Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP3777451B2 - Ozone water generation method and ozone water production apparatus - Google Patents
[go: Go Back, main page]

JP3777451B2 - Ozone water generation method and ozone water production apparatus - Google Patents

Ozone water generation method and ozone water production apparatus Download PDF

Info

Publication number
JP3777451B2
JP3777451B2 JP2004238692A JP2004238692A JP3777451B2 JP 3777451 B2 JP3777451 B2 JP 3777451B2 JP 2004238692 A JP2004238692 A JP 2004238692A JP 2004238692 A JP2004238692 A JP 2004238692A JP 3777451 B2 JP3777451 B2 JP 3777451B2
Authority
JP
Japan
Prior art keywords
ozone water
concentration
ozone
water
low
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP2004238692A
Other languages
Japanese (ja)
Other versions
JP2006055719A (en
Inventor
正行 加藤
久明 曽根
哲男 木下
勲 澤本
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.)
Pre Tech Co Ltd
Original Assignee
Pre Tech 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 Pre Tech Co Ltd filed Critical Pre Tech Co Ltd
Priority to JP2004238692A priority Critical patent/JP3777451B2/en
Publication of JP2006055719A publication Critical patent/JP2006055719A/en
Application granted granted Critical
Publication of JP3777451B2 publication Critical patent/JP3777451B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Oxygen, Ozone, And Oxides In General (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Description

この発明は、純水または炭酸水の少なくとも一方にオゾンガスを添加してオゾン水を生成するオゾン水生成方法、及びオゾン水製造装置に関し、また、純水に炭酸ガスが添加されたオゾンガスを添加してオゾン水を生成するオゾン水生成方法、及びオゾン水製造装置に関し、より詳細には、生成するオゾン水を容易に、また、安価に得るためのオゾン水生成方法及びオゾン水製造装置に関する。   The present invention relates to an ozone water generating method for generating ozone water by adding ozone gas to at least one of pure water or carbonated water, and an ozone water production apparatus. Further, ozone gas in which carbon dioxide gas is added to pure water is added. More particularly, the present invention relates to an ozone water generation method and an ozone water production apparatus for obtaining ozone water to be produced easily and inexpensively.

オゾンガスを溶液と接触させ、溶液を処理するオゾン処理は、古くは下水道の水処理をはじめ、いろいろな溶液の処理に使用されていた。また、近年では、中水道、上水道にいたるまで幅広く用いられるようになって来た。また、最近では、オゾンを純水に溶解したオゾン水が半導体や液晶の湿式洗浄にも広く利用されるようになってきている。   Ozone treatment in which ozone gas is brought into contact with a solution to treat the solution has long been used for treating various solutions including water treatment of sewers. Moreover, in recent years, it has come to be widely used from the middle water supply to the water supply. Recently, ozone water obtained by dissolving ozone in pure water has been widely used for wet cleaning of semiconductors and liquid crystals.

しかしながら、半導体や液晶では、オゾン水濃度を常に安定にし、また高濃度や低濃度の2つ以上の異なる濃度での同時使用がしばしば要求されることがあり、それにはまだまだ不十分で、2台以上のオゾン水装置を使用しないと安定したオゾン水濃度が得られず、コストも非常に高いものになっていた。   However, in semiconductors and liquid crystals, the ozone water concentration is always stable, and simultaneous use at two or more different concentrations of high and low concentrations is often required. If the above ozone water apparatus is not used, a stable ozone water concentration cannot be obtained, and the cost is very high.

また、オゾン水の作り方等によっては、その後のオゾン水濃度の減衰が大きく変わり、実際の洗浄槽でのオゾン水濃度の変動は大変大きかった。そのため、装置より供給されるオゾン水濃度は、実際に必要な濃度よりはるかに高い濃度で供給することにより余裕を見て半導体等の洗浄に使用しているのが現状である。   In addition, depending on how the ozone water was made, the subsequent attenuation of the ozone water concentration changed greatly, and the fluctuation of the ozone water concentration in the actual cleaning tank was very large. For this reason, the ozone water concentration supplied from the apparatus is used for cleaning semiconductors and the like with a margin by supplying it at a concentration much higher than the actually required concentration.

また、実際に使用されている現場からも、オゾン水濃度は余裕を見るのが当然であると思われており、オゾン水濃度が高くても現状での半導体等の洗浄では問題が無いと思われてきた。   In addition, it is natural that the ozone water concentration has a margin from the site where it is actually used, and even if the ozone water concentration is high, there is no problem in the current cleaning of semiconductors. I have been.

しかしながら、これでは被洗浄品の表面の洗浄程度が一定になるわけはなく、また、保護酸化膜の形成に使用されるときなどでは、オゾン水濃度の違いによる酸化膜の厚みの違いが生じてしまうこともあった。   However, this does not mean that the degree of cleaning of the surface of the article to be cleaned is constant, and when used for forming a protective oxide film, there is a difference in the thickness of the oxide film due to the difference in ozone water concentration. It sometimes happened.

