JP2000296899A - Method and apparatus for storing gas-dissolved water - Google Patents

Method and apparatus for storing gas-dissolved water

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Publication number
JP2000296899A
JP2000296899A JP11103534A JP10353499A JP2000296899A JP 2000296899 A JP2000296899 A JP 2000296899A JP 11103534 A JP11103534 A JP 11103534A JP 10353499 A JP10353499 A JP 10353499A JP 2000296899 A JP2000296899 A JP 2000296899A
Authority
JP
Japan
Prior art keywords
gas
dissolved
water
storage tank
dissolved water
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.)
Pending
Application number
JP11103534A
Other languages
Japanese (ja)
Inventor
Kofuku Yamashita
幸福 山下
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.)
Organo Corp
Original Assignee
Organo Corp
Japan Organo Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Organo Corp, Japan Organo Co Ltd filed Critical Organo Corp
Priority to JP11103534A priority Critical patent/JP2000296899A/en
Publication of JP2000296899A publication Critical patent/JP2000296899A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】 【課題】 余分なガスを溶解させること無く、ガス溶解
水に必要な溶存ガス濃度を保持でき、気相部で大気に溶
解ガスを拡散させず、回収処理や爆発の危険性を排除す
ることができるガス溶解水の貯留方法及びその貯留装置
を提供する。 【解決手段】 純水にガスを溶解するガス溶解水製造装
置3と、ガス溶解水製造装置3で製造されたガス溶解水
を貯留する貯留タンク11と、貯留タンク11の上方部
とガス溶解水製造装置3のガス供給源とを接続する配管
12と、配管12を流れるガス流量を調節する調節弁1
3と、調節弁13を操作するための検知制御装置14
と、を具備してなるガス溶解水の貯留装置であって、ガ
ス溶解水を貯留タンク11にて貯留する際、貯留タンク
11内に生じる気相部11aを純水に溶解したガスと同
一ガスにてシールする方法。
[57] [Abstract] [Problem] To maintain the concentration of dissolved gas required for gas-dissolved water without dissolving excess gas, prevent the dissolved gas from diffusing into the atmosphere in the gas phase, and pose a danger of recovery and explosion. Provided are a method for storing gas-dissolved water and a storage device for the same, which can eliminate the property. SOLUTION: A gas-dissolved water producing apparatus 3 for dissolving a gas in pure water, a storage tank 11 for storing the gas-dissolved water produced by the gas-dissolved water producing apparatus 3, an upper part of the storage tank 11, and a gas dissolved water. A pipe 12 for connecting a gas supply source of the manufacturing apparatus 3 and a control valve 1 for adjusting a gas flow rate flowing through the pipe 12
3 and a detection control device 14 for operating the control valve 13
And a gas dissolving water storage device comprising: a gas dissolving unit that stores a gas dissolving water in a storage tank 11; How to seal with

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、主にシリコンウエ
ハ、液晶ガラス基板等の洗浄を行うために使用するガス
溶解水を一時的に貯留し、洗浄パターンに効率良く対応
させるためのガス溶解水の貯留方法及びその貯留装置に
関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention mainly relates to temporarily storing gas-dissolved water used for cleaning silicon wafers, liquid crystal glass substrates, etc., and for efficiently coping with a cleaning pattern. And a storage device for the storage device.

【0002】[0002]

【従来の技術】電子部品及びその製造装置部材等の洗浄
は、純水に各種ガスを溶解したガス溶解水で行うことが
多い。そして、このガス溶解水を使用した洗浄は、常時
一定量のガス溶解水を洗浄機に供給する定量給水パター
ン以外に、間欠的、且つ一度に多量のガス溶解水を供給
するバッチ給水パターンがある。このようなバッチ給水
パターンに対応した能力のガス溶解水製造装置を設置す
ることは装置が過大になり過ぎるため、ガス溶解水を使
用していない時もガス溶解水を製造し続け、貯留タンク
に貯めておき、洗浄時、1バッチ洗浄に使用するガス溶
解水量を供給する方法が採られている。
2. Description of the Related Art In many cases, electronic components and members for manufacturing the same are cleaned with gas-dissolved water in which various gases are dissolved in pure water. The cleaning using the gas-dissolved water has a batch water supply pattern for intermittently supplying a large amount of the gas-dissolved water at one time other than a fixed water supply pattern for constantly supplying a fixed amount of the gas-dissolved water to the cleaning machine. . Installing a gas-dissolved water production device with a capacity corresponding to such a batch water supply pattern would make the device too large, so it would continue to produce gas-dissolved water even when gas-dissolved water was not used, and to store it in the storage tank. A method is used in which the gas is stored, and the amount of gas-dissolved water used for one batch cleaning is supplied during cleaning.

