JP3373763B2 - Breakthrough detection device for exhaust gas treatment equipment - Google Patents

Breakthrough detection device for exhaust gas treatment equipment

Info

Publication number
JP3373763B2
JP3373763B2 JP23336397A JP23336397A JP3373763B2 JP 3373763 B2 JP3373763 B2 JP 3373763B2 JP 23336397 A JP23336397 A JP 23336397A JP 23336397 A JP23336397 A JP 23336397A JP 3373763 B2 JP3373763 B2 JP 3373763B2
Authority
JP
Japan
Prior art keywords
gas
breakthrough
reaction tank
exhaust gas
cleaning
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
JP23336397A
Other languages
Japanese (ja)
Other versions
JPH1157386A (en
Inventor
太郎 永嶋
義男 伊藤
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP23336397A priority Critical patent/JP3373763B2/en
Publication of JPH1157386A publication Critical patent/JPH1157386A/en
Application granted granted Critical
Publication of JP3373763B2 publication Critical patent/JP3373763B2/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]

【発明の属する技術分野】本発明は半導体や液晶素子等
の精密電子部品の製造装置(以下、「半導体製造装置」
と称する)より排出される製造プロセスガスを除害処理
する排ガス処理装置の、特に半導体製造装置の反応室や
ガス流路のクリーニング目的で使用されるClF3ガス
を除害処理する排ガス処理装置の除害反応槽の交換時期
である破過を検知するのに好適な破過検知装置に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for manufacturing precision electronic parts such as semiconductors and liquid crystal elements (hereinafter referred to as "semiconductor manufacturing apparatus").
Of the manufacturing process gas discharged from the exhaust gas treatment apparatus, particularly of the exhaust gas treatment apparatus for detoxifying the ClF 3 gas used for cleaning the reaction chamber and the gas flow path of the semiconductor manufacturing apparatus. The present invention relates to a breakthrough detection device suitable for detecting breakthrough when it is time to replace a detoxification reaction tank.

【0002】[0002]

【従来の技術】半導体製造装置においては、種々の製造
プロセスガスを使用するが、該製造プロセスガスの多く
は有害ガスであり、そのまま大気に放出することができ
ない。そこで半導体製造装置から排出され製造プロセス
ガスを排ガス処理装置を通して、除害、即ち無害化して
いる。
2. Description of the Related Art In a semiconductor manufacturing apparatus, various manufacturing process gases are used, but most of the manufacturing process gases are harmful gases and cannot be directly discharged to the atmosphere. Therefore, the manufacturing process gas discharged from the semiconductor manufacturing apparatus is removed, that is, rendered harmless, through the exhaust gas processing apparatus.

【0003】図3はこのような排ガス処理設備の概要を
示す図である。図示するように半導体製造装置103に
はガス供給装置101からSiH4ガス等のデポガスが
供給されると共に、ガス供給装置102からは半導体製
造装置103の反応室やガス流路をクリーニングする為
のClF3ガス等が供給されるようになっている。ま
た、半導体製造装置103からのSiH4ガス等のデポ
ガスやClF3ガス等のクリーニングガスはドライポン
プ104により排ガス処理装置105に送られ、該排ガ
ス処理装置105で除害処理された後、工場ダクト10
6に排出されるようになっている。
FIG. 3 is a diagram showing an outline of such an exhaust gas treatment facility. As shown in the figure, the semiconductor manufacturing apparatus 103 is supplied with a deposition gas such as SiH 4 gas from the gas supply apparatus 101, and the gas supply apparatus 102 is used to clean the reaction chamber and the gas flow path of the semiconductor manufacturing apparatus 103 with ClF. 3 Gas, etc. are supplied. Deposition gas such as SiH 4 gas or cleaning gas such as ClF 3 gas from the semiconductor manufacturing apparatus 103 is sent to the exhaust gas treatment apparatus 105 by the dry pump 104, and after being detoxified by the exhaust gas treatment apparatus 105, the factory duct. 10
6 is discharged.

【0004】上記排ガス処理装置105にはSiH4
ス等のデポガスを除害するデポガス反応槽や、ClF3
ガス等のクリーニングガスを除害するクリーニングガス
反応槽が備えられており、それぞれデポガス及びクリー
ニングガスは除害される。これらデポガス反応槽やクリ
ーニングガス反応槽によって除害できるデポガスやクリ
ーニングガスの処理量は決まっており、この処理量を越
えると除害作用は著しく低下する。そこでこの処理量を
越えた時を反応槽の寿命(交換時期)、即ち破過として
デポガス反応槽やクリーニングガス反応槽を交換してい
る。
The exhaust gas treatment device 105 includes a depot gas reaction tank for removing depot gas such as SiH 4 gas and ClF 3 gas.
A cleaning gas reaction tank for removing a cleaning gas such as a gas is provided, and the deposition gas and the cleaning gas are removed respectively. The processing amount of the depot gas or the cleaning gas that can be removed by the depot gas reaction tank or the cleaning gas reaction tank is determined, and if the processing amount exceeds this amount, the detoxification effect is significantly reduced. Therefore, when the processing amount is exceeded, the life (replacement time) of the reaction tank, that is, breakthrough, is regarded as the breakthrough, and the depot gas reaction tank and the cleaning gas reaction tank are replaced.