さらに、オゾン水の利用が進んだ今日では、有機物を分解するだけではなく、基板上の金属を除去する工程、保護酸化膜を生成する工程、更にはパターンを組んだ後の洗浄にも使用されるようになってくるに従い、異なるオゾン水濃度で同時に使用することが多くなり、また、オゾン水濃度の範囲の限定も厳しくなってきている。   Furthermore, in today's use of ozone water, it is used not only for decomposing organic substances, but also for removing metal on the substrate, generating a protective oxide film, and cleaning after patterning. As it comes to be used, it is often used at different ozone water concentrations at the same time, and the limitation of the ozone water concentration range is becoming stricter.

最近では半導体の配線ピッチが狭くなるに従い、そこに使用される純水の水質が問題となり、非常に綺麗な純水が要求されるようになってきた。このような純水の水質は、比抵抗は18.24MΩcmの極限に近づき、TOCや一般の金属コンタミネーションは検出下限までの純度が要求されるようになってきた。   Recently, as the wiring pitch of semiconductors has become narrower, the quality of pure water used therein has become a problem, and very clean pure water has been required. The water quality of such pure water has approached the limit of 18.24 MΩcm, and TOC and general metal contamination have been required to have a purity up to the detection limit.

上記のように純水の純度が高くなるにつれ、その純水を用いたオゾン水生成は、純水の水質に依存すると思われるオゾン水濃度の変動が顕著になってきた。一般的には純水の純度が高くなるにつれ、オゾン水濃度が減少する傾向があった。 其の為、最近ではオゾン水を生成するときに、純水に炭酸ガスを添加して炭酸添加純水にした上でオゾンガスを添加して炭酸添加オゾン水を生成したり、純水に炭酸ガス添加オゾンガスを注入して炭酸添加オゾン水を生成する方法が取られるようになって来た。   As described above, as the purity of pure water becomes higher, ozone water generation using the pure water has noticeably fluctuated fluctuations in the concentration of ozone water that seems to depend on the quality of the pure water. In general, as the purity of pure water increases, the ozone water concentration tends to decrease. Therefore, recently, when generating ozone water, carbon dioxide gas is added to pure water to make carbonated pure water and then ozone gas is added to generate carbonated ozone water, or carbon dioxide gas is added to pure water. A method of injecting added ozone gas to generate carbonized ozone water has come to be used.

炭酸が添加されているオゾン水は、純水中のTOCに影響を受けないで、非常に高い濃度のオゾン水を容易に得ることが出来、また、生成されたオゾン水の濃度も減衰が非常に少なく、洗浄槽までの距離による減衰が少ないので、洗浄槽において高濃度のオゾン水を容易に得ることが出来るようになってきた(例えば、特許文献1)。
特開2003−145181号公報(第1頁〜第6頁、図1〜図4)
The ozone water to which carbonic acid is added is not affected by the TOC in pure water, so it is possible to easily obtain a very high concentration of ozone water, and the concentration of the generated ozone water is very attenuated. Since there is little attenuation due to the distance to the cleaning tank, high-concentration ozone water can be easily obtained in the cleaning tank (for example, Patent Document 1).
JP 2003-145181 A (page 1 to page 6, FIGS. 1 to 4)

しかしながら、安定した2つ以上の濃度のオゾン水を安価に提供することは非常に難しく、また、オゾン水装置の経時劣化によるオゾン水濃度の変動を検出することは全く出来なかった。   However, it has been very difficult to provide two or more stable concentrations of ozone water at low cost, and it has not been possible to detect any variation in the concentration of ozone water due to aging of the ozone water device.

この発明は、前述の従来技術の問題点を解消し、長期間にわたり連続的で、また、常に安定した2つ以上の濃度のオゾン水を得るためのオゾン水生成方法及びオゾン水製造装置を提供することを目的とする。   The present invention provides an ozone water generation method and an ozone water production apparatus for solving the above-mentioned problems of the prior art and obtaining ozone water having two or more concentrations that are continuous over a long period of time and always stable. The purpose is to do.

前記課題を解決し、かつ目的を達成するために、この発明は、以下のように構成した。   In order to solve the above problems and achieve the object, the present invention is configured as follows.

