JPH09150008A - Treating liquid supply device - Google Patents
Treating liquid supply deviceInfo
- Publication number
- JPH09150008A JPH09150008A JP7338235A JP33823595A JPH09150008A JP H09150008 A JPH09150008 A JP H09150008A JP 7338235 A JP7338235 A JP 7338235A JP 33823595 A JP33823595 A JP 33823595A JP H09150008 A JPH09150008 A JP H09150008A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- pipe
- degassing
- processing liquid
- vacuum chamber
- 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.)
- Granted
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 219
- 238000007872 degassing Methods 0.000 claims description 127
- 238000001514 detection method Methods 0.000 claims description 35
- 239000000463 material Substances 0.000 claims description 13
- 239000012528 membrane Substances 0.000 claims description 11
- 238000007599 discharging Methods 0.000 claims description 4
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 230000002159 abnormal effect Effects 0.000 abstract description 5
- 230000006378 damage Effects 0.000 abstract description 2
- 230000006866 deterioration Effects 0.000 abstract description 2
- 230000004941 influx Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 23
- 239000000758 substrate Substances 0.000 description 13
- 230000018109 developmental process Effects 0.000 description 9
- 230000005856 abnormality Effects 0.000 description 8
- 238000000576 coating method Methods 0.000 description 7
- 239000011248 coating agent Substances 0.000 description 6
- 229920002120 photoresistant polymer Polymers 0.000 description 6
- 238000004891 communication Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- 230000032683 aging Effects 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000004065 semiconductor Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000007688 edging Methods 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000009972 noncorrosive effect Effects 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Degasification And Air Bubble Elimination (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、被処理物、例え
ば半導体ウエハ、液晶表示装置(LCD)用ガラス基
板、フォトマスク用ガラス基板、光ディスク用基板など
の各種基板の表面に現像液、フォトレジスト液、純水等
の洗浄液などの処理液を供給する処理液供給装置に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a surface of various substrates such as a semiconductor wafer, a glass substrate for a liquid crystal display (LCD), a glass substrate for a photomask, a substrate for an optical disk, a developing solution and a photoresist. The present invention relates to a processing liquid supply device that supplies a processing liquid such as a cleaning liquid such as liquid or pure water.
【0002】[0002]
【従来の技術】例えば、半導体ウエハ、LCD用ガラス
基板等の基板を水平姿勢に保持して鉛直軸回りに回転さ
せながら、その基板表面に被着形成されたフォトレジス
ト膜を現像処理する場合、現像液は現像液供給源からフ
ィルタ等が介挿された送液用配管を通して吐出ノズルへ
送給され、吐出ノズルの吐出口から基板の表面へ供給さ
れるようになっている。そして、現像むらが生じないよ
うに、現像液が基板の表面全体にわたって均一に供給さ
れるように制御している。2. Description of the Related Art For example, when developing a photoresist film deposited on the surface of a substrate such as a semiconductor wafer or a glass substrate for LCD while holding the substrate in a horizontal posture and rotating it about a vertical axis, The developer is supplied from the developer supply source to the discharge nozzle through a liquid supply pipe in which a filter or the like is inserted, and is supplied from the discharge port of the discharge nozzle to the surface of the substrate. Then, the developer is controlled so as to be uniformly supplied over the entire surface of the substrate so as to prevent uneven development.
【0003】ところが、送液用配管内にエアーが噛んだ
り送液用配管内を流れる現像液中に気体が溶存したりす
ることがあり、この現像液をそのまま吐出ノズルから基
板の表面へ供給すると、現像液中の気体が基板上のフォ
トレジスト膜面に気泡として付着することになる。この
結果、気泡の付着部位における現像処理が阻害され、現
像不良を起こすことになる。これと同様の問題は、現像
処理に限らず各種処理工程においても起こり、例えば、
フォトレジスト液の塗布工程では、フォトレジスト液中
に気体が溶存していると、塗布むらの原因となる。However, air may be trapped in the liquid sending pipe or gas may be dissolved in the developing liquid flowing in the liquid sending pipe, and if this developing liquid is directly supplied from the discharge nozzle to the surface of the substrate. The gas in the developer adheres to the surface of the photoresist film on the substrate as bubbles. As a result, the development process at the air bubble adhesion site is hindered, resulting in poor development. Problems similar to this occur not only in the development processing but also in various processing steps.
In the photoresist liquid coating process, if gas is dissolved in the photoresist liquid, it causes uneven coating.
【0004】そこで、送液用配管内にエアーが噛んだり
処理液中に気体が溶存したりもすることによって引き起
こされる処理不良を無くすために、図2に示すように、
処理液供給源から処理液の吐出口へ至る送液用配管1の
途中に脱気モジュール2を介設して、その脱気モジュー
ル2を処理液が通過する際に処理液中の気体を除去し、
気体が溶存していない状態の処理液が吐出口から基板上
へ供給されるようにしている。図2に概略断面図を示し
た脱気モジュール2は、送液用配管1にそれぞれ流路接
続された入口側継手部3及び出口側継手部4、非腐食性
素材、例えば四フッ化エチレン樹脂からなる気体透過膜
材によって形成され、互いに平行に配設されてそれぞれ
両端部が両継手部3、4に連通された多数の細管で構成
された液流路5、並びに、この液流路5を内部に収容し
その周囲を気密に密閉した真空チャンバ6から構成され
ている。そして、脱気モジュール2に、その真空チャン
バ6内の密閉空間に連通するように脱気用配管7を接続
し、脱気用配管7を真空ポンプや工場内の真空ラインな
どの真空吸引源に接続している。脱気用配管7には、必
要により、真空チャンバ6内を真空吸引する真空圧を所
定値に調整して接続するための調圧弁8が介設される。Therefore, as shown in FIG. 2, in order to eliminate processing defects caused by air trapped in the liquid supply pipe or gas dissolved in the processing liquid, as shown in FIG.