【0005】ところでこのデポガス反応槽やクリーニン
グガス反応槽の交換時期、即ち破過を精度良く検知する
ことが重要となる。破過が早すぎるとまだ十分に除害機
能を有する反応槽を交換することになり費用の無駄とな
り、遅すぎると有害ガスが放出されるという問題があ
る。
By the way, it is important to accurately detect the replacement time of the deposition gas reaction tank or the cleaning gas reaction tank, that is, the breakthrough. If the breakthrough is too early, a reaction tank having a sufficient detoxification function will be replaced, resulting in a waste of cost, and if it is too late, harmful gas will be emitted.

【0006】従来、上記反応槽の破過を検知する方法、
特にClF3ガス等のクリーニングガスを除害する反応
槽の破過検知方法として、下記の及びの方法があっ
た。 反応槽から排出側にガス検知器を設け、該ガス検知器
でクリーニングガスの濃度を検知することにより、該濃
度が所定値以上になったら破過として破過を検知する方
[0006] Conventionally, a method for detecting the breakthrough of the reaction tank,
In particular, the following methods (1) and (2) have been mentioned as methods for detecting the breakthrough of the reaction tank for removing the cleaning gas such as ClF 3 gas. A method in which a gas detector is provided on the discharge side from the reaction tank and the concentration of the cleaning gas is detected by the gas detector to detect breakthrough as breakthrough when the concentration exceeds a predetermined value.

【0007】反応槽の重量を測定し、重量が所定値以
上増加したら破過として破過を検知する方法
A method of measuring the weight of a reaction tank and detecting the breakthrough as a breakthrough when the weight increases by a predetermined value or more.

【0008】[0008]

【発明が解決しようとする課題】上記ガス検知器を用い
る方法は、ガス検知器が長時間ClF3ガス等のクリー
ニングガスに暴露された時または6ケ月以上校正を行わ
れない場合に、正常にガスを検知しない可能性があると
いう問題があった。また、校正に手間とコストがかかる
という問題もあった。重量増加量による方法は、カラム
自重の割に、重量増加量が少なく、精度の良い検知がで
きないという問題があった。
The method using the gas detector described above is normally performed when the gas detector is exposed to a cleaning gas such as ClF 3 gas for a long time or when calibration is not performed for 6 months or more. There was a problem that gas might not be detected. In addition, there is also a problem that calibration takes time and cost. The method using the amount of weight increase has a problem that the amount of weight increase is small relative to the weight of the column and accurate detection cannot be performed.

【0009】本発明は上述の点に鑑みてなされたもの
で、上記問題点を解消し、精度の良い反応槽の破過を検
知できる製造プロセス排ガス処理装置の破過検知装置を
提供することを目的とする。
The present invention has been made in view of the above points, and it is an object of the present invention to solve the above problems and provide a breakthrough detection device for a manufacturing process exhaust gas treatment device which can detect the breakthrough of a reaction tank with high accuracy. To aim.

【0010】[0010]

【課題を解決するための手段】上記課題を解決するため
請求項1に記載の発明は、除害反応槽を具備し、製造装
置と通信回路で接続され、該製造装置との間で信号の送
受を行いながら該製造装置から排出される製造プロセス
排ガスを除害反応槽で除害する排ガス処理装置の該除害
反応槽の交換時期である破過を検知する破過検知手段を
具備する排ガス処理装置の破過検知装置において、製造
装置は製造プロセス排ガス排出1回当たりの排出時間及
び排出時の単位時間当たりの排出流量が予め設定されて
おり、破過検知手段は通信回路を介して製造装置から排
ガス処理装置に送られてくる排ガス放出指令の回数及び
/又は放出時間より破過を検知することを特徴とする。
In order to solve the above-mentioned problems, the invention according to claim 1 is provided with a detoxification reaction tank, is connected to a manufacturing apparatus by a communication circuit, and transmits a signal between the manufacturing apparatus. Exhaust gas equipped with breakthrough detection means for detecting breakthrough which is the time to replace the abatement reaction tank of an exhaust gas treatment device for removing a manufacturing process exhaust gas discharged from the manufacturing device while transmitting and receiving in an abatement reaction tank In the breakthrough detection device of the processing device, the manufacturing device is preset with the discharge time per exhaust of the manufacturing process exhaust gas and the discharge flow rate per unit time at the time of discharge, and the breakthrough detection means is manufactured through the communication circuit. The breakthrough is detected from the number and / or the release time of the exhaust gas release command sent from the device to the exhaust gas treatment device.

【0011】また、請求項2に記載の発明は請求項1に
記載の排ガス処理装置の破過検知装置において、破過検
知手段は排ガス排出指令の回数及び/又は放出時間より
破過を検知する手段に加え、ガス検知器で除害反応槽か
ら排出される排ガス濃度を検知して破過を検知する手段
及び/又は反応槽の重量増加より破過を検知する手段を
具備することを特徴とする。
The invention according to claim 2 is the breakthrough detection device for an exhaust gas treatment device according to claim 1, wherein the breakthrough detection means detects the breakthrough based on the number and / or the emission time of the exhaust gas discharge command. In addition to the means, a means for detecting breakthrough by detecting the concentration of exhaust gas discharged from the abatement reaction tank with a gas detector and / or a means for detecting breakthrough based on an increase in the weight of the reaction tank are provided. To do.