【0003】このガス溶解水の貯留方法を図3を参照し
て説明する。純水製造装置50にて製造された純水は、
ガス溶解槽51にてガス供給源、例えば水素供給源52
から供給された水素が溶解され、水素溶解水となる。こ
の水素溶解水は配管53にて貯留タンク54に送られ、
一時的に貯留される。この貯留タンク54は、特にシー
ルされていないため、貯留タンク54内に水素溶解水が
貯留され始めると、水素溶解水による液相部55と大気
による気相部56とが生じる。このため、液相部55の
水素溶解水中の溶存水素が気相部56の大気側に拡散
し、水素溶解水中の溶存水素濃度の低下を招き、そのま
ま供給ポンプ57によりユースポイントBに送られ、電
子部品及びその製造装置部材の洗浄に使用されると、洗
浄不良を起こすという問題がある。これを解決するため
に、貯留タンク54に貯留している間に気相部56の大
気側に拡散する溶存水素量を見越して、純水に水素を余
分に溶解させることが行われている。
[0003] A method for storing the gas-dissolved water will be described with reference to FIG. Pure water produced by the pure water production device 50 is:
In the gas dissolving tank 51, a gas supply source, for example, a hydrogen supply source 52
Is dissolved and hydrogen-dissolved water is obtained. This hydrogen-dissolved water is sent to a storage tank 54 via a pipe 53,
Stored temporarily. Since the storage tank 54 is not particularly sealed, when the hydrogen-dissolved water starts to be stored in the storage tank 54, a liquid-phase part 55 of the hydrogen-dissolved water and a gas-phase part 56 of the atmosphere are generated. For this reason, the dissolved hydrogen in the hydrogen-dissolved water in the liquid-phase part 55 diffuses to the atmosphere side of the gas-phase part 56, causing a decrease in the dissolved hydrogen concentration in the hydrogen-dissolved water, and is directly sent to the use point B by the supply pump 57, When used for cleaning electronic components and members for manufacturing the same, there is a problem that cleaning failure occurs. In order to solve this, extra hydrogen is dissolved in pure water in anticipation of the amount of dissolved hydrogen that diffuses to the atmosphere side of the gas phase portion 56 while being stored in the storage tank 54.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、上記従
来例では、気相部56の大気側へ拡散する溶存水素量を
見越して、純水に水素を余分に溶解させるから、その分
水素が無駄になり、水素供給源52も大きなものとする
必要がある。加えて、ガスの種類によっては、大気側へ
拡散したガスを回収しなければない。また、ガスが水素
ガスの場合、気相部56へ拡散した水素ガス濃度が4%
以上、気相部56の酸素ガス濃度が5%以上になると、
爆発の危険性がある。
However, in the above conventional example, extra hydrogen is dissolved in pure water in anticipation of the amount of dissolved hydrogen diffusing to the atmosphere side of the gas phase portion 56, so that hydrogen is wasted correspondingly. Therefore, the hydrogen supply source 52 also needs to be large. In addition, depending on the type of gas, it is necessary to collect gas diffused to the atmosphere. When the gas is a hydrogen gas, the concentration of the hydrogen gas diffused into the gas phase portion 56 is 4%.
As described above, when the oxygen gas concentration of the gas phase portion 56 becomes 5% or more,
Risk of explosion.

【0005】従って、本発明の目的は、余分なガスを溶
解させることなく、ガス溶解水の使用時に必要な溶存ガ
ス濃度を保持でき、気相部で大気側に溶存ガスを拡散さ
せないようにして、回収操作や爆発の危険性を排除する
ことができるガス溶解水の貯留方法及びその貯留装置を
提供することにある。
Accordingly, an object of the present invention is to maintain a dissolved gas concentration required when using gas-dissolved water without dissolving excess gas, and to prevent the dissolved gas from diffusing to the atmosphere in the gas phase. Another object of the present invention is to provide a method for storing gas-dissolved water and an apparatus for storing the same, which can eliminate the danger of recovery operation and explosion.

【0006】[0006]

【課題を解決するための手段】かかる実情において、本
発明者等は鋭意検討を行った結果、純水にガス、例え
ば、水素を溶解して得られる水素溶解水を機能水として
貯留タンクに貯留する際、貯留タンク内に生じる気相部
を前記水素溶解水製造の際に使用する水素ガスにてシー
ルすれば、機能水製造時の溶存水素濃度を維持でき、水
素溶解水中の溶存水素が大気中に拡散することを防止で
きることなどを見い出し、本発明を完成するに至った。
Under such circumstances, the present inventors have made intensive studies and as a result, have stored a gas, for example, hydrogen-dissolved water obtained by dissolving hydrogen in pure water as functional water in a storage tank. When the gas phase generated in the storage tank is sealed with hydrogen gas used in the production of the hydrogen-dissolved water, the dissolved hydrogen concentration in the production of the functional water can be maintained, and the dissolved hydrogen in the hydrogen-dissolved water is removed from the atmosphere. The present inventors have found out that it can be prevented from being diffused in, and have completed the present invention.

【0007】すなわち、請求項1の発明は、純水にガス
を溶解し、得られたガス溶解水を貯留タンクに貯留する
際、前記貯留タンク内に生じる気相部を前記純水に溶解
したガスと同一のガスにてシールすることを特徴とする
ガス溶解水の貯留方法を提供するものである。これによ
り、貯留タンク内に生じる気相部は、ガス溶解水と同一
ガスにてシールされているから、溶存ガスが気相部の大
気側に拡散することがないし、溶存ガス濃度の低下もな
い。
That is, according to the first aspect of the present invention, when a gas is dissolved in pure water and the obtained gas-dissolved water is stored in a storage tank, a gas phase generated in the storage tank is dissolved in the pure water. A method for storing gas-dissolved water characterized by sealing with the same gas as the gas. Thereby, the gas phase generated in the storage tank is sealed with the same gas as the gas-dissolved water, so that the dissolved gas does not diffuse to the atmosphere side of the gas phase and the concentration of the dissolved gas does not decrease. .

