred between them, and issues an alarm in S-25.

【0019】次に本発明の第4の実施の形態を図4の動
作フローチャートを併用して説明する。
Next, a fourth embodiment of the present invention will be described with reference to the operation flowchart of FIG.

【0020】まず図4のS−31において、全ガスのN
2 流量換算係数CF,設定流量Qset および許容誤差d
を検知制御部7に入力する。次でS−33において全て
の一次側自動遮断弁1を閉じ、全ての質量流量制御器2
と二次側自動遮断弁3と最終自動遮断弁4を開き、充分
真空排気した後、S−35で、ガス−1の一次側自動遮
断弁1を開き、質量流量制御器2にて設定流量に制御さ
れたガスを真空処理室6に導入する。次でS−36でこ
のとき質量流量計5での観測値QT が、ガス−1をN2
換算した流量QSET (1)CF(1)に対して許容誤差
d以下か否かを判断し、許容誤差dを超える場合はS−
38で「ガス−1の質量流量制御器2の制御流量異常検
知」警報を発する。また、許容誤差d以下の場合、ガス
−2からガス−Nまで順番に同様な処理を行い(S−3
3〜S−37)質量流量制御器2の異常箇所を特定す
る。
First, in step S-31 in FIG.
(2) Flow rate conversion coefficient CF, set flow rate Q set and allowable error d
Is input to the detection control unit 7. Next, in S-33, all the primary side automatic shutoff valves 1 are closed, and all the mass flow controllers 2 are closed.
, The secondary automatic shutoff valve 3 and the final automatic shutoff valve 4 are opened, and after sufficiently evacuating, the primary automatic shutoff valve 1 of the gas-1 is opened in S-35, and the set flow rate is set by the mass flow controller 2. Is introduced into the vacuum processing chamber 6. Observations Q T at the time mass flow meter 5 in S-36 in the following is a gas -1 N 2
It is determined whether or not the converted flow rate Q SET (1) CF (1) is equal to or less than an allowable error d.
At 38, an alarm "detection of abnormal control flow rate of gas-1 mass flow controller 2" is issued. When the error is equal to or smaller than the allowable error d, the same processing is sequentially performed from gas-2 to gas-N (S-3).
3-S-37) Identify the abnormal part of the mass flow controller 2.

【0021】次に具体例を挙げて説明する。ガス−1=
Cl2 の設定流量が50sccm,N2 換算係数が0.
86と入力された場合に、ガス配管系が正常なとき真空
処理室6へ導入されるガス−1のN2 換算流量は、 QSET (1)×CF(1)=50×0.86=43sc
cm である。
Next, a specific example will be described. Gas-1 =
The set flow rate of Cl 2 is 50 sccm, and the N 2 conversion coefficient is 0.
When 86 is input, when the gas piping system is normal, the N 2 conversion flow rate of gas-1 introduced into the vacuum processing chamber 6 is: Q SET (1) × CF (1) = 50 × 0.86 = 43sc
cm 2.

【0022】このとき質量流量制御器2が設定した流量
通りに制御できない場合、すなわち設定流量50scc
mに対して55sccmと誤制御されたとき、質量流量
計5でQT は QT =55×0.86=47.3sccm と観測される。このときの許容誤差d=2%と予め決め
てある場合 |ΔQ|=|〔(47.3−43)/43〕|×100
=10.0>2(%) となり、「ガス−1の質量流量制御器2の制御流量異常
検知」警報を発する。
At this time, when the mass flow controller 2 cannot perform the control according to the set flow rate, that is, the set flow rate 50 scc
When erroneously controlled to 55 sccm with respect to m, Q T is observed by the mass flow meter 5 as Q T = 55 × 0.86 = 47.3 sccm. In the case where the allowable error d at this time is predetermined to be 2%, | ΔQ | = | [(47.3-43) / 43] | × 100
= 10.0> 2 (%), and an alarm of "abnormal detection of control flow rate of gas-1 mass flow controller 2" is issued.

【0023】[0023]

【発明の効果】以上説明したように本発明による真空処
理装置は、真空処理室へガスを導入する直前に質量流量
計を設け、且つ真空処理中にこの質量流量計で観測され
た流量と、設定された流量を比較するという手段を講じ
ることにより、二次側ガス配管における大気成分の混入
を検知できるという効果を有する。また、真空処理に用
いられるガスの質量流量制御器の誤動作を検知できる効
果も有する。
As described above, in the vacuum processing apparatus according to the present invention, a mass flow meter is provided just before gas is introduced into the vacuum processing chamber, and the flow rate observed by the mass flow meter during vacuum processing is as follows: By taking the means of comparing the set flow rates, there is an effect that the entry of atmospheric components into the secondary gas pipe can be detected. Further, there is an effect that a malfunction of the mass flow controller of the gas used for the vacuum processing can be detected.