【0012】[0012]

【発明の実施の形態】以下、本発明の実施の形態例を図
面に基づいて説明する。図2はこの種の製造プロセス排
ガス処理装置の構成を示す図である。図2において、8
は成膜ガス等のデポガスを除害するデポガス反応槽、9
はClF3等のクリーニングガスを除害するクリーニン
グガス反応槽である。デポガス反応槽8は反応槽容器内
にデポガスを物理的吸着又は化学反応によって無害化す
る除害剤(薬剤)が充填されたものであり、クリーニン
グガス反応槽は反応槽容器内にClF3ガス等のクリー
ニングガスを物理的吸着又は化学反応によって無害化す
る除害剤(薬剤)が充填されたものである。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described below with reference to the drawings. FIG. 2 is a diagram showing the configuration of this type of manufacturing process exhaust gas treatment apparatus. In FIG. 2, 8
Is a deposition gas reaction tank for removing deposition gas such as deposition gas, 9
Is a cleaning gas reaction tank for removing a cleaning gas such as ClF 3 . The depot gas reaction tank 8 is one in which a detoxifying agent (chemical) that detoxifies the depot gas by physical adsorption or chemical reaction is filled in the reaction tank container, and the cleaning gas reaction tank is ClF 3 gas in the reaction tank container. The cleaning gas is filled with a detoxifying agent (medicine) that makes it harmless by physical adsorption or chemical reaction.

【0013】流入口11に流入する半導体製造装置から
のデポガスはデポ側流入弁2を通してデポガス反応槽8
に流入し、該デポガス反応槽8でSiH4ガス等のデポ
ガス成分は除害剤に物理的吸着又は化学反応によって無
害化(除害)され、デポ側流出弁4を通って、デポ用流
出口12から工場ダクト(図3の工場ダクト106参
照)に排出される。また、ClF3ガス等のクリーニン
グガスは流入口11に流入し、クリーニング側流入弁3
を通ってクリーニングガス反応槽9に流入し、該クリー
ニングガス反応槽9でClF3ガス成分は除害剤に物理
的吸着又は化学反応により無害化(除害)され、除害さ
れ、クリーニング側流出弁5及びクリーニング側流出口
弁7を通ってクリーニング用流出口13から工場ダクト
に排出される。
The depot gas from the semiconductor manufacturing equipment which flows into the inflow port 11 passes through the depot side inflow valve 2 and the depot gas reaction tank 8
The depot gas component such as SiH 4 gas is detoxified (detoxified) by physical adsorption or chemical reaction with the detoxifying agent in the depot gas reaction tank 8 and passes through the depot side outflow valve 4 to the depot outlet. 12 is discharged to the factory duct (see the factory duct 106 in FIG. 3). Further, a cleaning gas such as ClF 3 gas flows into the inflow port 11, and the cleaning side inflow valve 3
Flow into the cleaning gas reaction tank 9 through which the ClF 3 gas component is detoxified (detoxified) by physical adsorption or chemical reaction with the detoxifying agent, detoxified, and discharged to the cleaning side. It is discharged from the cleaning outlet 13 to the factory duct through the valve 5 and the cleaning side outlet valve 7.

【0014】1はバイパス弁であり、デポガス反応槽8
又はクリーニングガス反応槽9に詰まり等の障害が発生
し、デポガスのガス圧又はクリーニングガスのガス圧が
異常に高い場合、デポ側流入弁2又はクリーニング側流
入弁3を閉じ該バイパス弁1を開くと共に、デポ側流出
口弁6又はクリーニング側流出口弁7を開いて、デポガ
ス又はクリーニングガスを工場ダクトに排出する。
Reference numeral 1 denotes a bypass valve, which is a deposition gas reaction tank 8
Alternatively, when an obstacle such as clogging occurs in the cleaning gas reaction tank 9 and the gas pressure of the depot gas or the gas pressure of the cleaning gas is abnormally high, the depot side inflow valve 2 or the cleaning side inflow valve 3 is closed and the bypass valve 1 is opened. At the same time, the depot side outlet valve 6 or the cleaning side outlet valve 7 is opened to discharge the depot gas or the cleaning gas to the factory duct.

【0015】上記バイパス弁1、デポ側流入弁2、クリ
ーニング側流入弁3、デポ側流出弁4、クリーニング側
流出弁5、デポ側流出口弁6及びクリーニング側流出口
弁7等の作動弁AはN2流入口14を通ってN2源から供
給されるN2ガスによって作動する弁である。また、N2
ガスは該作動弁Aに供給されると共に、各部の気密をテ
ストするための気密テストブラケットB(図示せず)に
供給され、更に、バルブ15、減圧弁16、接点付流量
計17、逆止弁18を通して、デポ側にパージガスCと
して供給されるようになっている。
Operation valves A such as the bypass valve 1, the depot side inflow valve 2, the cleaning side inflow valve 3, the depot side outflow valve 4, the cleaning side outflow valve 5, the depot side outflow valve 6 and the cleaning side outflow valve 7. is a valve which operates by N 2 gas supplied from N 2 source through the N 2 inlet 14. Also, N 2
The gas is supplied to the actuation valve A and also to an airtightness test bracket B (not shown) for testing the airtightness of each part, and further, the valve 15, the pressure reducing valve 16, the flowmeter with contacts 17, the check valve. The purge gas C is supplied to the depot side through the valve 18.