A degassing module 2 is provided in the middle of the liquid sending pipe 1 from the processing liquid supply source to the processing liquid discharge port, and the gas in the processing liquid is removed when the processing liquid passes through the degassing module 2. Then
The processing liquid in which gas is not dissolved is supplied onto the substrate from the discharge port. The degassing module 2 whose schematic cross-sectional view is shown in FIG. 2 includes an inlet-side joint portion 3 and an outlet-side joint portion 4, which are flow-path-connected to the liquid-sending pipe 1, a non-corrosive material such as tetrafluoroethylene resin And a liquid flow path 5 composed of a large number of thin tubes which are formed of a gas permeable membrane material and which are arranged in parallel with each other and have both ends communicating with the joint parts 3 and 4, respectively. Is housed inside and the periphery thereof is hermetically sealed. Then, the deaeration module 2 is connected to the deaeration pipe 7 so as to communicate with the closed space in the vacuum chamber 6, and the deaeration pipe 7 is used as a vacuum suction source such as a vacuum pump or a vacuum line in a factory. Connected. A pressure regulating valve 8 for adjusting the vacuum pressure for vacuuming the inside of the vacuum chamber 6 to a predetermined value and connecting the degassing pipe 7 is provided in the degassing pipe 7 if necessary.
【0005】この脱気モジュール2に、処理液供給源か
ら送液用配管1を通って送給される現像液、フォトレジ
スト液、洗浄用純水などの処理液を流すと、気体透過膜
材によって形成された多数の細管からなる液流路5を処
理液が流れる間に、処理液中に溶存する空気等の気体が
細管の気体透過膜材を通し、真空下に保持された真空チ
ャンバ6内の密閉空間へ効果的に除去される。このよう
に、処理液は脱気モジュール2に連続して通される間に
速やかに脱気処理され、脱気処理された処理液が脱気モ
ジュール2の出口から排出されて送液用配管1内へ送り
出される。When a processing solution such as a developing solution, a photoresist solution, pure water for cleaning supplied from a processing solution supply source through the solution sending pipe 1 is flown into the degassing module 2, a gas permeable film material is obtained. While the processing liquid is flowing through the liquid flow path 5 composed of a large number of thin tubes formed by the above, a gas, such as air, dissolved in the processing liquid passes through the gas permeable membrane material of the thin tubes and is held in a vacuum chamber 6 under vacuum. Effectively removed into the enclosed space inside. As described above, the treatment liquid is quickly degassed while being continuously passed through the degassing module 2, and the degassed treatment liquid is discharged from the outlet of the degassing module 2 and the liquid sending pipe 1 Is sent in.
【0006】[0006]
【発明が解決しようとする課題】ところで、図2に示し
たような処理液供給装置を使用しているうちに、脱気モ
ジュール2の液流路5を構成している気体透過膜材から
なる細管が経時変化等によって破損した場合などには、
脱気モジュール2を通して処理液を流しても、処理液中
の気体は除去されず、脱気されないままの処理液が送液
用配管1の先端の吐出ノズルから基板の表面へ供給され
ることになり、現像不良や塗布むら等の原因となる。そ
して、このような状態をそのまま続けていると、歩留ま
りが著しく低下することとなる。By the way, while using the treatment liquid supply apparatus as shown in FIG. 2, the gas flow permeable membrane material constituting the liquid flow path 5 of the degassing module 2 is used. If the thin tube is damaged due to aging, etc.,
Even if the processing liquid is flown through the degassing module 2, the gas in the processing liquid is not removed, and the processing liquid that has not been degassed is supplied to the surface of the substrate from the discharge nozzle at the tip of the liquid supply pipe 1. And cause defective development and uneven coating. And if such a state is continued as it is, the yield will be remarkably reduced.
【0007】尚、脱気モジュール2における脱気能力の
低下を確実に知る方法は、従来特に無く、溶存窒素計を
使用して、送液用配管1の、脱気モジュール2より下流
側おいて処理液中に溶存している窒素ガス量を測定す
る、といった方法が考えられるが、その方法も信頼性に
欠ける。Incidentally, there is no particular method for surely knowing the decrease in the deaeration capacity of the deaeration module 2, and a dissolved nitrogen meter is used to place the degassing module 2 downstream of the deaeration module 2. A method of measuring the amount of nitrogen gas dissolved in the treatment liquid can be considered, but that method also lacks reliability.
【0008】また、脱気モジュール2の真空チャンバ6
に接続された脱気用配管7内には、真空チャンバ6内の
密閉空間から極く少量の液が滲み出すことがあり、従
来、その滲み出た液は、そのまま脱気用配管7を通って
真空吸引源、例えば工場内の真空ライン設備へ流れ込む
ようになっていた。そして、通常の状態では、その液の
滲み出し量は極く少量であるため、特に問題にはならな
い。ところが、脱気モジュール2の液流路5を構成して
いる気体透過膜材からなる細管が経時変化によって破損
した場合などの異常時には、大量の処理液が脱気用配管
7を通って真空設備側へ流れ込むことになる。この結
果、設備に多大のダメージを与えることになる。また、
真空設備を保護するために、真空吸引源として比較的安
価なエジェクタを使用することが考えられるが、その場
合には、上記した異常時において多量の気液混合流が発
生することになる。このため、ドレン回収が困難にな
り、もしくは、そのために複雑なシステムが必要になっ
てくる、といった問題点がある。Further, the vacuum chamber 6 of the degassing module 2
A very small amount of liquid may exude from the closed space in the vacuum chamber 6 into the degassing pipe 7 connected to the. The exuded liquid has conventionally passed through the degassing pipe 7 as it is. It was designed to flow into a vacuum suction source, such as a vacuum line facility in a factory. In a normal state, the amount of the exuded liquid is extremely small, so that there is no particular problem. However, in the event of an abnormality such as when the thin tube made of the gas permeable membrane material that constitutes the liquid flow path 5 of the degassing module 2 is damaged due to aging, a large amount of processing liquid passes through the degassing pipe 7 and vacuum equipment is installed. It will flow to the side. As a result, the equipment is greatly damaged. Also,
In order to protect the vacuum equipment, a relatively inexpensive ejector may be used as a vacuum suction source, but in that case, a large amount of gas-liquid mixed flow will be generated in the above-mentioned abnormal time. Therefore, there is a problem that it becomes difficult to collect the drain, or a complicated system is required for that.
【0009】この発明は、以上のような事情に鑑みてな
されたものであり、脱気モジュールの液流路の破損など
が起こった場合に、その異常を確実に検知して、脱気モ
ジュールにおける脱気能力の低下によって引き起こされ
る不都合を回避することができる処理液供給装置を提供
することを第1の目的とする。The present invention has been made in view of the above circumstances, and in the case where the liquid flow path of the degassing module is damaged, the abnormality is surely detected and the degassing module is operated. A first object of the present invention is to provide a treatment liquid supply device capable of avoiding the inconvenience caused by the deterioration of the degassing ability.