【0008】請求項2の発明は、純水にガスを溶解し、
得られたガス溶解水を貯留タンクにて貯留していく際、
前記貯留タンク内に生じる気相部を前記純水に溶解した
ガスと同一のガスでシールし、前記貯留タンク内が前記
ガス溶解水で満杯になったとき、前記ガスによるシール
を止める一方、前記ガス溶解水の供給は継続して前記貯
留タンクから溢流させることを特徴とするガス溶解水の
貯留方法を提供するものである。これにより、貯留タン
ク内がガス溶解水により満杯になると、実質的に気相部
が無くなりガスによるシールを停止するため、シールに
必要とするガスだけを貯留タンク内に供給することにな
って、ガスが無駄にならない。一方、貯留タンクに供給
が継続されるガス溶解水は溢流させるため、ガス溶解水
を使用しない限り、大気が直接介在する気相部が生じな
い。
According to a second aspect of the present invention, a gas is dissolved in pure water,
When storing the obtained gas dissolved water in a storage tank,
The gas phase part generated in the storage tank is sealed with the same gas as the gas dissolved in the pure water, and when the storage tank is full with the gas-dissolved water, the sealing by the gas is stopped, It is an object of the present invention to provide a method for storing gas-dissolved water, characterized in that supply of gas-dissolved water is continuously caused to overflow from the storage tank. Thereby, when the storage tank is filled with the gas-dissolved water, the gas phase part is substantially eliminated and the sealing with the gas is stopped, so that only the gas necessary for the sealing is supplied to the storage tank. Gas is not wasted. On the other hand, since the gas-dissolved water continuously supplied to the storage tank overflows, a gas-phase portion directly interposed by the atmosphere does not occur unless the gas-dissolved water is used.

【0009】請求項3の発明は、前記ガス溶解水中の溶
存ガス濃度を測定し、この溶存ガス濃度からガス分圧を
算定し、該ガス分圧と同圧又はそれ以上の圧となるよう
に前記貯留タンク内に前記ガスを供給することを特徴と
するガス溶解水の貯留方法を提供するものである。これ
により、貯留タンク内のガスによるシールはガス溶解水
中の溶存ガス濃度に応じた最適のものから安全サイドの
ものまでが可能となる。ここで、溶存ガス濃度からガス
分圧を算定する方法は、公知の方法に従い、ガスの種類
に応じた算定式に基づいて行われる。また、貯留タンク
内に供給するガス量は、ガス溶解水中のガス分圧と同圧
になるように供給するのが理想であるが、ガス溶解水中
のガス分圧より5〜20%程度のやや高めになるように
供給することが、若干のガス分圧の変動を吸収でき、且
つ溶解ガスの大気中への拡散を確実に抑制できる点で好
ましい。
According to a third aspect of the present invention, the dissolved gas concentration in the gas-dissolved water is measured, and the gas partial pressure is calculated from the dissolved gas concentration so that the gas partial pressure is equal to or higher than the gas partial pressure. The present invention provides a method for storing gas-dissolved water, wherein the gas is supplied into the storage tank. As a result, it is possible to seal the gas in the storage tank from the optimal one according to the dissolved gas concentration in the gas dissolved water to the safe side. Here, the method of calculating the gas partial pressure from the dissolved gas concentration is performed according to a known method based on a calculation formula according to the type of gas. Ideally, the amount of gas supplied into the storage tank should be supplied so as to be the same as the gas partial pressure in the gas-dissolved water. Supplying at a higher pressure is preferable in that it can absorb a slight change in gas partial pressure and can reliably suppress the diffusion of dissolved gas into the atmosphere.

【0010】請求項4の発明は、前記貯留タンクがシリ
コンウエハ、液晶ガラス基板等の洗浄を行う洗浄装置に
設けたワンバス洗浄槽であることを特徴とするガス溶解
水の貯留方法を提供するものである。これにより、ワン
バス洗浄槽内のガス溶解水中の溶存ガス濃度は設定濃度
より低下しないから、シリコンウエハ、液晶ガラス基板
等の洗浄に際し、常時一定水準の洗浄水を供給でき、安
定した洗浄を確保できる。
According to a fourth aspect of the present invention, there is provided a method for storing gas-dissolved water, wherein the storage tank is a one-bath cleaning tank provided in a cleaning apparatus for cleaning silicon wafers, liquid crystal glass substrates, and the like. It is. As a result, the concentration of dissolved gas in the gas-dissolved water in the one-bath washing tank does not drop below the set concentration, so that a constant level of washing water can always be supplied when washing silicon wafers, liquid crystal glass substrates, etc., and stable washing can be ensured. .

【0011】請求項5の発明は、純水にガスを溶解する
ガス溶解水製造装置と、該ガス溶解水製造装置で製造さ
れたガス溶解水を貯留する貯留タンクと、該貯留タンク
の上方部と前記ガス溶解水製造装置のガス供給源とを接
続する配管と、該配管を流れるガス圧力を調節する調節
弁と、該調節弁を操作するための検知制御装置と、を具
備してなることを特徴とするガス溶解水の貯留装置を提
供するものである。これにより、間欠的又は一度に多量
のガス溶解水を使用するような洗浄パターンに効率良く
対応させるための上記ガス溶解水の貯留方法が確実に実
現される。
A fifth aspect of the present invention provides a gas-dissolved water producing apparatus for dissolving a gas in pure water, a storage tank for storing the gas-dissolved water produced by the gas-dissolved water producing apparatus, and an upper part of the storage tank. And a pipe connecting the gas supply source of the gas-dissolved water producing apparatus, a control valve for adjusting the pressure of gas flowing through the pipe, and a detection control device for operating the control valve. And a storage device for storing gas-dissolved water. This reliably realizes the method of storing gas-dissolved water for efficiently coping with a cleaning pattern in which a large amount of gas-dissolved water is used intermittently or at once.