請求項1に記載の発明は、純水、または純水に炭酸ガスを溶解して得られた炭酸含有純水の少なくとも一方にオゾンガスを添加し、
また、純水に炭酸ガスが添加されたオゾンガスを添加し、
オゾン水を生成する方法において、
前記オゾンガスを溶解させ、オゾン水を生成している途中でその一部を低濃度オゾン水として取り出す低濃度オゾン水生成部と、
最後まで溶解させた高濃度オゾン水を生成して取り出すオゾン水生成部とを備え、
オゾンガスを前記オゾン水生成部で前記低濃度オゾン水生成部から供給された低濃度オゾン水に溶解させて高濃度オゾン水として取り出しオゾン水製造装置以外の箇所に供給し、
前記オゾン水生成部からの排オゾンガスを前記低濃度オゾン水生成部で純水に溶解して低濃度オゾン水を得て、一部を低濃度オゾン水として取り出しオゾン水製造装置以外の箇所に供給し、残部の低濃度オゾン水を前記オゾン水生成部に供給し、
前記途中で取り出した低濃度オゾン水の方が、前記最後まで溶解させた高濃度オゾン水より、濃度が低く、
前記低濃度オゾン水生成部及び前記オゾン水生成部は、膜を介してオゾンガスを溶解させ、オゾン水を生成し、
前記途中で取り出した低濃度オゾン水及び前記最後まで溶解させた高濃度オゾン水の各々のオゾン水濃度を測定し、その差が大きくなったときには高濃度側の膜の劣化を前もって予知する警報を発信することを特徴とするオゾン水生成方法である。
The invention according to claim 1 adds ozone gas to at least one of pure water or carbonic acid-containing pure water obtained by dissolving carbon dioxide in pure water,
Also, add ozone gas with carbon dioxide added to pure water,
In the method of generating ozone water,
A low-concentration ozone water generation unit that dissolves the ozone gas and extracts a portion of the ozone gas as low-concentration ozone water in the middle of generating ozone water;
An ozone water generation unit that generates and takes out high-concentration ozone water dissolved to the end,
Ozone gas is dissolved in the low-concentration ozone water supplied from the low-concentration ozone water generation unit in the ozone water generation unit, taken out as high-concentration ozone water, and supplied to places other than the ozone water production device,
Exhaust ozone gas from the ozone water generator is dissolved in pure water at the low-concentration ozone water generator to obtain low-concentration ozone water, and a part is taken out as low-concentration ozone water and supplied to places other than the ozone water production apparatus And supplying the remaining low-concentration ozone water to the ozone water generator,
Towards the low concentration ozone water taken out the halfway, higher concentrations of ozone water by dissolving up to the last concentration is rather low,
The low-concentration ozone water generation unit and the ozone water generation unit dissolve ozone gas through a film to generate ozone water,
Measure the ozone water concentration of each of the low-concentration ozone water taken out along the way and the high-concentration ozone water dissolved to the end, and when the difference becomes large, an alarm predicts in advance the deterioration of the high-concentration side film. It is the ozone water generation method characterized by transmitting .

請求項に記載の発明は、純水、または純水に炭酸ガスを溶解して得られた炭酸含有純水の少なくとも一方にオゾンガスを添加し、
また純水に炭酸ガスが添加されたオゾンガスを添加し、オゾン水を生成する装置において、
前記オゾンガスを溶解させ、オゾン水を生成している途中でその一部を低濃度オゾン水として取り出す低濃度オゾン水生成部と、
最後まで溶解させた高濃度オゾン水を生成して取り出すオゾン水生成部とを備え、
オゾンガスを前記オゾン水生成部で前記低濃度オゾン水生成部から供給された低濃度オゾン水に溶解させて高濃度オゾン水として取り出しオゾン水製造装置以外の箇所に供給し、
前記オゾン水生成部からの排オゾンガスを前記低濃度オゾン水生成部で純水に溶解して低濃度オゾン水を得て、一部を低濃度オゾン水として取り出しオゾン水製造装置以外の箇所に供給し、残部の低濃度オゾン水を前記オゾン水生成部に供給し、
前記途中で取り出した低濃度オゾン水の方が、前記最後まで溶解させた高濃度オゾン水より、濃度が低く、
前記低濃度オゾン水生成部及び前記オゾン水生成部は、膜を介して前記オゾンガスを溶解させ、オゾン水を生成し、
前記途中で取り出した低濃度オゾン水及び前記最後まで溶解させた高濃度オゾン水の各々のオゾン水濃度を測定するオゾン水濃度測定部を有し、
前記オゾン水濃度測定部は、前記各々のオゾン水濃度の差が大きくなったときには高濃度側の膜の劣化を前もって予知する警報を発信することを特徴とするオゾン水製造装置である。
The invention according to claim 2 adds ozone gas to at least one of pure water or carbonic acid-containing pure water obtained by dissolving carbon dioxide in pure water,
In addition, in an apparatus for generating ozone water by adding ozone gas in which carbon dioxide gas is added to pure water,
A low-concentration ozone water generation unit that dissolves the ozone gas and extracts a portion of the ozone gas as low-concentration ozone water in the middle of generating ozone water;
An ozone water generation unit that generates and takes out high-concentration ozone water dissolved to the end,
Ozone gas is dissolved in the low-concentration ozone water supplied from the low-concentration ozone water generation unit in the ozone water generation unit, taken out as high-concentration ozone water, and supplied to places other than the ozone water production device,
Exhaust ozone gas from the ozone water generator is dissolved in pure water at the low-concentration ozone water generator to obtain low-concentration ozone water, and a part is taken out as low-concentration ozone water and supplied to places other than the ozone water production apparatus And supplying the remaining low-concentration ozone water to the ozone water generator,
Towards the low concentration ozone water taken out the halfway, higher concentrations of ozone water by dissolving up to the last concentration is rather low,
The low-concentration ozone water generation unit and the ozone water generation unit dissolve the ozone gas through a film to generate ozone water,
An ozone water concentration measuring unit for measuring the concentration of each of the low-concentration ozone water taken out in the middle and the high-concentration ozone water dissolved up to the end;
The ozone water concentration measuring unit is an ozone water producing apparatus characterized in that when the difference between the respective ozone water concentrations becomes large, an alarm for predicting in advance the deterioration of the film on the high concentration side is transmitted.