【0024】さらに、各ガス配管を真空排気しながら各
種弁を開閉したときの質量流量計が流量を検出したか否
かで、どの部分で大気混入しているか検知できるという
効果を有する。
Further, there is an effect that it is possible to detect in which part the atmosphere is mixed by detecting whether or not the mass flow meter detects the flow rate when each valve is opened and closed while evacuating each gas pipe.

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

【図1】本発明の第1の実施形態の真空処理装置の構成
図。
FIG. 1 is a configuration diagram of a vacuum processing apparatus according to a first embodiment of the present invention.

【図2】本発明の第2の実施の形態を説明する為の動作
フローチャート。
FIG. 2 is an operation flowchart for explaining a second embodiment of the present invention.

【図3】本発明の第3の実施の形態を説明する為の動作
フローチャート。
FIG. 3 is an operation flowchart for explaining a third embodiment of the present invention.

【図4】本発明の第4の実施の形態を説明する為の動作
フローチャート。
FIG. 4 is an operation flowchart for explaining a fourth embodiment of the present invention.

【図5】従来の真空処理装置の構成図。FIG. 5 is a configuration diagram of a conventional vacuum processing apparatus.

【符号の説明】[Explanation of symbols]

1 一次側自動遮断弁 2 質量流量制御器 3 二次側自動遮断弁 4 最終自動遮断弁 5 質量流量計 6 真空処理室 7 検知制御部 8 ガスシリンダ収納容器 9 ガスシリンダ 10 減圧弁 11 ガス漏洩検知器 12 自動遮断弁 13,13A 二次側ガス配管 14 ガス配管収納容器 15,15A 一次側ガス配管 16 ガス質量流量制御器 DESCRIPTION OF SYMBOLS 1 Primary-side automatic shut-off valve 2 Mass flow controller 3 Secondary-side automatic shut-off valve 4 Final automatic shut-off valve 5 Mass flow meter 6 Vacuum processing chamber 7 Detection control part 8 Gas cylinder storage container 9 Gas cylinder 10 Pressure reducing valve 11 Gas leak detection Container 12 Automatic shut-off valve 13, 13A Secondary gas pipe 14 Gas pipe storage container 15, 15A Primary gas pipe 16 Gas mass flow controller

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) H01L 21/3065 B01J 3/03 C23F 4/00 H01L 21/205 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 6 , DB name) H01L 21/3065 B01J 3/03 C23F 4/00 H01L 21/205