【0016】デポガス反応槽8にはその出口側にガス検
知器19が設けられ、更に反応槽内の温度を検出する温
度センサ20及び温度指示計21が設けられている。ま
た、クリーニングガス反応槽9の出口側には流入弁SV
E1、流出弁SVE2を介してガス検知器22が設けら
れ、更に反応槽内の温度を検出する温度センサ23及び
温度指示計24が設けられている。また、クリーニング
ガス反応槽9の重量を検出する重量計25及び荷重指示
計26が設けられている。
A gas detector 19 is provided on the outlet side of the depot gas reaction tank 8, and a temperature sensor 20 and a temperature indicator 21 for detecting the temperature inside the reaction tank are further provided. Further, an inflow valve SV is provided on the outlet side of the cleaning gas reaction tank 9.
A gas detector 22 is provided via E1 and the outflow valve SVE2, and a temperature sensor 23 and a temperature indicator 24 for detecting the temperature in the reaction tank are further provided. Further, a weight scale 25 for detecting the weight of the cleaning gas reaction tank 9 and a load indicator 26 are provided.

【0017】27、28は圧力スイッチであり、圧力ス
イッチ27は、流入口11から流入するデポガス又はク
リーニングガスの圧力が高圧力(例えば0.04Kgf
/cm2(G)以上)になると警報を出し、異常高圧力
(例えば0.1Kgf/cm2(G)以上)になると警
報と共にバイパス弁1を開いて、デポガス又はクリーニ
ングガスをデポ用流出口12又はクリーニング用流出口
13から工場ダクトに排出する。また、圧力スイッチ2
8はN2流入口14に流入するN2ガスの圧力が上記作動
弁Aを作動させる所定の圧力以下のとき警報を出す。
Reference numerals 27 and 28 denote pressure switches. The pressure switch 27 has a high pressure (for example, 0.04 Kgf) for the deposit gas or the cleaning gas flowing from the inlet 11.
/ Cm 2 (G) or more), an alarm is issued, and when abnormally high pressure (eg, 0.1 Kgf / cm 2 (G) or more) is opened, the bypass valve 1 is opened together with the alarm, and the depot gas or cleaning gas is discharged to the depot outlet. 12 or the cleaning outlet 13 is discharged to the factory duct. Also, pressure switch 2
8 issues an alarm when the pressure of the N 2 gas flowing into the N 2 inlet 14 is below a predetermined pressure for actuating the actuation valve A.

【0018】29はデポ用破過検知器で、ガス検知器1
9で検知したデポガスの濃度が所定の設定値以上になる
とデポガス反応槽8の交換指令信号を出力する。30は
ClF3用破過検知器で、ガス検知器22で検知された
クリーニングガスであるClF3ガスの濃度が所定の設
定値以上になるとクリーニングガス反応槽9の交換指令
信号を出力する。31はClF3用破過検知器で、荷重
指示計26の指示値が設定値以上となったら、クリーニ
ングガス反応槽9の交換指令信号を出力する。32は温
度指示計21の指示するデポガス反応槽8の温度が所定
の設定値以上になった場合に警報を出す警報器である。
Reference numeral 29 is a breakthrough detector for a depot, which is a gas detector 1
When the concentration of the depot gas detected at 9 becomes equal to or higher than a predetermined set value, a replacement command signal for the depot gas reaction tank 8 is output. A breakthrough detector 30 for ClF 3 outputs a replacement command signal for the cleaning gas reaction tank 9 when the concentration of the cleaning gas ClF 3 gas detected by the gas detector 22 exceeds a predetermined set value. Reference numeral 31 is a breakthrough detector for ClF 3 , which outputs a replacement command signal for the cleaning gas reaction tank 9 when the value indicated by the load indicator 26 exceeds a set value. Reference numeral 32 is an alarm device that issues an alarm when the temperature of the depot gas reaction tank 8 indicated by the temperature indicator 21 exceeds a predetermined set value.

【0019】また、33は温度指示計24の指示するク
リーニングガス反応槽9の温度が所定の設定値以上にな
った場合に警報を出す警報器である。また、34は接点
付流量計17がN2ガスの低流量を検出した場合、即ち
2ガスのパージ流量が低い場合に警報を出す警報器で
ある。また、35〜38はフレキシブル配管であり、デ
ポガス反応槽8の入出力側及びクリーニングガス反応槽
9の入出力側に設けられ、これらの反応槽の交換作業が
容易にできるようになっている。
Reference numeral 33 is an alarm device that issues an alarm when the temperature of the cleaning gas reaction tank 9 indicated by the temperature indicator 24 exceeds a predetermined set value. Further, 34 is a alarm to alert when the contact with the flow meter 17 when detecting a low flow rate of N 2 gas, namely purge flow of N 2 gas is low. Further, 35 to 38 are flexible pipes, which are provided on the input / output side of the deposition gas reaction tank 8 and the input / output side of the cleaning gas reaction tank 9 so that the replacement work of these reaction tanks can be easily performed.