以下、この発明を詳細に説明する。例えば、オゾン水濃度100mg/lと10mg/lを同時に供給する装置の場合、2台のオゾン装置に対し、1台で行った場合には費用は2/3になった。   Hereinafter, the present invention will be described in detail. For example, in the case of an apparatus that supplies ozone water concentrations of 100 mg / l and 10 mg / l at the same time, the cost is reduced to 2/3 when one apparatus is used for two ozone apparatuses.

この発明では、1台の装置で、異なる濃度のオゾン水を2箇所以上供給することにより、生成するオゾン水の濃度の変動を抑え、高濃度で安定した安価なオゾン水生成が可能となった。   In this invention, by supplying two or more ozone waters having different concentrations with a single device, fluctuations in the concentration of the generated ozone water can be suppressed, and stable and inexpensive ozone water generation can be achieved. .

次に、この発明に係わるオゾン水製造装置に関する詳細の条件について説明する。純水にオゾンガスを溶解させオゾン水にする方法にはいくつかの方法があり、その方法によってオゾン水濃度は多少変わってくる。しかしながら、オゾン水濃度を決定する大きな因子は、オゾンガス量、及びオゾンガス濃度であることは当然であるが、純水の水質が大きく関係していることが最近わかってきた。   Next, detailed conditions regarding the ozone water production apparatus according to the present invention will be described. There are several methods for dissolving ozone gas in pure water to make ozone water, and the ozone water concentration varies somewhat depending on the method. However, it is natural that the major factors that determine the concentration of ozone water are the amount of ozone gas and the concentration of ozone gas, but it has recently been found that the quality of pure water is greatly related.

ここで純水とは、通常の水道水の比抵抗が1/100〜1/200MΩcmであるのに対し、その中のメタルコンタミネーションを除去することで1MΩcm以上の純度にしたものをいう。   Here, the pure water has a specific resistance of 1/100 to 1/200 MΩcm, while having a specific resistance of 1 MΩcm or more by removing metal contamination therein.

半導体では、更に水の純度を上げ、比抵抗では18MΩcm以上の超純水にしたものや、最近では更に純度の高い、比抵抗は18.24MΩcmの極限に近づき、TOCや一般の金属コンタミネーションは検出下限まで純度を上げた超超純水が使用されるようになってきている。   In semiconductors, the purity of water is further increased, and the specific resistance is made to be ultrapure water of 18 MΩcm or more. Recently, the purity is further increased and the specific resistance is approaching the limit of 18.24 MΩcm, and TOC and general metal contamination are Ultra-pure water whose purity has been increased to the lower detection limit has been used.

上記の超純水や、超超純水にオゾンガスを溶解させてオゾン水を生成し、同時に2箇所以上に供給することは、通常2台のオゾン水装置を用いて行っている。 しかしながら、2台のオゾン水装置が各々のオゾン濃度計によりコントロールされてオゾン水を生成するので、洗浄側との信号のやり取りが非常に煩雑であった。   Usually, ozone water is dissolved in the above-described ultrapure water or ultrapure water to generate ozone water and simultaneously supply it to two or more locations using two ozone water devices. However, since the two ozone water devices are controlled by the respective ozone concentration meters to generate ozone water, the exchange of signals with the cleaning side is very complicated.

また、各々のオゾン水が安定に動作するためのコントロールは各々別々の装置で行っている為、その判断が難しく、ましてや、予防的に装置の経時劣化を前もって予知することは不可能であった。   In addition, since control for each ozone water to operate stably is performed by a separate device, it is difficult to make a judgment, and moreover, it is impossible to predict the deterioration of the device over time proactively. .

しかしながら、1台の装置にし、その各々のオゾン水濃度を測定し、以前の状態と比較することにより、装置の経時劣化を推測することが可能となった。   However, it is possible to estimate the deterioration of the apparatus over time by measuring the ozone water concentration of each apparatus and comparing it with the previous state.

たとえば、オゾンガスを純水に溶解しオゾン水を生成するときの方法のひとつとして、膜を介してオゾンガスを純水に溶解させる方法がある。高濃度のオゾン水を生成するときには、膜を何段も介して溶解させている。   For example, as a method for generating ozone water by dissolving ozone gas in pure water, there is a method of dissolving ozone gas in pure water through a membrane. When producing high-concentration ozone water, the membrane is dissolved through many stages.

オゾンガスと純水は、いわゆるカウンターフローで接触する。いくつもの実験の結果、膜は、高濃度のオゾンガスと接触している膜の方が、低濃度のオゾンガスと接触している膜より経時劣化が激しいことがわかっている。   Ozone gas and pure water come into contact with each other by so-called counter flow. As a result of several experiments, it has been found that the film in contact with high-concentration ozone gas is more deteriorated with time than the film in contact with low-concentration ozone gas.