【0012】[0012]

【発明の実施の形態】本発明において、ガスが溶解され
る純水としては、特に制限されないが、例えば、原水を
凝集沈殿装置、砂濾過装置、活性炭濾過装置を順次通し
処理した前処理装置段階での前処理水、該前処理水を逆
浸透膜装置、2床3塔イオン交換装置、混床式イオン交
換装置、精密フィルターを順次通し処理した一次純水製
造装置段階での一次純水又は更に、この一次純水に紫外
線照射、混床式ポリッシャー、限外濾過膜処理を施し、
一次純水中に残留する微粒子、コロイド物質、有機物、
金属イオン、陰イオン等を除去する二次純水製造装置段
階での二次純水、所謂超純水が挙げられる。
DETAILED DESCRIPTION OF THE INVENTION In the present invention, the pure water in which the gas is dissolved is not particularly limited. For example, a pretreatment device in which raw water is passed through a coagulating sedimentation device, a sand filtration device, and an activated carbon filtration device in order. Pretreatment water in the above, the purified water in the stage of the primary pure water production equipment stage which passed through the reverse osmosis membrane device, the two-bed three-column ion exchange device, the mixed bed type ion exchange device, the precision filter in order Furthermore, this primary pure water is subjected to ultraviolet irradiation, mixed bed polisher, ultrafiltration membrane treatment,
Fine particles, colloidal substances, organic matter,
Secondary pure water at the stage of the secondary pure water producing apparatus for removing metal ions, anions and the like, that is, so-called ultrapure water.

【0013】上記純水に溶解させるガスとしては、特に
制限されないが、例えばオゾン、酸素、水素、炭酸ガス
等が挙げられる。純水にガスを溶解させる方法として
は、特に制限されないが、純水にガス透過膜を通してガ
スを注入し溶解させる膜溶解法、純水にガスをばっ気し
て溶解させるばっ気溶解法、純水にエジェクターを通し
てガスを溶解させるエジェクター法及びガス溶解槽に純
水を送るポンプのサクション側にガスを供給しポンプ内
乱流によりガスを溶解させるポンプ内攪拌法等が挙げら
れる。
The gas dissolved in the pure water is not particularly restricted but includes, for example, ozone, oxygen, hydrogen, carbon dioxide and the like. The method for dissolving the gas in pure water is not particularly limited, but a film dissolving method in which the gas is injected into pure water through a gas permeable membrane to dissolve the gas, an aeration dissolving method in which the gas is dissolved in pure water by aeration, and a pure dissolving method. An ejector method in which gas is dissolved in water through an ejector, a pump stirring method in which gas is supplied to the suction side of a pump that sends pure water to a gas dissolving tank, and the gas is dissolved by turbulent flow in the pump, and the like.

【0014】次に、本発明の第1の実施の形態における
ガス溶解水の貯留方法について、図1のガス溶解水の貯
留装置のフロー図に基づいて説明する。図中、ガス溶解
水製造装置Aは、前処理水を純水にする純水製造装置1
と、オゾン、水素等のガス発生装置2と、純水製造装置
1で製造された純水にオゾン、水素等のガスを溶解する
ガス溶解槽3とから構成される。前処理水は、まず純水
製造装置1に送られ、これが一次純水製造装置であれば
一次純水にされ、更に、二次純水製造装置で処理されれ
ば、所謂超純水が得られる。この超純水は、配管4によ
りガス溶解槽3に送られ、ガス溶解槽3にてガス発生装
置2から配管5を通り供給された例えば、オゾン、水素
等のガスが溶解される。ガス溶解槽3では膜溶解法が採
用されているから、ガス溶解槽3内のガス透過膜6によ
り、気相室3aと液相室3bとに分割されている。この
ガス溶解槽3の気相室3aからガスが注入され、ガス透
過膜6を通って液相室3bの超純水にガスが溶解され
る。
Next, a method for storing gas-dissolved water according to the first embodiment of the present invention will be described with reference to the flowchart of the apparatus for storing gas-dissolved water shown in FIG. In the figure, a gas-dissolved water producing apparatus A is a pure water producing apparatus 1 for converting pre-treated water into pure water.
And a gas generator 2 for generating ozone, hydrogen and the like, and a gas dissolving tank 3 for dissolving a gas such as ozone and hydrogen in the pure water produced by the pure water producing apparatus 1. The pre-treated water is first sent to the pure water producing apparatus 1, and if it is a primary pure water producing apparatus, it is converted into primary pure water. Further, if it is treated by a secondary pure water producing apparatus, so-called ultra pure water is obtained. Can be The ultrapure water is sent to the gas dissolving tank 3 by the pipe 4, and the gas such as ozone and hydrogen supplied from the gas generator 2 through the pipe 5 is dissolved in the gas dissolving tank 3. Since the gas dissolving tank 3 employs the membrane dissolving method, the gas dissolving tank 3 is divided into a gas phase chamber 3a and a liquid phase chamber 3b by the gas permeable membrane 6 in the gas dissolving tank 3. Gas is injected from the gas phase chamber 3a of the gas dissolving tank 3, and passes through the gas permeable membrane 6 to be dissolved in the ultrapure water of the liquid phase chamber 3b.