【0020】図1は半導体製造装置103と排ガス処理
装置105の間で送受する信号例を示す図である。図示
するように、半導体製造装置103から排ガス処理装置
105へデポ指令信号S1、クリーニング指令信号S
2、デポ生ガス放出指令信号S3及びクリーニング生ガ
ス放出指令信号S4が出力される。また、排ガス処理装
置105から半導体製造装置103へデポ運転OK信号
S5、デポ反応槽交換準備OK信号S6、クリーニング
運転OK信号S7、クリーニング反応槽交換準備OK信
号S8及び残ガス放出中信号S9が出力される。排ガス
処理装置105から半導体製造装置103へは、重大故
障を示す重故障信号S10、軽い故障を示す軽故障信号
S12及び反応槽交換信号S13も出力される。
FIG. 1 is a diagram showing an example of signals transmitted and received between the semiconductor manufacturing apparatus 103 and the exhaust gas treatment apparatus 105. As shown in the figure, the semiconductor manufacturing apparatus 103 transfers the depot command signal S1 and the cleaning command signal S to the exhaust gas treatment device 105.
2. Deposition raw gas release command signal S3 and cleaning raw gas release command signal S4 are output. Further, the exhaust gas treatment device 105 outputs a depot operation OK signal S5, a depot reaction tank replacement preparation OK signal S6, a cleaning operation OK signal S7, a cleaning reaction tank replacement preparation OK signal S8 and a residual gas releasing signal S9 to the semiconductor manufacturing apparatus 103. To be done. From the exhaust gas treatment device 105 to the semiconductor manufacturing device 103, a serious failure signal S10 indicating a serious failure, a minor failure signal S12 indicating a minor failure, and a reaction vessel replacement signal S13 are also output.

【0021】上記重故障信号S10は故障が重大で排ガ
ス処理が不可能な場合に出力される信号であり、ここで
は上記圧力スイッチ27で検出したデポガス圧力やクリ
ーニングガス圧力が異常高圧(例えば0.1Kgf/c
2(G)以上)の場合、漏電及び停電の場合に出され
る。また、軽故障信号S12は故障が軽い場合に出力さ
れる信号であり、ここでは、上記圧力スイッチ27で検
出したデポガス圧力やクリーニングガス圧力が高圧(例
えば0.04Kgf/cm2(G)以上)の場合、上記
圧力スイッチ28が検出するN2ガスの圧力が作動弁を
作動させる所定の圧力以下の場合、N2ガスのパージ流
量が少なく警報器34から警報が発せられた場合、デポ
ガス反応槽8の温度が高く警報器32から警報が発せら
れた場合、クリーニングガス反応槽9の温度が高く警報
器33から警報が発せられた場合に出される。
The serious failure signal S10 is a signal that is output when the failure is serious and exhaust gas treatment is impossible, and here, the deposition gas pressure and the cleaning gas pressure detected by the pressure switch 27 are abnormally high (for example, 0. 1 Kgf / c
m 2 (G) or more), it will be issued in case of electric leakage and power failure. Further, the light failure signal S12 is a signal output when the failure is light, and here, the deposition gas pressure or the cleaning gas pressure detected by the pressure switch 27 is high (for example, 0.04 Kgf / cm 2 (G) or more). If the pressure of the N 2 gas detected by the pressure switch 28 is less than or equal to the predetermined pressure for operating the operating valve, the purge flow rate of the N 2 gas is small and the alarm 34 issues an alarm, the depot gas reaction tank It is issued when the temperature of 8 is high and the alarm 32 issues an alarm, and when the temperature of the cleaning gas reaction tank 9 is high and the alarm 33 issues an alarm.

【0022】また、反応槽交換信号S13は上記デポ用
破過検知器29がガス検知器19で検知したデポガスの
濃度が所定の設定値以上になり、デポガス反応槽8の交
換時期を検知した場合に出力される交換指令信号、上記
ClF3用破過検知器30がガス検知器22で検知した
ClF3ガスの濃度が所定の設定値以上になり、クリー
ニングガス反応槽9の交換時期を検知した場合に出力さ
れる交換指令信号、及び上記ClF3用破過検知器31
が荷重指示計26の指示値が設定値以上を示し、クリー
ニングガス反応槽9の交換時期を検知した場合に出力さ
れる交換指令信号である。
Further, the reaction tank exchange signal S13 is used when the depot breakthrough detector 29 detects that the concentration of the depot gas detected by the gas detector 19 is equal to or higher than a predetermined set value and the time for exchanging the depot gas reaction tank 8 is detected. The replacement command signal output to the above, the concentration of ClF 3 gas detected by the gas detector 22 by the breakthrough detector 30 for ClF 3 exceeds a predetermined set value, and the replacement time of the cleaning gas reaction tank 9 is detected. The replacement command signal output in this case and the breakthrough detector 31 for ClF 3
Is a replacement command signal output when the value indicated by the load indicator 26 is equal to or greater than the set value and the replacement time of the cleaning gas reaction tank 9 is detected.

【0023】図3に示すような構成の排ガス処理設備に
おいては、通常オペレータは半導体製造装置103の側
に居る。排ガス処理装置105でデポ用破過検知器29
及びClF3用破過検知器30、31がデポガス反応槽
8及びクリーニングガス反応槽9の交換時期を検知し、
反応槽交換信号S13を半導体製造装置103に出力し
た場合、オペレータは排ガス処理装置105に出向き、
デポガス反応槽8又はクリーニングガス反応槽9を交換
する。しかしながら、デポ用破過検知器29及びClF
3用破過検知器30、31による破過検知、特にClF3
用破過検知器30、31によるガス濃度による破過検知
や重量による破過検知は上記のように精度の良い破過を
検知することができないという問題があった。
In the exhaust gas treatment facility having the structure shown in FIG. 3, the operator is usually on the side of the semiconductor manufacturing apparatus 103. Breakthrough detector for depot 29 with exhaust gas treatment device 105
And the breakthrough detectors 30 and 31 for ClF 3 detect the replacement time of the depot gas reaction tank 8 and the cleaning gas reaction tank 9,
When the reaction tank exchange signal S13 is output to the semiconductor manufacturing apparatus 103, the operator goes to the exhaust gas treatment apparatus 105,
The deposit gas reaction tank 8 or the cleaning gas reaction tank 9 is replaced. However, the depot breakthrough detector 29 and ClF
3 breakthrough detectors 30 and 31 for breakthrough detection, especially ClF 3
The breakthrough detection based on the gas concentration and the breakthrough detection based on the weight by the breakthrough detectors 30 and 31 have a problem that the breakthrough cannot be detected with high accuracy as described above.