したがって、1台の装置で、高濃度のオゾンガスと接触し、高濃度オゾン水を生成するものと、低濃度になったオゾンガスと接触し、低濃度オゾン水を生成するものとを、オゾン水濃度測定部により各々のオゾン水濃度を測定して定期的に比較することで、高濃度側の膜の劣化を前もって予知することが可能となり、実際に劣化する前に膜を交換することで、装置を長期間停止することなく、連続的に運転することが出来るようになった。
Thus, a single apparatus, in contact with a high concentration of ozone gas, as to generate a high concentration ozone water, contact with ozone gas in a low concentration, and thereby generating a low concentration ozone water, ozone water concentration By measuring each ozone water concentration by the measurement unit and comparing it periodically, it becomes possible to predict in advance the deterioration of the membrane on the high concentration side, and by replacing the membrane before it actually deteriorates, the device Can be operated continuously without stopping for a long time.

この発明では、簡単に、安定した、しかも2通りの濃度のオゾン水を生成するための方
法として、オゾンガスを溶解させ、オゾン水を生成している途中でその一部をオゾン水として取り出し、最後まで溶解させたオゾン水を生成して取り出し、それぞれオゾン水製造装置以外の箇所に供給して使用する
In the present invention, as a method for generating ozone water having two concentrations in a simple and stable manner, ozone gas is dissolved and a part of the ozone water is taken out while the ozone water is being generated. Ozone water dissolved up to is generated and taken out, and supplied to locations other than the ozone water production apparatus for use .

前記構成により、この発明は、以下のような効果を有する。   With the above configuration, the present invention has the following effects.

前記したように、この発明では、常に安定した濃度のオゾン水を得ることができる。また、高濃度のオゾン水と低濃度のオゾン水が同時に生成できる。更には、前もって溶解膜による劣化を前もって予測でき、交換することにより、長期にわたり安定した濃度のオゾン水発生装置を得ることが可能となった。   As described above, in the present invention, ozone water having a stable concentration can be obtained at all times. Moreover, high concentration ozone water and low concentration ozone water can be generated simultaneously. Furthermore, it is possible to predict in advance the deterioration due to the dissolved membrane in advance, and by exchanging it, it is possible to obtain an ozone water generator having a stable concentration over a long period of time.

以下、この発明のオゾン水生成方法及びオゾン水製造装置の実施の形態について説明する。また、この発明の実施の形態は、発明の最も好ましい形態を示すものであり、この発明はこれに限定されない。   Hereinafter, embodiments of the ozone water generating method and the ozone water producing apparatus of the present invention will be described. The embodiment of the present invention shows the most preferable mode of the present invention, and the present invention is not limited to this.

次に、添付図面に基づいて、この発明に係わる実施の形態の一例を示す。   Next, an example of an embodiment according to the present invention will be described based on the attached drawings.

図1は、一般的なオゾン水生成の概念図であり、図2は、この発明の実施の形態に係わるオゾン水生成で1台の装置で2つ異なる濃度のオゾン水を供給する概念図である。   FIG. 1 is a conceptual diagram of general ozone water generation, and FIG. 2 is a conceptual diagram for supplying ozone water of two different concentrations with one apparatus for ozone water generation according to the embodiment of the present invention. is there.

図1において、オゾン水生成では、純水1は、オゾン水生成部3に導かれる。同様にオゾン水生成部3にはオゾンガス4が供給される。オゾン水生成部3にて純水1は供給されたオゾンガス4によってオゾン水となりオゾン水生成部3から吐出されオゾン水2として供給される。オゾン水生成部3でオゾン水とならなかったオゾンガスは、排オゾンガスとしてオゾンガス処理部5にて処理される。   In FIG. 1, in the ozone water generation, pure water 1 is guided to the ozone water generation unit 3. Similarly, ozone gas 4 is supplied to the ozone water generator 3. The pure water 1 is converted into ozone water by the supplied ozone gas 4 in the ozone water generation unit 3 and is discharged from the ozone water generation unit 3 and supplied as ozone water 2. Ozone gas that has not become ozone water in the ozone water generation unit 3 is processed in the ozone gas processing unit 5 as exhaust ozone gas.