【0010】また、この発明は、脱気モジュールの液流
路の破損などが起こった場合に、大量の処理液が脱気モ
ジュールから脱気用配管を通って真空吸引源である真空
設備側へ流れ込むのを防止して、設備にダメージを与え
ることがない処理液供給装置を提供することを第2の目
的とする。Further, according to the present invention, when the liquid flow path of the degassing module is damaged, a large amount of processing liquid is passed from the degassing module to the vacuum equipment side which is a vacuum suction source through the degassing pipe. A second object is to provide a processing liquid supply apparatus that prevents the liquid from flowing into the equipment and does not damage the equipment.
【0011】[0011]
【課題を解決するための手段】請求項1に係る発明は、
処理液を送給する送液用配管と、この送液用配管の途中
に介挿され、気体透過膜材によって形成され入口と出口
とを連通させる液流路を有し、その液流路の周囲を真空
チャンバで気密に密閉してなる脱気モジュールと、この
脱気モジュールの前記真空チャンバ内の密閉空間を真空
吸引源に接続する脱気用配管とを備えた処理液供給装置
において、前記脱気用配管内に前記脱気モジュールの真
空チャンバ内から処理液が流入したことを検知する検知
手段を設け、その検知手段から出力される検知信号に基
づいて前記脱気用配管内への処理液の流入を報知する報
知手段を設けたことを特徴とする。The invention according to claim 1 is
A liquid-feeding pipe for feeding the treatment liquid, and a liquid-flow passage that is inserted in the middle of the liquid-feeding pipe and is formed of a gas-permeable membrane material and connects the inlet and the outlet, In a processing liquid supply device comprising a degassing module that hermetically seals the surroundings in a vacuum chamber, and a degassing pipe that connects a sealed space in the vacuum chamber of the degassing module to a vacuum suction source, A detection unit is provided in the degassing pipe to detect that the processing liquid has flowed from the vacuum chamber of the degassing module, and the process into the degassing pipe is performed based on a detection signal output from the detection unit. It is characterized in that a notifying means for notifying the inflow of the liquid is provided.
【0012】請求項2に係る発明は、請求項1記載の処
理液供給装置において、脱気用配管及び/又は送液用配
管の、脱気モジュールより上流側に、常時は開かれ検知
手段の検知信号により閉じられる緊急遮断弁を介設した
ことを特徴とする。According to a second aspect of the present invention, in the treatment liquid supply apparatus according to the first aspect, the degassing pipe and / or the liquid sending pipe is always opened upstream of the degassing module and has a detecting means. It is characterized in that an emergency shutoff valve that is closed by a detection signal is provided.
【0013】請求項3に係る発明は、処理液を送給する
送液用配管と、この送液用配管の途中に介挿され、気体
透過膜材によって形成され入口と出口とを連通させる液
流路を有し、その液流路の周囲を真空チャンバで気密に
密閉してなる脱気モジュールと、この脱気モジュールの
前記真空チャンバ内の密閉空間を真空吸引源に接続する
脱気用配管とを備えた処理液供給装置において、前記脱
気用配管の途中に、前記脱気モジュールの真空チャンバ
内から脱気用配管内へ流入した処理液を気体から分離し
貯留して真空吸引源の方へ処理液が流れ込むのを防止す
る液溜め部を介設したことを特徴とする。According to a third aspect of the present invention, there is provided a liquid feed pipe for feeding a treatment liquid, and a liquid which is inserted in the middle of the liquid feed pipe and which is formed of a gas permeable membrane material and which connects the inlet and the outlet. A degassing module having a flow path and hermetically sealing the periphery of the liquid flow path in a vacuum chamber, and a degassing pipe connecting a closed space in the vacuum chamber of the degassing module to a vacuum suction source. In the treatment liquid supply apparatus including, in the middle of the degassing pipe, the treatment liquid that has flowed into the degassing pipe from the vacuum chamber of the degassing module is separated from the gas and stored to be a vacuum suction source. It is characterized in that a liquid reservoir portion for preventing the processing liquid from flowing inward is provided.
【0014】請求項4に係る発明は、請求項3記載の処
理液供給装置において、液溜め部に、その内部に貯留さ
れた処理液が所定量に達したことを検知する貯留量検知
手段を設け、その貯留量検知手段から出力される検知信
号に基づいて前記液溜め部に処理液が所定量貯留された
ことを報知する貯留量報知手段を設けたことを特徴とす
る。According to a fourth aspect of the present invention, in the treatment liquid supply apparatus according to the third aspect, a storage amount detecting means for detecting that the treatment liquid stored therein reaches a predetermined amount is provided in the liquid reservoir. And a storage amount notifying unit for notifying that a predetermined amount of the processing liquid has been stored in the liquid storage unit based on a detection signal output from the storage amount detecting unit.
【0015】請求項5に係る発明は、請求項3又は請求
項4記載の処理液供給装置において、液溜め部の底部
に、液溜め部に溜まった液体を排出するためのドレン排
出用配管を接続し、そのドレン排出用配管に開閉弁を介
設したことを特徴とする。According to a fifth aspect of the invention, in the treatment liquid supply apparatus according to the third or fourth aspect, a drain discharge pipe for discharging the liquid accumulated in the liquid reservoir is provided at the bottom of the liquid reservoir. It is characterized in that it is connected and an on-off valve is provided in the drain discharge pipe.
【0016】ここで、脱気モジュールの液流路を形成し
ている気体透過膜材が破損した場合などには、脱気モジ
ュールの真空チャンバ内から脱気用配管内へ処理液が流
入してくる。上記した請求項1に係る発明の処理液供給
装置では、検知手段により脱気用配配管内へ処理液が流
入したことが検知され、その脱気用配管内への処理液の
流入が報知手段によって作業者に知らされる。従って、
作業者が被処理物への処理液の供給を停止させることに
より、脱気されないままの処理液が被処理物上へ供給さ
れて現像不良や塗布むらなどを生じる、といった不都合
を回避することが可能になる。When the gas permeable membrane material forming the liquid flow path of the degassing module is damaged, the processing liquid flows from the vacuum chamber of the degassing module into the degassing pipe. come. In the processing liquid supply apparatus of the invention according to the above-mentioned claim 1, the detection means detects that the processing liquid has flowed into the degassing distribution pipe, and the inflow means of the processing liquid has flowed into the degassing pipe. Informs the operator. Therefore,
By stopping the supply of the processing liquid to the object to be processed by the worker, it is possible to avoid the inconvenience that the processing liquid that has not been degassed is supplied onto the object to be processed, resulting in poor development and uneven coating. It will be possible.