【0015】液相室3bでガスが溶解されたガス溶解水
は、ガス溶解水の貯留装置10に送られ、そのユースポ
イントBでの使用条件に合わせて貯留される。ガス溶解
水の貯留装置10は、ガス溶解水製造装置Aで製造され
たガス溶解水を貯留する貯留タンク11と、ガス発生装
置2とガス溶解槽3を接続する配管5から分岐して貯留
タンク11の上方部に接続する配管12と、配管12を
流れるガス圧力を調節する調節弁13と、調節弁13を
操作するための検知制御装置14と、を具備してなるも
のである。
The gas-dissolved water in which the gas is dissolved in the liquid phase chamber 3b is sent to the gas-dissolved water storage device 10 and stored according to the use conditions at the use point B. The gas-dissolved water storage device 10 includes a storage tank 11 for storing the gas-dissolved water produced by the gas-dissolved water production device A, and a storage tank branched from the pipe 5 connecting the gas generator 2 and the gas dissolution tank 3. The apparatus comprises a pipe 12 connected to an upper part of the pipe 11, a control valve 13 for adjusting a gas pressure flowing through the pipe 12, and a detection control device 14 for operating the control valve 13.

【0016】貯留タンク11にガス溶解水を貯留する場
合、先ず、貯留タンク11内はその全てが気相部11a
となり、大気が充満しているから、オーバーフローライ
ン15に設置した溢流弁16を閉じ、調節弁13を開い
て、ガス発生装置2からガスを配管5及び配管5から分
岐する配管12を通り貯留タンク11内に供給し、貯留
タンク11内の大気をガスにて置換しつつ、条件を解除
し「開」にした圧力制御弁17から大気を排出し、貯留
タンク11内の気相部11aをガスにてシールする。気
相部11aをガスにてシールし始めると同時に、あるい
はシールしつつ又はシール終了後に、ガス溶解槽3の液
相室3bからガス溶解水を配管18を通して貯留タンク
11内に投入し始め、液相部11bを形成させる。貯留
タンク11内の大気をガスにて置換し終わったら、圧力
制御弁17の条件を設定して「閉」にし、貯留タンク1
1内にガス溶解水を満杯になるまで投入する。貯留タン
ク11内に設置した液面センサ19にてガス溶解水が満
杯になったことを検知し、液面センサ19から調節弁1
3に対して閉信号を出し、調節弁13を閉じる。同時に
溢流弁16に対して開信号を出し溢流弁16を開いて、
ガス溶解水をオーバーフローライン15を通して元のガ
ス溶解槽3の液相室3bに戻す。この貯留タンク11内
に貯留されたガス溶解水は、ユースポイントBからの使
用指令に基づいて供給ポンプ20が稼働され、配管21
を通りユースポイントBに送られ、ユースポイントBに
おける使用目的に沿いガス溶解水が使用される。
When storing gas-dissolved water in the storage tank 11, first, all of the gas in the storage tank 11 is in the gas phase portion 11a.
Since the atmosphere is full, the overflow valve 16 installed in the overflow line 15 is closed, the control valve 13 is opened, and gas is stored from the gas generator 2 through the pipe 5 and the pipe 12 branched from the pipe 5. While supplying the gas into the tank 11 and replacing the atmosphere in the storage tank 11 with a gas, the atmosphere is discharged from the pressure control valve 17 which has been released from the condition and opened, and the gas phase portion 11a in the storage tank 11 is discharged. Seal with gas. At the same time as starting to seal the gas phase portion 11a with gas, or while or after sealing, gas-dissolved water from the liquid-phase chamber 3b of the gas dissolving tank 3 is started to be injected into the storage tank 11 through the pipe 18, The phase part 11b is formed. After replacing the atmosphere in the storage tank 11 with the gas, the condition of the pressure control valve 17 is set to “close”, and the storage tank 1 is closed.
Charge the gas-dissolved water in 1 until it is full. When the liquid level sensor 19 installed in the storage tank 11 detects that the gas dissolved water is full, the liquid level sensor 19 sends the control valve 1
3 and a control signal 13 is closed. At the same time, an open signal is issued to the overflow valve 16 and the overflow valve 16 is opened,
The gas dissolved water is returned to the original liquid phase chamber 3b of the gas dissolving tank 3 through the overflow line 15. The supply pump 20 is operated based on the use command from the use point B, and the gas dissolved water stored in the storage tank 11 is operated.
, And is sent to use point B, and the gas-dissolved water is used according to the purpose of use at use point B.