図2において、オゾン水生成では、純水1は、低濃度オゾン水生成部3bに導かれる。同様に低濃度オゾン水生成部3bには高濃度のオゾン水生成部3を経由した経由オゾンガス4bが供給される。オゾン水生成部3にて純水1は供給されたオゾンガス4bによってオゾン水となり低濃度オゾン水生成部3bから吐出され低濃度オゾン水6として供給される。さらに同一濃度の経由オゾン水2bは、さらにオゾン水生成部3に導かれる。同様にオゾン水生成部3にはオゾンガス4が供給される。オゾン水生成部3にて経由オゾン水2bは供給されたオゾンガス4によって高濃度オゾン水となりオゾン水生成部3から吐出されオゾン水2として供給される。オゾン水生成部3でオゾン水とならなかったオゾンガスは、排オゾンガスとしてオゾンガス処理部5にて処理される。   In FIG. 2, in the ozone water generation, the pure water 1 is guided to the low-concentration ozone water generation unit 3b. Similarly, the low-concentration ozone water generation unit 3b is supplied with the passing ozone gas 4b via the high-concentration ozone water generation unit 3. The pure water 1 is converted into ozone water by the supplied ozone gas 4 b in the ozone water generation unit 3 and is discharged from the low concentration ozone water generation unit 3 b and supplied as low concentration ozone water 6. Further, the via ozone water 2 b having the same concentration is further guided to the ozone water generating unit 3. Similarly, ozone gas 4 is supplied to the ozone water generator 3. In the ozone water generation unit 3, the via ozone water 2 b becomes high-concentration ozone water by the supplied ozone gas 4 and is discharged from the ozone water generation unit 3 and supplied as ozone water 2. Ozone gas that has not become ozone water in the ozone water generation unit 3 is processed in the ozone gas processing unit 5 as exhaust ozone gas.

オゾン水生成部3でのオゾン水の溶解は、図示しない膜を介してオゾンガスを溶解させ、オゾン水を生成する。   In the ozone water generation unit 3, the ozone water is dissolved by dissolving ozone gas through a film (not shown) to generate ozone water.

途中で取り出した低濃度オゾン水6、および最後まで溶解させたオゾン水2の各々のオゾン水濃度を、オゾン水濃度測定部10により測定し、その差が大きくなったときには警報を発信する。   The ozone water concentration of each of the low-concentration ozone water 6 taken out in the middle and the ozone water 2 dissolved to the end is measured by the ozone water concentration measuring unit 10, and an alarm is issued when the difference becomes large.

図1及び図2においては、純水1にオゾンガス4を添加しているが、炭酸水にオゾンガス4を添加するものでもよく、また純水1及び炭酸水にオゾンガス4を添加するものでもよい。また、純水1に炭酸ガスが添加されたオゾンガス4を添加してもよい。   1 and 2, ozone gas 4 is added to pure water 1, but ozone gas 4 may be added to carbonated water, or ozone gas 4 may be added to pure water 1 and carbonated water. Further, ozone gas 4 in which carbon dioxide gas is added to pure water 1 may be added.

[実施例]
次に、この発明に係わるオゾン発生装置の実施例を記載するが、この実施例はこの発明を限定するものではない。
(実施例1)
オゾン水濃度100mg/lと10mg/lを同時に供給する装置を用いてオゾン水生成を行った。
[Example]
Next, although the Example of the ozone generator concerning this invention is described, this Example does not limit this invention.
Example 1
Ozone water was generated using an apparatus that simultaneously supplied ozone water concentrations of 100 mg / l and 10 mg / l.

当初は非常に安定していたオゾン水濃度が、2年を経過したところオゾン水濃度が90mg/lに低下してきた。しかしながら、低濃度側の10mg/lのオゾン水濃度には変化は無かった。   When the concentration of ozone water, which was very stable at the beginning, passed 2 years, the concentration of ozone water decreased to 90 mg / l. However, there was no change in the ozone water concentration of 10 mg / l on the low concentration side.

(比較例1)
オゾン水濃度100mg/lと10mg/lの2台のオゾン水装置を用いてオゾン水生成を行った。オゾン水濃度は2台の間でばらつき、2年経過したときには、各々90〜100mg/l,8〜10mg/lでオゾン水濃度が膜の経時劣化による変化かどうか判断が出来なかった。
(Comparative Example 1)
Ozone water generation was performed using two ozone water devices with ozone water concentrations of 100 mg / l and 10 mg / l. The ozone water concentration varied between the two units, and when two years passed, it was not possible to determine whether the ozone water concentration was changed due to deterioration of the film over time at 90 to 100 mg / l and 8 to 10 mg / l, respectively.

オゾンガスを溶解させ、オゾン水を生成している途中でその一部をオゾン水として取り出し、最後まで溶解させたオゾン水と同時に使用し、長期間にわたり連続的で、また、常に安定した2つ以上の濃度のオゾン水を得る。   Dissolve ozone gas, take out part of it as ozone water, and use it simultaneously with ozone water dissolved to the end. To obtain ozone water of concentration.

一般的なオゾン水生成の概念図である。It is a conceptual diagram of general ozone water generation. この発明の実施の形態に係わるオゾン水生成で1台の装置で2つ異なる濃度のオゾン水を供給する概念図である。It is a conceptual diagram which supplies ozone water of two different density | concentration with one apparatus by the ozone water production | generation concerning embodiment of this invention.