【0017】請求項2に係る発明の処理液供給装置で
は、検知手段により脱気用配配管内への処理液の流入が
検知された時に、脱気用配管及び/又は送液用配管の、
脱気モジュールより上流側に介設された緊急遮断弁が閉
じられる。これにより、脱気用配配管内へ流入した処理
液が真空吸引源の方へ流れ込むのが防止され、及び/又
は、処理液供給源から送液用配管を通って処理液が脱気
モジュール内へ流れるのが止められて、脱気モジュール
から脱気用配管内への処理液の流入が停止する。In the treatment liquid supply apparatus according to the second aspect of the invention, when the detection means detects the inflow of the treatment liquid into the degassing distribution pipe, the degassing pipe and / or the liquid sending pipe are
The emergency shutoff valve installed upstream of the degassing module is closed. This prevents the processing liquid that has flowed into the degassing distribution pipe from flowing into the vacuum suction source, and / or the processing liquid from the processing liquid supply source through the liquid sending pipe into the degassing module. Is stopped and the inflow of the processing liquid from the degassing module into the degassing pipe is stopped.
【0018】請求項3に係る発明の処理液供給装置で
は、脱気モジュールの液流路を形成している気体透過膜
材が破損して脱気モジュールの真空チャンバ内から脱気
用配管内へ処理液が流入したときに、その処理液は、脱
気用配管の途中に介設された液溜め部に流れ込み、液溜
め部において気体から分離されて貯留される。このた
め、脱気モジュールから脱気用配管内へ流入した処理液
をそのまま真空吸引源の方へ流れ込むのが防止される。In the treatment liquid supply apparatus according to the third aspect of the present invention, the gas permeable membrane material forming the liquid flow path of the degassing module is damaged and the vacuum chamber of the degassing module moves into the degassing pipe. When the treatment liquid flows in, the treatment liquid flows into a liquid reservoir provided in the middle of the degassing pipe, and is separated from the gas and stored in the liquid reservoir. Therefore, it is possible to prevent the processing liquid flowing from the degassing module into the degassing pipe from flowing into the vacuum suction source as it is.
【0019】請求項4に係る発明の処理液供給装置で
は、脱気モジュールから脱気用配管内へ流入して液溜め
部の内部に貯留された処理液が所定量に達した時に、そ
のことが貯留量検知手段によって検知され貯留量報知手
段によって作業者に知らされる。これにより、作業者
は、脱気モジュールに異常が発生したことを知り、被処
理物への処理液の供給を停止させることにより、脱気さ
れないままの処理液が被処理物上へ供給されて現像不良
や塗布むらなどを生じる、といった不都合を回避するこ
とが可能になる。In the treatment liquid supply apparatus according to the fourth aspect of the invention, when the treatment liquid flowing from the degassing module into the degassing pipe and stored in the liquid reservoir reaches a predetermined amount, Is detected by the storage amount detecting means, and the worker is notified by the storage amount notifying means. As a result, the worker knows that an abnormality has occurred in the degassing module, and by stopping the supply of the processing liquid to the object to be processed, the processing liquid that has not been degassed is supplied onto the object to be processed. It is possible to avoid inconveniences such as poor development and uneven coating.
【0020】通常の状態においても、脱気モジュールの
真空チャンバ内から脱気用配管内へ極く少量の液が滲み
出すことがあり、また、脱気用配管内で結露が生じるこ
ともある。その液の量は極く僅かであるが、長い期間が
経過するうちに液溜め部内に次第に液が溜まってくる。
請求項5に係る発明の処理液供給装置では、液溜め部の
底部に接続されたドレン排出用配管に介設された開閉弁
を開くことにより、液溜め部内に溜まった液がドレン排
出用配管を通して排出される。特に、液溜め部に貯留量
検知手段が設けられているような場合には、液溜め部内
に溜まった液を定期的に排出するようにすることによ
り、定常時における液溜め部内の液の貯留によって貯留
量検知手段が誤動作することが無くなり、異常時におけ
る液溜め部への処理液の流入だけを確実に検知すること
が可能になる。Even in a normal state, a very small amount of liquid may exude from the vacuum chamber of the degassing module into the degassing pipe, and dew condensation may occur in the degassing pipe. Although the amount of the liquid is extremely small, the liquid gradually accumulates in the liquid reservoir over a long period of time.
In the treatment liquid supply apparatus according to the fifth aspect of the present invention, the on-off valve provided in the drain discharge pipe connected to the bottom of the liquid reservoir is opened so that the liquid accumulated in the liquid reservoir is drained. Exhausted through. In particular, when a storage amount detecting means is provided in the liquid reservoir, the liquid accumulated in the liquid reservoir is periodically discharged so that the liquid is stored in the liquid reservoir in a steady state. As a result, the storage amount detection means does not malfunction, and it becomes possible to reliably detect only the inflow of the processing liquid into the liquid storage section at the time of an abnormality.
【0021】[0021]
【発明の実施の形態】以下、この発明の最良の実施形態
について図1を参照しながら説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The best embodiment of the present invention will be described below with reference to FIG.
【0022】図1は、この発明の実施形態の1例を示す
処理液供給装置の概略構成図である。この装置は、処理
液供給源から処理液の吐出口へ至る送液用配管1の途中
に脱気モジュール2が介挿されている。脱気モジュール
2の構成は、図2に基づいて上述した処理液供給装置と
同じであり、また、処理液の脱気作用も同様に行なわれ
るので、ここではその説明を省略する。脱気モジュール
2の真空チャンバには、その密閉空間に連通するように
脱気用配管10が接続されており、脱気用配管10は真
空吸引源、例えば工場内の真空ラインや真空ポンプなど
に接続されている。尚、脱気モジュールの構成は、上記
説明したものに限定されず、同様の脱気作用が得られる
ものであれば、どのような構成のものであってもよい。FIG. 1 is a schematic configuration diagram of a processing liquid supply apparatus showing an example of an embodiment of the present invention. In this apparatus, a degassing module 2 is inserted in the middle of a liquid sending pipe 1 from a processing liquid supply source to a processing liquid discharge port. The configuration of the degassing module 2 is the same as that of the processing liquid supply device described above with reference to FIG. 2, and the degassing action of the processing liquid is also performed in the same manner, and therefore the description thereof is omitted here. A degassing pipe 10 is connected to the vacuum chamber of the degassing module 2 so as to communicate with the closed space, and the degassing pipe 10 is connected to a vacuum suction source such as a vacuum line or a vacuum pump in a factory. It is connected. The configuration of the degassing module is not limited to that described above, and may have any configuration as long as the same degassing action can be obtained.