【0017】ユースポイントBにガス溶解水が供給ポン
プ20により送られると、貯留タンク11内のガス溶解
水が減るから、それを液面センサ19により検知して、
調節弁13に対して開信号を出し調節弁13を開きガス
を送り、同時に液面センサ19により溢流弁16に対し
ても閉信号を出し溢流弁16を閉じて、貯留タンク11
内に生じる気相部11aをガスにてシールする。ユース
ポイントBにおけるガス溶解水の使用が終われば、再び
貯留タンク11内がガス溶解水で満杯になるため、液面
センサ19にて検知し、液面センサ19から調節弁13
に対して閉信号を出し、調節弁13を閉じ、同時に溢流
弁16に対して開信号を出し溢流弁16を開いて、ガス
溶解水をオーバーフローライン15を通して元のガス溶
解槽3の液相室3bに戻す。以後は上記の繰り返しとな
る。なお、前記検知制御装置14は、図1のガス溶解水
の貯留装置のフローでは、具体的には液面センサ19を
示し、貯留タンク11内でのガス溶解水量を検知して、
その情報により調節弁13及び溢流弁16に対して開信
号及び閉信号を出力し、弁13及び16を制御するもの
である。
When the gas-dissolved water is sent to the use point B by the supply pump 20, the gas-dissolved water in the storage tank 11 decreases.
An open signal is sent to the control valve 13 to open the control valve 13 and gas is sent. At the same time, a close signal is also sent to the overflow valve 16 by the liquid level sensor 19 to close the overflow valve 16 and the storage tank 11
The gas phase 11a generated therein is sealed with gas. When the use of the gas-dissolved water at the use point B is finished, the inside of the storage tank 11 is again filled with the gas-dissolved water.
, The control valve 13 is closed, and at the same time, an open signal is sent to the overflow valve 16 to open the overflow valve 16, and the gas-dissolved water flows through the overflow line 15 into the original gas-dissolved tank 3. Return to shared room 3b. Thereafter, the above is repeated. The detection control device 14 specifically shows the liquid level sensor 19 in the flow of the gas-dissolved water storage device in FIG. 1 and detects the amount of gas-dissolved water in the storage tank 11,
Based on the information, an open signal and a close signal are output to the control valve 13 and the overflow valve 16 to control the valves 13 and 16.

【0018】図2は本発明の第2の実施の形態における
ガス溶解水の貯留装置のフロー図を示す。図中、第1の
実施の形態例と同一構成要素には同一符号を付して、そ
の説明を省略し、異なる点について説明する。すなわ
ち、ガス溶解水の貯留装置10aと図1の実施の形態例
に示すガス溶解水の貯留装置10との相違点は、配管1
8を分岐して溶存ガス濃度計30を取り付け、貯留タン
ク11に隣接した配管12に圧力計31を取り付け、更
に溶存ガス濃度計30及び圧力計31により検知した出
力(情報)を受け、それらに基づいて演算し調節弁13
の開度を調節する供給量指令を出す演算制御器32を備
える、検知制御装置14aを有している点にある。すな
わち、配管18を流れるガス溶解水のガス濃度を溶存ガ
ス濃度計30により検知し、このガス濃度信号を演算制
御器32に送り、ここでガス溶解水のガス分圧に換算
し、このガス分圧に基づいて調節弁13の開度を演算し
供給量指令として調節弁13に出し、調節弁13の開度
を調節する。一方、圧力計31により貯留タンク11内
のオゾン等のガス圧力を検知し、このガス圧力信号を演
算制御器32に送り、ここでガス溶解水の上記のように
演算したガス分圧と対比し、異なればガス分圧になるよ
うな調節弁13の開度を演算し精密な供給量指令として
調節弁13に出し、調節弁13の開度を調節して、貯留
タンク11内のガス圧力を調節し、ガス溶解水のガス分
圧に合わる。
FIG. 2 is a flow chart of a gas dissolved water storage device according to a second embodiment of the present invention. In the figure, the same components as those of the first embodiment are denoted by the same reference numerals, the description thereof will be omitted, and different points will be described. That is, the difference between the gas dissolved water storage device 10a and the gas dissolved water storage device 10 shown in the embodiment of FIG.
8, the dissolved gas concentration meter 30 is attached, the pressure gauge 31 is attached to the pipe 12 adjacent to the storage tank 11, and the output (information) detected by the dissolved gas concentration meter 30 and the pressure gauge 31 is received. Control valve 13
In that it has a detection control device 14a including an operation controller 32 for issuing a supply amount command for adjusting the opening degree of the sensor. That is, the gas concentration of the gas-dissolved water flowing through the pipe 18 is detected by the dissolved gas concentration meter 30, and this gas concentration signal is sent to the arithmetic and control unit 32, where it is converted into the gas partial pressure of the gas-dissolved water. The opening degree of the control valve 13 is calculated based on the pressure and output to the control valve 13 as a supply amount command to adjust the opening degree of the control valve 13. On the other hand, the gas pressure of ozone or the like in the storage tank 11 is detected by the pressure gauge 31, and this gas pressure signal is sent to the arithmetic and control unit 32, where it is compared with the gas partial pressure calculated as described above. Calculate the opening of the control valve 13 to obtain a gas partial pressure if different, issue it to the control valve 13 as a precise supply amount command, and adjust the opening of the control valve 13 to reduce the gas pressure in the storage tank 11. Adjust to match the gas partial pressure of the gas dissolved water.

【0019】[0019]

【発明の効果】請求項1の発明によれば、貯留タンク内
に生じる気相部は、ガス溶解水と同一ガスにてシールさ
れているから、溶存ガスが気相部の大気に拡散すること
がなく、溶存ガス濃度の低下もない。従って、余分なガ
スを溶解させることなく、ガス溶解水の使用時に必要な
溶存ガス濃度を保持でき、気相部で大気側に溶存ガスを
拡散させないようにして、回収操作や爆発の危険性を排
除することができる。
According to the first aspect of the present invention, since the gas phase generated in the storage tank is sealed with the same gas as the gas-dissolved water, the dissolved gas diffuses into the atmosphere of the gas phase. And no decrease in dissolved gas concentration. Therefore, it is possible to maintain the required dissolved gas concentration when using gas-dissolved water without dissolving the excess gas, and to prevent the dissolved gas from diffusing to the atmosphere side in the gas phase to reduce the danger of recovery operation and explosion. Can be eliminated.