【0024】そこで、本実施形態例では、図1に示すよ
うに、半導体製造装置103からのクリーニング生ガス
放出指令信号S4の出力回数及び/又はクリーニングガ
ス放出時間をカウントするカウンター40を設け、この
カウント値からクリーニングガスの排出量を検知し、ク
リーニングガス反応槽9の交換時期を検知するようにし
た。
Therefore, in this embodiment, as shown in FIG. 1, a counter 40 for counting the number of times the cleaning raw gas release command signal S4 is output from the semiconductor manufacturing apparatus 103 and / or the cleaning gas release time is provided. The discharge amount of the cleaning gas is detected from the count value, and the replacement time of the cleaning gas reaction tank 9 is detected.

【0025】図2に示す構成の排ガス処理装置におい
て、該排ガス処理装置の流入口11から流入した半導体
製造装置103(図3参照)の反応室やガス流路をクリ
ーニングしたクリーニングガス(主にClF3ガス)は
クリーニングガス反応槽9に流入し、該反応槽容器に充
填された除害剤により物理的吸着又は化学反応によって
無害化される。この際、除害剤はクリーニングガスが流
入する流入口に近い方から除々に無害性能を失なう。1
本のクリーニングガス反応槽で除害されるクリーニング
ガス量は決められており、流入するクリーニングガス量
がその量に達すると、クリーニングガス反応槽9はその
無害性能を失なう。
In the exhaust gas treating apparatus having the structure shown in FIG. 2, a cleaning gas (mainly ClF) is used for cleaning the reaction chamber and the gas flow path of the semiconductor manufacturing apparatus 103 (see FIG. 3) that has flowed in from the inlet 11 of the exhaust gas treating apparatus. 3 gas) flows into the cleaning gas reaction tank 9 and is detoxified by physical adsorption or chemical reaction by the detoxifying agent filled in the reaction tank container. At this time, the detoxifying agent gradually loses its harmless performance from the side closer to the inflow port into which the cleaning gas flows. 1
The amount of cleaning gas removed in the cleaning gas reaction tank of the book is fixed, and when the amount of inflowing cleaning gas reaches that amount, the cleaning gas reaction tank 9 loses its harmless performance.

【0026】クリーニングガス反応槽9に流入するガス
流入量は単位時間当たりのガス流入量と流入時間の積で
決まるから、排ガス処理装置に流入する単位時間当たり
の流入量及びクリーニング1回当たりの流入時間は予め
半導体製造装置103の側で決められている。クリーニ
ングガスの流入タイミング及び流入時間は、図1の排ガ
ス処理装置105が半導体製造装置103からクリーニ
ング生ガス放出指令信号S4を受け取ることで確認でき
る。従って、このクリーニング生ガス放出指令信号S4
の出力回数及びクリーニング時間(クリーニングガス排
出時間)を計測するカウンター40を設け、該カウンタ
ー40に予めクリーニングガス反応槽9で処理できるク
リーニング回数及びクリーニング時間を設定しておき、
クリーニング回数又はクリーニング時間のどちらかが設
定値に達した時にクリーニングガス反応槽9の交換時期
として、半導体製造装置103に反応槽交換信号S13
を出力し、クリーニングガス反応槽9の破過を知らせ
る。
Since the gas inflow amount flowing into the cleaning gas reaction tank 9 is determined by the product of the gas inflow amount per unit time and the inflow time, the inflow amount per unit time flowing into the exhaust gas treating apparatus and the inflow per cleaning operation. The time is predetermined by the semiconductor manufacturing apparatus 103 side. The inflow timing and inflow time of the cleaning gas can be confirmed by the exhaust gas processing device 105 of FIG. 1 receiving the cleaning raw gas release command signal S4 from the semiconductor manufacturing device 103. Therefore, this cleaning raw gas release command signal S4
Is provided with a counter 40 for measuring the number of output times and the cleaning time (cleaning gas discharge time), and the number of cleanings and the cleaning time that can be processed in the cleaning gas reaction tank 9 are set in advance in the counter 40.
When either the number of cleanings or the cleaning time reaches a set value, the cleaning gas reaction tank 9 is replaced with the reaction tank replacement signal S13 to the semiconductor manufacturing apparatus 103.
Is output to notify the breakthrough of the cleaning gas reaction tank 9.

【0027】上記のように、クリーニングガス反応槽9
の破過検知をClF3用破過検知器30、31によるガ
ス濃度や重量による破過検知とは異なり、半導体製造装
置103から排ガス処理装置105に出力されるクリー
ニング生ガス放出指令信号S4の出力回数とクリーニン
グ時間から検知するので、精度良く確実にクリーニング
ガス反応槽9の破過を検知できる。しかも、クリーニン
グ生ガス放出指令信号S4の出力回数とクリーニング時
間はカウンターを設けるのみで計測できるから、破過検
知装置の構成が極めて簡単となる。
As described above, the cleaning gas reaction tank 9
Is different from the breakthrough detection based on the gas concentration and weight by the breakthrough detectors 30 and 31 for ClF 3 , the output of the cleaning raw gas release command signal S4 output from the semiconductor manufacturing apparatus 103 to the exhaust gas processing apparatus 105. Since the detection is performed based on the number of times and the cleaning time, the breakthrough of the cleaning gas reaction tank 9 can be accurately detected. Moreover, since the number of times the cleaning raw gas release command signal S4 is output and the cleaning time can be measured only by providing a counter, the configuration of the breakthrough detection device becomes extremely simple.