【0023】この処理液供給装置では、脱気用配管10
に気液分離して液を溜めるトラップタンク12が介設さ
れている。また、脱気用配管10には、トラップタンク
12より真空吸引源側に、常時は開かれ異常時に閉じら
れる緊急遮断弁14が介設されている。また、送液用配
管1にも、常時は開かれ異常時に閉じられる緊急遮断弁
16が介設されているが、緊急遮断弁は、脱気用配管1
0又は送液用配管1の何れか一方だけに設けるようにし
てもよい。In this treatment liquid supply apparatus, the degassing pipe 10 is used.
A trap tank 12 that separates gas and liquid and stores the liquid is interposed. Further, the degassing pipe 10 is provided with an emergency shutoff valve 14 which is normally opened and closed in an abnormal state on the vacuum suction source side of the trap tank 12. Further, the liquid delivery pipe 1 is also provided with an emergency shutoff valve 16 that is normally opened and closed in an abnormal state. The emergency shutoff valve is used as the degassing pipe 1.
It may be provided in only one of 0 and the liquid sending pipe 1.
【0024】トラップタンク12の底部には、タンク内
に溜まった液体を排出するためのドレン排出用配管18
が連通接続されており、そのドレン排出用配管18に開
閉弁20が介設されている。トラップタンク12の上部
には、大気に連通した大気連通配管22が連通接続され
ており、その大気連通配管22に大気開放弁24が介設
されている。また、脱気用配管10の、トラップタンク
12と脱気モジュール2の真空チャンバとの間に縁切り
弁30が介設されている。At the bottom of the trap tank 12, a drain discharge pipe 18 for discharging the liquid accumulated in the tank
Are connected in communication with each other, and an on-off valve 20 is provided in the drain discharge pipe 18. An atmosphere communication pipe 22 that communicates with the atmosphere is communicatively connected to the upper portion of the trap tank 12, and an atmosphere release valve 24 is provided in the atmosphere communication pipe 22. Further, an edge cutoff valve 30 is provided between the trap tank 12 of the degassing pipe 10 and the vacuum chamber of the degassing module 2.
【0025】また、トラップタンク12には、そのタン
ク内に貯留された処理液が所定量に達したことを検知す
る貯留量検知センサ32が設けられている。貯留量検知
センサ32としては、フロートスイッチ方式、光電方
式、静電容量方式等のうちの何れか適当な方式のものを
使用すればよい。貯留量検知センサ32から出力される
検知信号は、CPU34に送られるようになっている。
そして、緊急遮断弁14、16、開閉弁20、大気開放
弁24及び縁切り弁30の開閉がそれぞれCPU34に
よって制御される。また、CPU34には、貯留量検知
センサ32からの検知信号に基づいてトラップタンク1
2に処理液が所定量貯留されたことを報知する警報器3
6が接続されている。Further, the trap tank 12 is provided with a storage amount detection sensor 32 for detecting that the processing liquid stored in the tank has reached a predetermined amount. As the storage amount detection sensor 32, any one of a float switch system, a photoelectric system, an electrostatic capacity system and the like may be used. The detection signal output from the storage amount detection sensor 32 is sent to the CPU 34.
The CPU 34 controls opening / closing of the emergency shutoff valves 14 and 16, the opening / closing valve 20, the atmosphere opening valve 24, and the edging valve 30. Further, the CPU 34 notifies the trap tank 1 based on the detection signal from the storage amount detection sensor 32.
Alarm device 3 for notifying that a predetermined amount of processing liquid is stored in 2.
6 are connected.
【0026】次に、図1に示した処理液供給装置におい
て、脱気モジュール2の液流路を構成している気体透過
膜材からなる細管が破損した場合における動作について
説明する。Next, the operation of the treatment liquid supply apparatus shown in FIG. 1 when the thin tube made of the gas permeable membrane material forming the liquid flow path of the degassing module 2 is broken will be described.
【0027】常時は、緊急遮断弁14、16及び縁切り
弁30はそれぞれ開かれており、開閉弁20及び大気開
放弁24はそれぞれ閉じられている。脱気モジュール2
の液流路の細管が破損すると、その破損部分から処理液
が流出し、脱気モジュール2の真空チャンバ内から脱気
用配管10内へ処理液が流入してくる。脱気用配管10
内へ流入してきた処理液は、トラップタンク12内へ流
れ込み、トラップタンク12において気体から分離され
て貯留される。従って、気体だけが真空吸引源によって
吸引され、脱気モジュール2から脱気用配管10内へ流
入した処理液がそのまま真空吸引源の方へ流れ込むこと
はない。脱気モジュール2から脱気用配管10内へ流入
してトラップタンク12内に貯留された処理液が所定量
に達すると、貯留量検知センサ32によってそれが検知
され、その検知信号がCPU34へ送られる。そして、
CPU34から警報器36へ信号が送られて、警報器3
6が作動して、異常事態の発生が作業者に知らされる。
これと同時に、CPU34から緊急遮断弁14、16へ
制御信号が送られ、緊急遮断弁14、16が閉じられ
る。これにより、真空吸引源と脱気モジュール2の真空
チャンバ内部との連通が遮断されるとともに、処理液供
給源から送液用配管1を通って処理液が脱気モジュール
2内へ流れるのが止められて、脱気モジュール2から脱
気用配管10内への処理液の流入が停止する。そして、
作業者は、警報器36からの警報を受けて、処理液供給
装置の運転を完全に停止させる。At normal times, the emergency shutoff valves 14 and 16 and the edge cutoff valve 30 are open, and the open / close valve 20 and the atmosphere open valve 24 are closed. Degas module 2
When the thin tube of the liquid flow path is damaged, the processing liquid flows out from the damaged part, and the processing liquid flows from the vacuum chamber of the degassing module 2 into the degassing pipe 10. Degassing pipe 10
The processing liquid that has flowed in flows into the trap tank 12, is separated from the gas in the trap tank 12, and is stored. Therefore, only the gas is sucked by the vacuum suction source, and the processing liquid flowing from the degassing module 2 into the degassing pipe 10 does not flow directly to the vacuum suction source. When the treatment liquid flowing from the degassing module 2 into the degassing pipe 10 and stored in the trap tank 12 reaches a predetermined amount, the storage amount detection sensor 32 detects it and sends the detection signal to the CPU 34. To be And
A signal is sent from the CPU 34 to the alarm device 36, and the alarm device 3
6 is activated to notify the operator of the occurrence of the abnormal situation.