符号の説明Explanation of symbols

1 純水
2 オゾン水
3 オゾン水生成部
4 オゾンガス
5 オゾンガス処理部
2b 経由オゾン水
3b 低濃度オゾン水生成部
4b 経由オゾンガス
6 低濃度オゾン水
10 オゾン水濃度測定部
DESCRIPTION OF SYMBOLS 1 Pure water 2 Ozone water 3 Ozone water production | generation part 4 Ozone gas 5 Ozone gas processing part 2b Via ozone water 3b Low concentration ozone water production | generation part 4b Via ozone gas 6 Low concentration ozone water 10 Ozone water concentration measurement part

Claims (2)

純水、または純水に炭酸ガスを溶解して得られた炭酸含有純水の少なくとも一方にオゾンガスを添加し、
また、純水に炭酸ガスが添加されたオゾンガスを添加し、
オゾン水を生成する方法において、
前記オゾンガスを溶解させ、オゾン水を生成している途中でその一部を低濃度オゾン水として取り出す低濃度オゾン水生成部と、
最後まで溶解させた高濃度オゾン水を生成して取り出すオゾン水生成部とを備え、
オゾンガスを前記オゾン水生成部で前記低濃度オゾン水生成部から供給された低濃度オゾン水に溶解させて高濃度オゾン水として取り出しオゾン水製造装置以外の箇所に供給し、
前記オゾン水生成部からの排オゾンガスを前記低濃度オゾン水生成部で純水に溶解して低濃度オゾン水を得て、一部を低濃度オゾン水として取り出しオゾン水製造装置以外の箇所に供給し、残部の低濃度オゾン水を前記オゾン水生成部に供給し、
前記途中で取り出した低濃度オゾン水の方が、前記最後まで溶解させた高濃度オゾン水より、濃度が低く、
前記低濃度オゾン水生成部及び前記オゾン水生成部は、膜を介してオゾンガスを溶解させ、オゾン水を生成し、
前記途中で取り出した低濃度オゾン水及び前記最後まで溶解させた高濃度オゾン水の各々のオゾン水濃度を測定し、その差が大きくなったときには高濃度側の膜の劣化を前もって予知する警報を発信することを特徴とするオゾン水生成方法
Add ozone gas to pure water or at least one of carbonated pure water obtained by dissolving carbon dioxide in pure water,
Also, add ozone gas with carbon dioxide added to pure water,
In the method of generating ozone water,
A low-concentration ozone water generation unit that dissolves the ozone gas and extracts a portion of the ozone gas as low-concentration ozone water in the middle of generating ozone water;
An ozone water generation unit that generates and takes out high-concentration ozone water dissolved to the end,
Ozone gas is dissolved in the low-concentration ozone water supplied from the low-concentration ozone water generation unit in the ozone water generation unit, taken out as high-concentration ozone water, and supplied to places other than the ozone water production device,
Exhaust ozone gas from the ozone water generator is dissolved in pure water at the low-concentration ozone water generator to obtain low-concentration ozone water, and a part is taken out as low-concentration ozone water and supplied to places other than the ozone water production apparatus And supplying the remaining low-concentration ozone water to the ozone water generator,
Towards the low concentration ozone water taken out the halfway, higher concentrations of ozone water by dissolving up to the last concentration is rather low,
The low-concentration ozone water generation unit and the ozone water generation unit dissolve ozone gas through a film to generate ozone water,
Measure the ozone water concentration of each of the low-concentration ozone water taken out along the way and the high-concentration ozone water dissolved to the end, and when the difference becomes large, an alarm predicts in advance the deterioration of the high-concentration side film. A method for generating ozone water characterized by transmitting .
純水、または純水に炭酸ガスを溶解して得られた炭酸含有純水の少なくとも一方にオゾンガスを添加し、
また純水に炭酸ガスが添加されたオゾンガスを添加し、オゾン水を生成する装置において、
前記オゾンガスを溶解させ、オゾン水を生成している途中でその一部を低濃度オゾン水として取り出す低濃度オゾン水生成部と、
最後まで溶解させた高濃度オゾン水を生成して取り出すオゾン水生成部とを備え、
オゾンガスを前記オゾン水生成部で前記低濃度オゾン水生成部から供給された低濃度オゾン水に溶解させて高濃度オゾン水として取り出しオゾン水製造装置以外の箇所に供給し、
前記オゾン水生成部からの排オゾンガスを前記低濃度オゾン水生成部で純水に溶解して低濃度オゾン水を得て、一部を低濃度オゾン水として取り出しオゾン水製造装置以外の箇所に供給し、残部の低濃度オゾン水を前記オゾン水生成部に供給し、
前記途中で取り出した低濃度オゾン水の方が、前記最後まで溶解させた高濃度オゾン水より、濃度が低く、
前記低濃度オゾン水生成部及び前記オゾン水生成部は、膜を介して前記オゾンガスを溶解させ、オゾン水を生成し、
前記途中で取り出した低濃度オゾン水及び前記最後まで溶解させた高濃度オゾン水の各々のオゾン水濃度を測定するオゾン水濃度測定部を有し、
前記オゾン水濃度測定部は、前記各々のオゾン水濃度の差が大きくなったときには高濃度側の膜の劣化を前もって予知する警報を発信することを特徴とするオゾン水製造装置。
Add ozone gas to pure water or at least one of carbonated pure water obtained by dissolving carbon dioxide in pure water,
In addition, in an apparatus for generating ozone water by adding ozone gas in which carbon dioxide gas is added to pure water,
A low-concentration ozone water generation unit that dissolves the ozone gas and extracts a portion of the ozone gas as low-concentration ozone water in the middle of generating ozone water;
An ozone water generation unit that generates and takes out high-concentration ozone water dissolved to the end,
Ozone gas is dissolved in the low-concentration ozone water supplied from the low-concentration ozone water generation unit in the ozone water generation unit, taken out as high-concentration ozone water, and supplied to places other than the ozone water production device,
Exhaust ozone gas from the ozone water generator is dissolved in pure water at the low-concentration ozone water generator to obtain low-concentration ozone water, and a part is taken out as low-concentration ozone water and supplied to places other than the ozone water production apparatus And supplying the remaining low-concentration ozone water to the ozone water generator,
Towards the low concentration ozone water taken out the halfway, higher concentrations of ozone water by dissolving up to the last concentration is rather low,
The low-concentration ozone water generation unit and the ozone water generation unit dissolve the ozone gas through a film to generate ozone water,
An ozone water concentration measuring unit for measuring the concentration of each of the low-concentration ozone water taken out in the middle and the high-concentration ozone water dissolved up to the end;
The ozone water concentration measuring apparatus transmits an alarm for predicting in advance the deterioration of the high-concentration side film when the difference between the ozone water concentrations becomes large .
JP2004238692A 2004-08-18 2004-08-18 Ozone water generation method and ozone water production apparatus Expired - Lifetime JP3777451B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004238692A JP3777451B2 (en) 2004-08-18 2004-08-18 Ozone water generation method and ozone water production apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004238692A JP3777451B2 (en) 2004-08-18 2004-08-18 Ozone water generation method and ozone water production apparatus