【0020】請求項2の発明によれば、貯留タンク内が
ガス溶解水により満杯になると、実質的に気相部がなく
なりガスによるシールを止めるため、シールに必要とす
るガスだけを貯留タンク内に供給することになって、ガ
スが無駄にならない。一方、貯留タンクに供給が継続さ
れるガス溶解水は溢流させるから、ガス溶解水を使用し
ない限り、大気が直接介在する気相部が生じない。従っ
て、上記効果に加えて、ガスを無駄に使用することがな
く、無駄となったガスの回収や無害化処理もなくなる。
According to the second aspect of the present invention, when the inside of the storage tank is filled with the gas-dissolved water, the gas phase is substantially eliminated and the sealing by the gas is stopped, so that only the gas necessary for the sealing is stored in the storage tank. Gas will not be wasted. On the other hand, since the gas-dissolved water continuously supplied to the storage tank overflows, a gas-phase portion directly interposed by the atmosphere does not occur unless the gas-dissolved water is used. Therefore, in addition to the above effects, there is no wasteful use of gas, and there is no need to recover waste gas or perform detoxification processing.

【0021】請求項3の発明によれば、貯留タンク内の
ガスによるシールがガス溶解水中の溶存ガス濃度に応じ
た適切なものとすることが可能になる。従って、上記効
果に加えて、なお一層ガスを無駄に使用することがなく
なり、ガス溶解水中の溶存ガス濃度も安定し、ガス溶解
水の使用目的を達成できる。
According to the third aspect of the present invention, it is possible to properly seal the gas in the storage tank according to the concentration of the dissolved gas in the gas-dissolved water. Therefore, in addition to the above effects, the gas is not wasted more and more, the concentration of the dissolved gas in the gas-dissolved water is stabilized, and the purpose of use of the gas-dissolved water can be achieved.

【0022】請求項4の発明によれば、ワンバス洗浄槽
内のガス溶解水中の溶存ガス濃度が設定濃度より低下し
ないから、シリコンウエハ、液晶ガラス基板等の洗浄効
果が常時一定水準を確保したものになる。従って、上記
のような厳しい洗浄条件を容易にクリアーできる。
According to the fourth aspect of the present invention, since the concentration of the dissolved gas in the gas-dissolved water in the one-bath cleaning tank does not drop below the set concentration, the cleaning effect of the silicon wafer, the liquid crystal glass substrate, etc. is always maintained at a constant level. become. Therefore, the strict cleaning conditions as described above can be easily cleared.

【0023】請求項5の発明によれば、バッチ洗浄パタ
ーンのような貯留したガス溶解水の性能保持が難しい状
態のものであっても、効率良く対応させるための上記ガ
ス溶解水の貯留方法を確実に実現することができ、しか
も貯留したガス溶解水の性能を安定したものとすること
ができる。
According to the fifth aspect of the present invention, there is provided a method for storing gas-dissolved water for efficiently handling stored gas-dissolved water even in a state where the performance of stored gas-dissolved water is difficult to maintain, such as a batch cleaning pattern. As a result, the performance of the stored gas-dissolved water can be stabilized.

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

【図1】本発明の第1の実施の形態例を示すガス溶解水
の貯留装置のフロー図である。
FIG. 1 is a flow chart of a storage device for gas-dissolved water showing a first embodiment of the present invention.

【図2】本発明の第2の実施の形態例を示すガス溶解水
の貯留装置のフロー図である。
FIG. 2 is a flow chart of a gas dissolved water storage device according to a second embodiment of the present invention.

【図3】従来例を示すガス溶解水の貯留装置のフロー図
である。
FIG. 3 is a flow chart of a gas dissolved water storage device showing a conventional example.

【符号の説明】[Explanation of symbols]

1、50 純水製造装置 2 ガス発生装置 3、51 ガス溶解槽 3a 気相室 3b 液相室 4、5、12、15、18、21、53 配管 6 ガス透過膜 10、10a ガス溶解水の貯留装置 11、54 貯留タンク 11a、55 気相部 11b、56 液相部 13 調節弁 14、14a 検知制御装置 15 オーバーフローライン 16 溢流弁 17 圧力制御弁 19 液面センサ 20、57 供給ポンプ 30 溶存ガス濃度計 31 圧力計 32 演算制御器 52 水素供給源 A ガス溶解水製造装置 B ユースポイント 1,50 Pure water production apparatus 2 Gas generator 3,51 Gas dissolution tank 3a Gas phase chamber 3b Liquid phase chamber 4,5,12,15,18,21,53 Piping 6 Gas permeable membrane 10,10a Gas dissolved water Storage device 11, 54 Storage tank 11a, 55 Gas phase portion 11b, 56 Liquid phase portion 13 Control valve 14, 14a Detection control device 15 Overflow line 16 Overflow valve 17 Pressure control valve 19 Liquid level sensor 20, 57 Supply pump 30 Dissolution Gas concentration meter 31 Pressure gauge 32 Arithmetic controller 52 Hydrogen source A Gas dissolved water production equipment B Use point