At the same time, a control signal is sent from the CPU 34 to the emergency shutoff valves 14 and 16, and the emergency shutoff valves 14 and 16 are closed. As a result, the communication between the vacuum suction source and the inside of the vacuum chamber of the degassing module 2 is cut off, and the processing liquid stops flowing from the processing liquid supply source through the liquid sending pipe 1 into the degassing module 2. Then, the inflow of the processing liquid from the degassing module 2 into the degassing pipe 10 is stopped. And
Upon receiving the alarm from the alarm device 36, the worker completely stops the operation of the processing liquid supply device.
【0028】処理液供給装置の運転が停止すると、縁切
り弁30を閉じるとともに、大気開放弁24及び開閉弁
20をそれぞれ開く。これにより、トラップタンク12
内に溜まった処理液は、ドレン排出用配管18を通って
外部へ排出される。そして、破損した脱気モジュール2
を新しいものと交換するなどの必要な処置を行なう。ド
レンの排出が終わると、再び、開閉弁20及び大気開放
弁24がそれぞれ閉じられ、縁切り弁30が開かれる。
そして、緊急遮断弁14、16が元の状態に復帰され、
処理液供給装置の運転が再開される。When the operation of the processing liquid supply device is stopped, the edge cutoff valve 30 is closed and the atmosphere opening valve 24 and the opening / closing valve 20 are opened. As a result, the trap tank 12
The processing liquid accumulated inside is discharged to the outside through the drain discharge pipe 18. And the damaged degassing module 2
Take the necessary measures such as replacing with a new one. When drainage is completed, the on-off valve 20 and the atmosphere release valve 24 are closed again and the rim cut valve 30 is opened again.
Then, the emergency shutoff valves 14 and 16 are returned to their original states,
The operation of the processing liquid supply device is restarted.
【0029】尚、通常の状態においても、脱気モジュー
ル2の真空チャンバ内から脱気用配管10内へ極く少量
の液が滲み出したり、脱気用配管10内で結露が生じた
りして、長い期間が経過するうちにトラップタンク12
内に次第に液が溜まることがある。このような場合に
は、定期的に、大気開放弁24及び開閉弁20をそれぞ
れ開くことにより、トラップタンク12内に溜まった液
がドレン排出用配管18を通って排出されるようにする
とよい。このようにすると、定常時におけるトラップタ
ンク12内の液の貯留によって貯留量検知センサ32が
作動することがなくなるので、異常時におけるトラップ
タンク12への処理液の流入だけを貯留量検知センサ3
2が確実に検知することになる。Even in a normal state, a very small amount of liquid may seep out of the vacuum chamber of the degassing module 2 into the degassing pipe 10, or dew may condense in the degassing pipe 10. , Over a long period of time, the trap tank 12
Liquid may gradually accumulate inside. In such a case, it is preferable to periodically open the atmosphere opening valve 24 and the opening / closing valve 20 so that the liquid accumulated in the trap tank 12 is discharged through the drain discharge pipe 18. In this case, the storage amount detection sensor 32 does not operate due to the storage of the liquid in the trap tank 12 in a steady state, so that only the storage amount detection sensor 3 detects the inflow of the processing liquid into the trap tank 12 at the time of abnormality.
2 will definitely detect.
【0030】図1に示した装置では、脱気用配管10に
トラップタンク12を介設するようにしたが、例えば、
脱気用配管の一部をU字形に屈曲させて、その屈曲部を
トラップ部とするようにしてもよい。また、脱気用配管
10を途中でドレン排出用配管18と分岐させて処理液
を気体から分離し、ドレン排出用配管18に設けた開閉
弁20より上流に処理液を溜めるようにして液溜め部を
構成し、ドレン排出用配管18に貯留した処理液を貯留
量検知センサ32で検知するようにしてもよい。また、
開閉弁20、大気開放弁24及び縁切り弁30の切換え
操作は、自動でなく手動で行なわせるようにしてもよ
い。さらに、CPU34からの信号によって作動する緊
急遮断弁14、16を特に設けずに、警報器36の警報
によって作業者が、送液用配管1又は脱気用配管10に
設けられた開閉弁を手動で閉じるようにしてもよい。ま
た、貯留量検知センサ32やドレン排出用配管18は、
特に必要が無ければ設けなくても構わない。In the apparatus shown in FIG. 1, the trap tank 12 is provided in the degassing pipe 10, but, for example,
A part of the degassing pipe may be bent in a U shape so that the bent portion serves as a trap portion. Further, the degassing pipe 10 is branched along the way with the drain discharge pipe 18 to separate the processing liquid from the gas, and the processing liquid is collected upstream of the on-off valve 20 provided in the drain discharge pipe 18. Alternatively, the processing liquid stored in the drain discharge pipe 18 may be detected by the storage amount detection sensor 32. Also,
The switching operation of the opening / closing valve 20, the atmosphere opening valve 24, and the edge cutoff valve 30 may be performed manually instead of automatically. Further, the operator does not manually provide the emergency shutoff valves 14 and 16 which are operated by the signal from the CPU 34, but the operator manually operates the open / close valve provided in the liquid sending pipe 1 or the degassing pipe 10 by the alarm of the alarm device 36. You may close it with. Further, the storage amount detection sensor 32 and the drain discharge pipe 18 are
If it is not necessary, it may not be provided.
【0031】以上説明した実施形態は、脱気用配管10
にトラップタンク12を介設して、真空吸引源側へ処理
液が流れ込まないようにしたものであるが、脱気用配管
にトラップタンクのような液溜め部を設けずに、単に、
脱気用配管に、その配管内に脱気モジュールの真空チャ
ンバ内から処理液が流入したことを検知する検知センサ
を設け、その検知センサから出力される検知信号により
警報器を作動させるだけの構成でもよい。この場合に
は、警報器の警報によって作業者が、送液用配管又は脱
気用配管に設けられた開閉弁を手動で閉じるようにす
る。或いは、検知センサから出力される検知信号によ
り、送液用配管又は脱気用配管に設けられた緊急遮断弁
を自動的に閉じるようにする。In the embodiment described above, the degassing pipe 10 is used.