Claims (6)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ガスシリンダに順次接続された一次側自
動遮断弁と質量流量制御器と二次側自動遮断弁とからな
る複数組のガスラインと、前記ガスラインの各前記二次
側自動遮断弁に一端が接続され他端が一系統にまとめら
れたガス配管と、このガス配管に接続された最終自動遮
断弁と、この最終自動遮断弁に接続された質量流量計
と、この質量流量計に接続された真空処理室と、前記質
量流量計に接続され複数組の前記ガスラインを流れる処
理ガスの総設定流量の値を記憶しこの設定値と前記質量
流量計の測定値とを比較し測定値が設定値より大きい場
合は警報を発生すると共に前記一次側自動遮断弁と前記
二次側自動遮断弁を閉る為の信号を送出する検知制御手
段とを含むことを特徴とする真空処理装置。
1. A plurality of gas lines comprising a primary automatic shutoff valve, a mass flow controller, and a secondary automatic shutoff valve sequentially connected to a gas cylinder, and each of the secondary automatic shutoffs of the gas line. A gas pipe having one end connected to the valve and the other end integrated into one system, a final automatic shutoff valve connected to the gas pipe, a mass flowmeter connected to the final automatic shutoff valve, and the mass flowmeter The vacuum processing chamber connected to the, stores the value of the total set flow rate of the processing gas flowing through the plurality of gas lines connected to the mass flow meter, and compares this set value with the measured value of the mass flow meter. A vacuum processing unit that generates an alarm when the measured value is larger than a set value, and includes a detection control unit that sends a signal for closing the primary automatic shutoff valve and the secondary automatic shutoff valve. apparatus.
【請求項2】 検知制御手段は、一次側自動遮断弁又は
二次側自動遮断弁又は最終自動遮断弁を閉じて、真空処
理室を真空引きした時に、質量流量計に設定値以上のガ
スが流れた場合警報を発生する機能を合せ持つ請求項1
記載の真空処理装置。
2. The detection control means closes a primary automatic shutoff valve, a secondary automatic shutoff valve, or a final automatic shutoff valve, and when the vacuum processing chamber is evacuated, gas exceeding a set value is supplied to a mass flow meter. 2. The system according to claim 1, further comprising a function of generating an alarm when the flow is generated.
The vacuum processing apparatus as described in the above.
【請求項3】 請求項1又は請求項2記載の真空処理装
置を用い、前記一次側自動遮断弁と前記二次側自動遮断
弁と前記最終自動遮断弁を開き、各ラインに前記各質量
流量制御器により設定されたガスを流し、このガス流量
の総和を前記質量流量計で測定し、この測定値が所定の
値以上である場合は大気混入の警報を発生させることを
特徴とする真空処理装置への大気混入の検知方法。
3. The vacuum processing apparatus according to claim 1, wherein the primary automatic shutoff valve, the secondary automatic shutoff valve, and the final automatic shutoff valve are opened, and each of the mass flow rates is set to each line. A vacuum process characterized by flowing a gas set by a controller, measuring the sum of the gas flow rates by the mass flow meter, and, when the measured value is equal to or more than a predetermined value, generating an alarm of air mixing. A method for detecting atmospheric contamination in equipment.
【請求項4】 請求項2記載の真空処理装置を用い、前
記一次側自動遮断弁と前記二次側自動遮断弁と前記最終
自動遮断弁を閉じたのち前記真空処理室を真空引きし、
この時前記質量流量計で測定されたガス量が所定の値以
上である場合は大気混入の警報を発させることを特徴と
する真空処理装置への大気混入の検知方法。
4. The vacuum processing apparatus according to claim 2, wherein the primary automatic shutoff valve, the secondary automatic shutoff valve, and the final automatic shutoff valve are closed, and then the vacuum processing chamber is evacuated;
At this time, when the gas amount measured by the mass flow meter is equal to or more than a predetermined value, a warning of the atmospheric contamination is issued to the vacuum processing apparatus, wherein a method of detecting atmospheric contamination in the vacuum processing apparatus is provided.
【請求項5】 質量流量計で測定されたガス量が所定値
以下の場合、前記最終自動遮断弁を開け前記真空処理室
を真空引きし、この時前記質量流量計で測定されたガス
量が所定の値以上である場合は大気混入の警報を発生さ
せる請求項4記載の真空処理装置への大気混入の検知方
法。
5. When the gas amount measured by the mass flow meter is equal to or less than a predetermined value, the final automatic shut-off valve is opened, and the vacuum processing chamber is evacuated. 5. The method according to claim 4, wherein when the value is equal to or more than a predetermined value, an alarm of air entrapment is generated.
【請求項6】 最終自動遮断弁を開けた後に質量流量計
で測定されたガス量が所定値以下の場合、前記二次側自
動遮断弁を開け前記真空処理室を真空引きし、この時前
記質量流量計で測定されたガス量が所定の値以上の場合
は大気混入の警報を発生させる請求項5記載の真空処理
装置への大気混入の検知方法。
6. When the gas amount measured by the mass flow meter after opening the final automatic shutoff valve is equal to or less than a predetermined value, the secondary side automatic shutoff valve is opened and the vacuum processing chamber is evacuated. 6. The method according to claim 5, wherein when the gas amount measured by the mass flow meter is equal to or more than a predetermined value, an alarm of air entrapment is generated.
JP7208899A 1995-08-16 1995-08-16 Vacuum processing apparatus and method for detecting atmospheric contamination in vacuum processing apparatus Expired - Lifetime JP2885142B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

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JP2885142B2 true JP2885142B2 (en) 1999-04-19

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SE513333C2 (en) * 1998-11-13 2000-08-28 Alfa Laval Ab Methods and arrangements for monitoring a process carried out under vacuum
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JP5175447B2 (en) * 2006-03-27 2013-04-03 トヨタ自動車株式会社 GAS FLOW CONTROL DEVICE, FUEL CELL SYSTEM, AND GAS FLOW CONTROL METHOD
KR100969990B1 (en) * 2008-03-21 2010-07-15 주식회사 아토 Checking method and apparatus of mass flow controller
US10359743B2 (en) 2014-11-25 2019-07-23 Applied Materials, Inc. Substrate processing systems, apparatus, and methods with substrate carrier and purge chamber environmental controls
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