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2005305674A Division JP2006102745A (en) 2005-10-20 2005-10-20 Method and apparatus for producing ozone water

Publications (2)

Publication Number Publication Date
JP2006055719A JP2006055719A (en) 2006-03-02
JP3777451B2 true JP3777451B2 (en) 2006-05-24

Family

ID=36103639

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004238692A Expired - Lifetime JP3777451B2 (en) 2004-08-18 2004-08-18 Ozone water generation method and ozone water production apparatus

Country Status (1)

Country Link
JP (1) JP3777451B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN119735291A (en) * 2018-08-29 2025-04-01 Mks仪器公司 Ozone water delivery system and method of use thereof
JP6670910B1 (en) * 2018-10-26 2020-03-25 リオウ、フエイ タルングLiou, Huei Tarng Gas dissolution system with double mixer

Also Published As

Publication number Publication date
JP2006055719A (en) 2006-03-02

Similar Documents

Publication Publication Date Title
Tlili et al. Influence of the interfacial pH on electrochemical CaCO3 precipitation
JP5213601B2 (en) Circulating ozone water generation method and circulating ozone water production apparatus
JP6591093B1 (en) Ozone water generation apparatus, water treatment apparatus, ozone water generation method, and cleaning method
WO2015075835A1 (en) Control method and control program for water treatment facility and water treatment system
KR20170044609A (en) Exhaust gas treatment device and waste water treatment method for exhaust gas treatment device
JP5796419B2 (en) Water treatment method and water treatment apparatus
JP3777451B2 (en) Ozone water generation method and ozone water production apparatus
JP5659968B2 (en) Water quality analyzer
JP5943196B2 (en) Water treatment facility control method, control program, and water treatment system
JP2006102745A (en) Method and apparatus for producing ozone water
JP6616583B2 (en) Organic acid solution decomposition system and organic acid solution decomposition method
CN114031209B (en) Method for supervising and treating water in thermal power plant
JP4299515B2 (en) Hydrogen water production equipment
JP2006150320A (en) Wastewater pyrolysis system
JP3743768B2 (en) Ozone water generation method and ozone water production apparatus
JP2006322777A (en) Fluid measuring instrument
JP2007152285A (en) Liquid processing method and apparatus
JP6031795B2 (en) Ion exchange device breakthrough detection method and operation method
KR20130102288A (en) Flow measurement and control methods for ballast water treatment system
JP2005334755A (en) Exhaust gas abatement apparatus, abatement method therefor, and electronic device manufacturing system
JP3979172B2 (en) Method and apparatus for producing pure water and scale monitor apparatus
KR100304854B1 (en) Underwater Sterilization and Disinfection Equipment Using Current Modulation Metal Ion
JP4116931B2 (en) Ozone treatment method and ozone treatment system
JP5843600B2 (en) Method for generating and injecting dilute aqueous sodium hypochlorite solution
JP2019155296A (en) Pure water production apparatus

Legal Events

Date Code Title Description
A911 Transfer to examiner for re-examination before appeal (zenchi)

Free format text: JAPANESE INTERMEDIATE CODE: A911

Effective date: 20060118

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20060209

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20060209

R150 Certificate of patent or registration of utility model

Ref document number: 3777451

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090310

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100310

Year of fee payment: 4

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110310

Year of fee payment: 5

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110310

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120310

Year of fee payment: 6

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120310

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130310

Year of fee payment: 7

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140310

Year of fee payment: 8

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

EXPY Cancellation because of completion of term