The trap tank 12 is provided in the above to prevent the processing liquid from flowing into the vacuum suction source side. However, the degassing pipe is not provided with a liquid reservoir such as a trap tank, but simply
The degassing pipe is provided with a detection sensor that detects that the processing liquid has flowed into the degassing module from the vacuum chamber of the degassing module, and only the alarm device is activated by the detection signal output from the detection sensor. But it's okay. In this case, the operator manually closes the on-off valve provided in the liquid sending pipe or the degassing pipe by the alarm of the alarm device. Alternatively, the emergency shutoff valve provided in the liquid sending pipe or the degassing pipe is automatically closed by the detection signal output from the detection sensor.
【0032】[0032]
【発明の効果】請求項1に係る発明の処理液供給装置を
使用すると、脱気モジュールの液流路の破損などが起こ
った場合に、その異常を確実に検知して、脱気モジュー
ルの脱気能力が低下して脱気されないままの処理液が基
板等の被処理物へ供給されることにより現像不良や塗布
むらなどを生じる、といった不都合を回避することがで
き、歩留まりの低下を防ぐことができる。When the treatment liquid supply apparatus according to the first aspect of the present invention is used, when the liquid flow path of the degassing module is damaged, the abnormality is surely detected and the degassing module is degassed. It is possible to avoid inconveniences such as poor development and uneven coating caused by the supply of processing liquid that has not been degassed due to a decrease in vapor capacity to the object to be processed, and to prevent a decrease in yield. You can
【0033】請求項2に係る発明の処理液供給装置で
は、脱気用配配管内へ流入した処理液が真空吸引源の方
へ流れ込むのを防止し、及び/又は、処理液供給源から
送液用配管を通って処理液が脱気モジュール内へ流れる
のを止めて、脱気モジュールから脱気用配管内への処理
液の流入を停止させることができるため、大量の処理液
が脱気モジュールから脱気用配管を通って真空吸引源で
ある真空設備側へ流れ込むのを自動的に止めて、設備に
ダメージが与えられるのを防止することができる。In the treatment liquid supply apparatus according to the second aspect of the present invention, the treatment liquid flowing into the degassing distribution pipe is prevented from flowing toward the vacuum suction source and / or sent from the treatment liquid supply source. A large amount of processing liquid is degassed because the processing liquid can be stopped from flowing through the liquid piping into the degassing module and the flow of processing liquid from the degassing module into the degassing piping can be stopped. It is possible to prevent the equipment from being damaged by automatically stopping the flow from the module to the vacuum equipment, which is the vacuum suction source, through the degassing pipe.
【0034】請求項3に係る発明の処理液供給装置を使
用すると、脱気モジュールの液流路の破損などが起こっ
た場合に、大量の処理液が脱気モジュールから脱気用配
管を通って真空吸引源である真空設備側へ流れ込むこと
が無くなるため、設備にダメージが与えられるのを防止
することができる。With the treatment liquid supply apparatus according to the third aspect of the present invention, when the liquid flow path of the degassing module is damaged, a large amount of treatment liquid flows from the degassing module through the degassing pipe. Since it does not flow into the vacuum equipment that is the vacuum suction source, it is possible to prevent the equipment from being damaged.
【0035】請求項4に係る発明の処理液供給装置で
は、脱気モジュールに異常が発生したことが作業者に知
らされるため、作業者が被処理物への処理液の供給を停
止させることにより、脱気されないままの処理液が被処
理物上へ供給されて現像不良や塗布むらなどを生じる、
といった不都合を回避することができる。In the treatment liquid supply apparatus according to the fourth aspect of the present invention, since the worker is informed that an abnormality has occurred in the degassing module, the worker must stop the supply of the treatment liquid to the object to be processed. As a result, the processing liquid that has not been degassed is supplied onto the object to be processed, resulting in poor development and uneven coating.
It is possible to avoid such inconvenience.
【0036】請求項5に係る発明の処理液供給装置で
は、液溜め部内に溜まった液をドレン排出用配管を通し
て排出することができる。また、液溜め部内に溜まった
液を定期的に排出するようにすることにより、定常時に
おける液溜め部内の液の貯留によって貯留量検知手段が
動作することが無くなるため、異常時における液溜め部
への処理液の流入だけを貯留量検知手段が確実に検知す
ることができる。In the treatment liquid supply apparatus according to the fifth aspect of the present invention, the liquid accumulated in the liquid reservoir can be discharged through the drain discharge pipe. Further, by periodically discharging the liquid accumulated in the liquid reservoir, the storage amount detecting means does not operate due to the storage of the liquid in the liquid reservoir during a steady state, so that the liquid reservoir at the time of abnormality Only the inflow of the treatment liquid to the storage amount detection means can be surely detected.
【図1】この発明の実施形態の1例を示す処理液供給装
置の概略構成図である。FIG. 1 is a schematic configuration diagram of a processing liquid supply apparatus showing an example of an embodiment of the present invention.
【図2】従来の処理液供給装置の1例を示す概略構成図
である。FIG. 2 is a schematic configuration diagram showing an example of a conventional processing liquid supply apparatus.
【符号の説明】 1 送液用配管 2 脱気モジュール 3 入口側継手部 4 出口側継手部 5 液流路 6 真空チャンバ 7、10 脱気用配管 12 トラップタンク 14、16 緊急遮断弁 18 ドレン排出用配管 20 開閉弁 22 大気連通配管 24 大気開放弁 30 縁切り弁 32 貯留量検知センサ 34 CPU 36 警報器[Explanation of reference signs] 1 pipe for liquid supply 2 degassing module 3 joint part on inlet side 4 joint part on outlet side 5 liquid channel 6 vacuum chamber 7, 10 pipe for degassing 12 trap tank 14, 16 emergency shutoff valve 18 drain discharge Pipe 20 Open / close valve 22 Atmosphere communication pipe 24 Atmosphere release valve 30 Edge cut valve 32 Storage amount detection sensor 34 CPU 36 Alarm device
Claims (5)
て形成され入口と出口とを連通させる液流路を有し、そ
の液流路の周囲を真空チャンバで気密に密閉してなる脱
気モジュールと、 この脱気モジュールの前記真空チャンバ内の密閉空間を
真空吸引源に接続する脱気用配管とを備えた処理液供給
装置において、 前記脱気用配管内に前記脱気モジュールの真空チャンバ
内から処理液が流入したことを検知する検知手段を設け
るとともに、 その検知手段から出力される検知信号に基づいて前記脱
気用配管内への処理液の流入を報知する報知手段を設け
たことを特徴とする処理液供給装置。1. A liquid-feeding pipe for feeding a processing liquid, and a liquid flow path which is inserted in the middle of the liquid-feeding pipe and which is formed of a gas-permeable membrane material and connects an inlet and an outlet, A treatment liquid including a degassing module that hermetically seals the periphery of the liquid flow path in a vacuum chamber, and a degassing pipe that connects a sealed space in the vacuum chamber of the degassing module to a vacuum suction source. In the supply device, the degassing pipe is provided with a detection means for detecting that the processing liquid has flowed from the vacuum chamber of the degassing module, and the degassing is performed based on the detection signal output from the detection means. A processing liquid supply device, characterized by comprising an informing means for informing of the inflow of the processing liquid into the pipe for use.