【0028】なお、上記実施形態例ではクリーニングガ
ス反応槽9の破過検知を例に示したが、本発明はこれに
限定されるものではなく、半導体製造装置のデポ運転に
おける単位時間当たりのデポガス流量及びデポ運転時間
が予め決められている場合、デポ生ガス放出指令信号S
3の出力回数及びデポ運転時間をカウント(計測)する
カウンターを設け、該カウンターにデポガス反応槽8で
処理できるデポ運転回数及びデポガス排出(流入)時間
を設定しておき、デポ運転回数又はデポガス排出(流
入)時間のどちらかが設定値に達した時にデポガス反応
槽8の交換時期として、半導体製造装置103に反応槽
交換信号S13を出力し、デポガス反応槽8の破過を知
らせるように構成してもよい。
In the above embodiment, the detection of the breakthrough of the cleaning gas reaction tank 9 is shown as an example, but the present invention is not limited to this, and the deposition gas per unit time in the depot operation of the semiconductor manufacturing apparatus is not limited thereto. When the flow rate and the depot operation time are predetermined, the depot raw gas release command signal S
3 is provided with a counter for counting (measuring) the number of outputs and the depot operation time, and the number of depot operations and the depot gas discharge (inflow) time that can be processed in the depot gas reaction tank 8 are set in the counter, and the number of depot operations or the depot gas discharge When either of the (inflow) times has reached a set value, it is configured to output a reaction tank exchange signal S13 to the semiconductor manufacturing apparatus 103 to notify the breakthrough of the depot gas reaction tank 8 as the replacement time of the depot gas reaction tank 8. May be.

【0029】なお、上記例ではデポガスとしてモノシラ
ン(SiH4)を示したが、デポガスとしては例えばホ
スファン(PH3)、アルシン(AsH3)、ジボラン
(B26)、ジシラン(Si26)等でよい。またクリ
ーニングガスもClF3ガスに限定されるものではな
い。
Although monosilane (SiH 4 ) is shown as the deposition gas in the above example, examples of the deposition gas are phosphane (PH 3 ), arsine (AsH 3 ), diborane (B 2 H 6 ), disilane (Si 2 H 6). ) And so on. Also, the cleaning gas is not limited to ClF 3 gas.

【0030】[0030]

【発明の効果】以上説明したように請求項1に記載の発
明によれば、破過検知手段は通信回路を介して製造装置
から送られてくる排ガス放出指令の回数及び/又は排出
時間より破過を検知するので、構成が簡単で精度良い破
過検知装置を提供できる。
As described above, according to the first aspect of the present invention, the breakthrough detection means breaks from the number and / or the discharge time of the exhaust gas discharge command sent from the manufacturing apparatus through the communication circuit. Since the excess is detected, it is possible to provide an accurate breakthrough detection device having a simple structure.

【0031】また、請求項2に記載の発明によれば、破
過検知手段は排ガス放出指令の回数及び/又は排出時間
より破過を検知する手段に加え、ガス検知器で除害反応
槽から排出されるガス濃度を検知して破過を検知する手
段及び/又は反応槽の重量増加による破過を検知する手
段を具備するので、確実に破過を検知することができ、
排ガス処理装置から有害ガスが排出することを極力防止
できる。
According to the second aspect of the present invention, the breakthrough detection means is a means for detecting the breakthrough based on the number of exhaust gas discharge commands and / or the discharge time, and a gas detector is used to remove the detoxification reaction tank. Since a means for detecting the breakthrough by detecting the concentration of the discharged gas and / or a means for detecting the breakthrough due to the increase in the weight of the reaction tank is provided, the breakthrough can be surely detected.
It is possible to prevent harmful gas from being emitted from the exhaust gas treatment device as much as possible.

【0032】また、各請求項に記載の発明は、ClF3
ガスを使用したクリーニングに限定されず、バッチ式の
製造装置であればプロセスに関係なく精度良い破過検知
装置を提供できる。
The invention described in each claim is ClF 3
The invention is not limited to cleaning using gas, but a batch-type manufacturing apparatus can provide an accurate breakthrough detection apparatus regardless of the process.

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

【図1】本発明の破過検知装置を具備する排ガス処理装
置と半導体製造装置の間の信号の送受関係を示す図であ
る。
FIG. 1 is a diagram showing a signal transmission / reception relationship between an exhaust gas treatment apparatus equipped with a breakthrough detection device of the present invention and a semiconductor manufacturing apparatus.

【図2】本発明の破過検知装置を具備する排ガス処理装
置の構成を示す図である。
FIG. 2 is a diagram showing a configuration of an exhaust gas treatment apparatus including a breakthrough detection device of the present invention.

【図3】排ガス処理設備の概要を示す図である。FIG. 3 is a diagram showing an outline of an exhaust gas treatment facility.