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 純水にガスを溶解し、得られたガス溶解
水を貯留タンクに貯留する際、前記貯留タンク内に生じ
る気相部を前記純水に溶解したガスと同一のガスにてシ
ールすることを特徴とするガス溶解水の貯留方法。
When a gas is dissolved in pure water and the obtained gas-dissolved water is stored in a storage tank, a gas phase generated in the storage tank is filled with the same gas as the gas dissolved in the pure water. A method for storing gas-dissolved water, characterized by sealing.
【請求項2】 純水にガスを溶解し、得られたガス溶解
水を貯留タンクにて貯留していく際、前記貯留タンク内
に生じる気相部を前記純水に溶解したガスと同一のガス
でシールしつつ、前記貯留タンク内が前記ガス溶解水で
満杯になったときは、前記ガスによるシールを止める一
方、前記ガス溶解水の供給は継続して前記貯留タンクか
ら溢流させることを特徴とするガス溶解水の貯留方法。
2. When dissolving a gas in pure water and storing the obtained gas-dissolved water in a storage tank, a gas phase generated in the storage tank is the same as the gas dissolved in the pure water. When the storage tank is filled with the gas-dissolved water while sealing with gas, while stopping the sealing by the gas, the supply of the gas-dissolved water is allowed to continuously overflow from the storage tank. Characteristic method of storing gas-dissolved water.
【請求項3】 前記ガス溶解水中の溶存ガス濃度を測定
し、この溶存ガス濃度からガス分圧を算定し、該ガス分
圧と同圧又はそれ以上の圧となるように前記貯留タンク
内に前記ガスを供給することを特徴とする請求項1記載
のガス溶解水の貯留方法。
3. A method for measuring the concentration of a dissolved gas in the gas-dissolved water, calculating a gas partial pressure from the dissolved gas concentration, and storing the gas partial pressure in the storage tank so as to be equal to or higher than the gas partial pressure. 2. The method according to claim 1, wherein the gas is supplied.
【請求項4】 前記貯留タンクはシリコンウエハ、液晶
ガラス基板等の洗浄を行う洗浄装置に設けたワンバス洗
浄槽であることを特徴とする請求項1〜3のいずれか1
項に記載のガス溶解水の貯留方法。
4. The storage tank according to claim 1, wherein the storage tank is a one-bath cleaning tank provided in a cleaning apparatus for cleaning a silicon wafer, a liquid crystal glass substrate, or the like.
The method for storing gas-dissolved water according to item 6.
【請求項5】 純水にガスを溶解するガス溶解水製造装
置と、該ガス溶解水製造装置で製造されたガス溶解水を
貯留する貯留タンクと、該貯留タンクの上方部と前記ガ
ス溶解水製造装置のガス供給源とを接続する配管と、該
配管を流れるガス圧力を調節する調節弁と、該調節弁を
操作するための検知制御装置と、を具備してなることを
特徴とするガス溶解水の貯留装置。
5. A gas-dissolved water producing apparatus for dissolving a gas in pure water, a storage tank for storing the gas-dissolved water produced by the gas-dissolved water producing apparatus, an upper part of the storage tank and the gas-dissolved water. A gas comprising: a pipe for connecting a gas supply source of a manufacturing apparatus; a control valve for adjusting a gas pressure flowing through the pipe; and a detection control device for operating the control valve. Device for storing dissolved water.
JP11103534A 1999-04-12 1999-04-12 Method and apparatus for storing gas-dissolved water Pending JP2000296899A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11103534A JP2000296899A (en) 1999-04-12 1999-04-12 Method and apparatus for storing gas-dissolved water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11103534A JP2000296899A (en) 1999-04-12 1999-04-12 Method and apparatus for storing gas-dissolved water

Publications (1)

Publication Number Publication Date
JP2000296899A true JP2000296899A (en) 2000-10-24

Family

ID=14356542

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11103534A Pending JP2000296899A (en) 1999-04-12 1999-04-12 Method and apparatus for storing gas-dissolved water

Country Status (1)

Country Link
JP (1) JP2000296899A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005087396A1 (en) * 2004-03-17 2005-09-22 Kurita Water Industries Ltd. Circulation type gas-dissolved water supply device and method of operating such device
WO2018221069A1 (en) * 2017-05-31 2018-12-06 カーリットホールディングス株式会社 Hydrogen water production device and production method
JP2020179372A (en) * 2019-04-26 2020-11-05 オルガノ株式会社 Gas dissolution water manufacturing apparatus and method

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005087396A1 (en) * 2004-03-17 2005-09-22 Kurita Water Industries Ltd. Circulation type gas-dissolved water supply device and method of operating such device
JP2005262031A (en) * 2004-03-17 2005-09-29 Kurita Water Ind Ltd Circulating gas-dissolved water supply device and method for operating the device
WO2018221069A1 (en) * 2017-05-31 2018-12-06 カーリットホールディングス株式会社 Hydrogen water production device and production method
JP2018202289A (en) * 2017-05-31 2018-12-27 カーリットホールディングス株式会社 Production apparatus and production method of hydrogen water
TWI736770B (en) * 2017-05-31 2021-08-21 日商佳里多控股公司 Apparatus and method of producing hydrogen water
JP2020179372A (en) * 2019-04-26 2020-11-05 オルガノ株式会社 Gas dissolution water manufacturing apparatus and method
JP7292957B2 (en) 2019-04-26 2023-06-19 オルガノ株式会社 Dissolved gas water production device and method

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