気モジュールより上流側に、常時は開かれ検知手段の検
知信号により閉じられる緊急遮断弁が介設された請求項
1記載の処理液供給装置。2. An emergency shutoff valve which is normally opened and closed by a detection signal of a detection means is provided upstream of the degassing module in the degassing pipe and / or the liquid sending pipe. Processing liquid supply device.
て形成され入口と出口とを連通させる液流路を有し、そ
の液流路の周囲を真空チャンバで気密に密閉してなる脱
気モジュールと、 この脱気モジュールの前記真空チャンバ内の密閉空間を
真空吸引源に接続する脱気用配管とを備えた処理液供給
装置において、 前記脱気用配管の途中に、前記脱気モジュールの真空チ
ャンバ内から脱気用配管内へ流入した処理液を気体から
分離し貯留して真空吸引源の方へ処理液が流れ込むのを
防止する液溜め部を介設したことを特徴とする処理液供
給装置。3. A liquid feed pipe for feeding a treatment liquid, and a liquid flow path which is inserted in the middle of the liquid feed pipe and which is formed of a gas permeable membrane material and connects an inlet and an outlet, A treatment liquid including a degassing module that hermetically seals the periphery of the liquid flow path in a vacuum chamber, and a degassing pipe that connects a sealed space in the vacuum chamber of the degassing module to a vacuum suction source. In the supply device, in the middle of the degassing pipe, the processing liquid flowing from the vacuum chamber of the degassing module into the degassing pipe is separated from the gas and stored, and the processing liquid flows toward the vacuum suction source. A treatment liquid supply device characterized in that a treatment liquid reservoir for preventing the above is provided.
液が所定量に達したことを検知する貯留量検知手段が設
けられるとともに、 その貯留量検知手段から出力される検知信号に基づいて
前記液溜め部に処理液が所定量貯留されたことを報知す
る貯留量報知手段が設けられた請求項3記載の処理液供
給装置。4. A liquid storage part is provided with a storage amount detection means for detecting that the processing liquid stored therein reaches a predetermined amount, and based on a detection signal output from the storage amount detection means. 4. The processing liquid supply apparatus according to claim 3, further comprising storage amount notifying means for notifying that a predetermined amount of the processing liquid has been stored in the liquid storage section.
液体を排出するためのドレン排出用配管が接続され、そ
のドレン排出用配管に開閉弁が介設された請求項3又は
請求項4記載の処理液供給装置。5. The drain discharge pipe for discharging the liquid accumulated in the liquid storage part is connected to the bottom of the liquid storage part, and an opening / closing valve is provided in the drain discharge pipe. Item 4. The processing liquid supply apparatus according to item 4.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33823595A JP3347929B2 (en) | 1995-11-30 | 1995-11-30 | Processing liquid supply device |
| US08/753,706 US5762684A (en) | 1995-11-30 | 1996-11-27 | Treating liquid supplying method and apparatus |
| KR1019960059120A KR100197198B1 (en) | 1995-11-30 | 1996-11-28 | Treating liquid supplying method and apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33823595A JP3347929B2 (en) | 1995-11-30 | 1995-11-30 | Processing liquid supply device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH09150008A true JPH09150008A (en) | 1997-06-10 |
| JP3347929B2 JP3347929B2 (en) | 2002-11-20 |
Family
ID=18316208
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP33823595A Expired - Fee Related JP3347929B2 (en) | 1995-11-30 | 1995-11-30 | Processing liquid supply device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3347929B2 (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11333206A (en) * | 1998-05-26 | 1999-12-07 | Nitto Denko Corp | Degassing device |
| CN104415579B (en) * | 2013-08-20 | 2016-03-16 | 沈阳芯源微电子设备有限公司 | Fluid defoaming apparatus and method in a kind of semiconductor processing system |
| CN109940515A (en) * | 2019-04-16 | 2019-06-28 | 广东天机工业智能系统有限公司 | Vacuum energy station |
| JP2021067686A (en) * | 2019-10-18 | 2021-04-30 | エフ.ホフマン−ラ ロシュ アーゲーF. Hoffmann−La Roche Aktiengesellschaft | Techniques for checking state of analyzer |
| WO2026000101A1 (en) * | 2024-06-24 | 2026-01-02 | 深圳华大智造科技股份有限公司 | Liquid treatment system, liquid treatment method, and biochemical analysis system |
-
1995
- 1995-11-30 JP JP33823595A patent/JP3347929B2/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH11333206A (en) * | 1998-05-26 | 1999-12-07 | Nitto Denko Corp | Degassing device |
| CN104415579B (en) * | 2013-08-20 | 2016-03-16 | 沈阳芯源微电子设备有限公司 | Fluid defoaming apparatus and method in a kind of semiconductor processing system |
| CN109940515A (en) * | 2019-04-16 | 2019-06-28 | 广东天机工业智能系统有限公司 | Vacuum energy station |
| JP2021067686A (en) * | 2019-10-18 | 2021-04-30 | エフ.ホフマン−ラ ロシュ アーゲーF. Hoffmann−La Roche Aktiengesellschaft | Techniques for checking state of analyzer |
| US11530943B2 (en) | 2019-10-18 | 2022-12-20 | Roche Diagnostics Operations, Inc. | Techniques for checking state of analyzers |
| WO2026000101A1 (en) * | 2024-06-24 | 2026-01-02 | 深圳华大智造科技股份有限公司 | Liquid treatment system, liquid treatment method, and biochemical analysis system |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3347929B2 (en) | 2002-11-20 |
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