【符号の説明】[Explanation of symbols]

1 バイパス弁 2 デポ側流入弁 3 クリーニング側流入弁 4 デポ側流出弁 5 クリーニング側流出弁 6 デポ側流出口弁 7 クリーニング側流出口弁 8 デポガス反応槽 9 クリーニングガス反応槽 11 流入口 12 デポ用流出口 13 クリーニング用流出口 14 N2流入口 15 バルブ 17 接点付流量計 19 ガス検知器 20 温度センサ 21 温度指示計 22 ガス検知器 23 温度センサ 24 温度指示計 25 重量計 26 荷重指示計 27 圧力スイッチ 28 圧力スイッチ 29 デポ用破過検知器 30 ClF3用破過検知器 31 ClF3用破過検知器 32 警報器 33 警報器 34 警報器 40 カウンター 103 半導体製造装置 105 排ガス処理装置1 Bypass Valve 2 Depot Side Inflow Valve 3 Cleaning Side Inflow Valve 4 Depot Side Outflow Valve 5 Cleaning Side Outflow Valve 6 Depot Side Outlet Valve 7 Cleaning Side Outlet Valve 8 Depot Gas Reaction Tank 9 Cleaning Gas Reaction Tank 11 Inlet 12 For Depot Outlet 13 Cleaning Outlet 14 N 2 Inlet 15 Valve 17 Flowmeter with Contact 19 Gas Detector 20 Temperature Sensor 21 Temperature Indicator 22 Gas Detector 23 Temperature Sensor 24 Temperature Indicator 25 Weight Scale 26 Load Indicator 27 Pressure switch 28 pressure switch 29 depot for breakthrough detector 30 ClF 3 for breakthrough detectors 31 ClF 3 for breakthrough detector 32 alarm device 33 alarms 34 alarm 40 counter 103 semiconductor manufacturing device 105 an exhaust gas treatment apparatus

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B01D 53/30 B01D 53/34 ─────────────────────────────────────────────────── ─── Continuation of the front page (58) Fields surveyed (Int.Cl. 7 , DB name) B01D 53/30 B01D 53/34

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 除害反応槽を具備し、製造装置と通信回
路で接続され、該製造装置との間で信号の送受を行いな
がら該製造装置から排出される製造プロセス排ガスを前
記除害反応槽で除害する排ガス処理装置の該除害反応槽
の交換時期である破過を検知する破過検知手段を具備す
る排ガス処理装置の破過検知装置において、 前記製造装置は製造プロセス排ガス排出1回当たりの排
出時間及び排出時の単位時間当たりの排出流量が予め設
定されており、 前記破過検知手段は前記通信回路を介して製造装置から
排ガス処理装置に送られてくる排ガス放出指令の回数及
び/又は放出時間より破過を検知することを特徴とする
排ガス処理装置の破過検知装置。
1. An abatement reaction tank, comprising a detoxification reaction tank, connected to a manufacturing apparatus by a communication circuit, and transmitting and receiving a signal to and from the manufacturing apparatus while producing process exhaust gas discharged from the manufacturing apparatus. In a breakthrough detection device for an exhaust gas treatment device, which comprises a breakthrough detection means for detecting breakthrough when it is time to replace the detoxification reaction tank of the exhaust gas treatment device for detoxification in a tank, the manufacturing device is a manufacturing process exhaust gas discharge 1 The discharge time per time and the discharge flow rate per unit time at the time of discharge are set in advance, and the breakthrough detection means is the number of exhaust gas emission commands sent from the manufacturing apparatus to the exhaust gas processing apparatus via the communication circuit. And / or a breakthrough detection device for an exhaust gas treatment device, which detects breakthrough based on a release time.
【請求項2】 前記破過検知手段は前記排ガス放出指令
の回数及び/又は放出時間より破過を検知する手段に加
え、ガス検知器で前記除害反応槽から排出される排ガス
濃度を検知して破過を検知する手段及び/又は反応槽の
重量増加より破過を検知する手段を具備することを特徴
とする請求項1に記載の排ガス処理装置の破過検知装
置。
2. The breakthrough detection means detects the concentration of exhaust gas discharged from the abatement reaction tank with a gas detector in addition to means for detecting breakthrough based on the number and / or release time of the exhaust gas discharge command. The breakthrough detection device for an exhaust gas treatment apparatus according to claim 1, further comprising: a means for detecting breakthrough and / or a means for detecting breakthrough based on an increase in weight of the reaction tank.
JP23336397A 1997-08-13 1997-08-13 Breakthrough detection device for exhaust gas treatment equipment Expired - Fee Related JP3373763B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23336397A JP3373763B2 (en) 1997-08-13 1997-08-13 Breakthrough detection device for exhaust gas treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23336397A JP3373763B2 (en) 1997-08-13 1997-08-13 Breakthrough detection device for exhaust gas treatment equipment

Publications (2)

Publication Number Publication Date
JPH1157386A JPH1157386A (en) 1999-03-02
JP3373763B2 true JP3373763B2 (en) 2003-02-04

Family

ID=16953978

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23336397A Expired - Fee Related JP3373763B2 (en) 1997-08-13 1997-08-13 Breakthrough detection device for exhaust gas treatment equipment

Country Status (1)

Country Link
JP (1) JP3373763B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4707421B2 (en) 2005-03-14 2011-06-22 東京エレクトロン株式会社 Processing apparatus, consumable part management method for processing apparatus, processing system, and consumable part management method for processing system
JP4963817B2 (en) * 2005-09-21 2012-06-27 株式会社日立国際電気 Substrate processing equipment

Also Published As

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