JP5213601B2 - Circulating ozone water generation method and circulating ozone water production apparatus - Google Patents
Circulating ozone water generation method and circulating ozone water production apparatus Download PDFInfo
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この発明は、ポンプを使った循環式オゾン水生成方法及び循環式オゾン水製造装置に関し、より詳細には、オゾン水濃度をより安定にし、また、オゾン水濃度を高濃度にし、しかも安価な循環式オゾン水生成方法及び循環式オゾン水製造装置に関する。 The present invention relates to a circulating ozone water generation method and a circulating ozone water production apparatus using a pump. More specifically, the ozone water concentration is more stable, the ozone water concentration is high, and the circulation is inexpensive. The present invention relates to an ozone water generation method and a circulating ozone water production apparatus.
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きた。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 used widely 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、また常に高濃度に保つこと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、安定なオゾン水濃度の水を長期にわたって生成することは困難であった。 However, in semiconductors and liquid crystals, it is often required to keep the ozone water concentration stable and always kept at a high concentration, which is still insufficient and produces water with a stable ozone water concentration over a long period of time. It was difficult.
また、オゾン水の作り方等によっても、その後のオゾン水濃度の減衰が大きく変わってくることより、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。 In addition, the ozone water concentration in the actual cleaning tank fluctuated greatly because the attenuation of the ozone water concentration changed greatly depending on how the ozone water was made.
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った。 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 much higher concentration than actually required.
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、オゾン水濃度の範囲の限定が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, the limitation of the ozone water concentration range has become 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に極限に近づき、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 quality of such pure water has a specific resistance approaching the limit of 18.24 MΩcm, and TOC and general metal contamination are 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。 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.
このため、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きた。 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 ozone gas to generate carbonated 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でき、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得ることができるようになってきた(例えば、特許文献1)。
しかしながら、炭酸が添加されているオゾン水を生成する方法は、いずれも純水に炭酸ガスを添加する工程が必要であり、生成コストが嵩むなどの問題があった。 However, all the methods for generating ozone water to which carbonic acid is added require a step of adding carbon dioxide gas to pure water, and there are problems such as an increase in production cost.
この発明は、前述の従来技術の問題点を解消し、生成したオゾンガスを有効に利用することができ、オゾン水濃度をより安定にし、また、オゾン水濃度を高濃度にし、しかも安価な循環式オゾン水生成方法及び循環式オゾン水製造装置を提供することを目的とする。 The present invention solves the above-mentioned problems of the prior art, can effectively use the generated ozone gas, makes the ozone water concentration more stable, makes the ozone water concentration high, and is inexpensive. An object of the present invention is to provide an ozone water generation method and a circulating ozone water production apparatus.
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-described problems and achieve the object, the present invention is configured as follows.
請求項1に記載の発明は、ポンプにてオゾン水を循環させ、その途中にオゾンガス、及び純水を注入してオゾンガスを溶解してオゾン水を生成する循環式オゾン水生成方法において、
オゾン水を循環するオゾン水循環ラインとは別にオゾンガス接触機構を備え、
オゾン水の生成により排出される排オゾンガスを前記オゾンガス接触機構に供給し、
前記オゾンガス接触機構により供給される純水と前記排オゾンガスを接触させて純水に排オゾンガスを溶解し、
前記オゾンガス接触機構を介して前記排オゾンガスを溶解したオゾン水を前記オゾン水循環ラインに供給することを特徴とする循環式オゾン水生成方法である。
The invention according to claim 1 is a circulating ozone water generation method in which ozone water is circulated by a pump, ozone gas and pure water are injected in the middle thereof to dissolve ozone gas and generate ozone water.
Apart from the ozone water circulation line that circulates ozone water, it has an ozone gas contact mechanism,
Supplying exhaust ozone gas discharged by generation of ozone water to the ozone gas contact mechanism;
The dissolving discharge ozone ozone gas contact mechanism wherein contacting the exhaust ozone gas and pure water supplied by it in pure water,
A circulating ozone water producing method characterized that you supplying ozone water obtained by dissolving the exhaust ozone gas through the ozone gas contact mechanism with the ozone water circulation line.
請求項2に記載の発明は、前記オゾンガス接触機構を介して前記純水が前記オゾン水となる構造は、フッ素樹脂で形成された膜を有し、
一方に前記純水を、他方に前記排オゾンガスを導入して前記膜を介して前記排オゾンガスが前記純水に溶け込み、前記純水を前記オゾン水にする構造であることを特徴とする請求項1に記載の循環式オゾン水生成方法である。
According to a second aspect of the present invention, the structure in which the pure water becomes the ozone water through the ozone gas contact mechanism has a film formed of a fluororesin,
Claim Meanwhile wherein the pure water, and introducing the exhaust ozone gas to the other penetration into the exhaust ozone gas the pure water through the membrane, wherein said a structure pure water to the ozone water 1. A circulating ozone water generation method according to 1.
請求項3に記載の発明は、前記一度使用された排オゾンガスのオゾンガス濃度を測定することにより、演算をして前記循環するオゾン水に注入される前記オゾンガスのオゾンガス量、及び/またはオゾンガス濃度をコントロールすることを特徴とする請求項1または請求項2に記載の循環式オゾン水生成方法である。 According to a third aspect of the present invention, the ozone gas concentration and / or ozone gas concentration of the ozone gas injected into the circulating ozone water is calculated by measuring the ozone gas concentration of the exhaust ozone gas once used. It is controlled, It is the circulation type ozone water production | generation method of Claim 1 or Claim 2 characterized by the above-mentioned.
請求項4に記載の発明は、前記オゾンガス接触機構によりオゾン水になったオゾン水濃度を測定することにより、演算をして前記循環するオゾン水に注入される前記オゾンガスのオゾンガス量、及び/またはオゾンガス濃度をコントロールすることを特徴とする請求項1または請求項2に記載の循環式オゾン水生成方法である。 The invention according to claim 4 is an ozone gas amount of the ozone gas that is calculated and injected into the circulating ozone water by measuring the concentration of ozone water that has become ozone water by the ozone gas contact mechanism, and / or The circulating ozone water generation method according to claim 1 or 2, wherein the ozone gas concentration is controlled.
請求項5に記載の発明は、ポンプにてオゾン水を循環するオゾン水循環ラインを有し、その途中にオゾンガス、及び純水を注入してオゾンガスを溶解してオゾン水を生成する循環式オゾン水製造装置において、
オゾン水を循環するオゾン水循環ラインとは別にオゾンガス接触機構を備え、
オゾン水の生成により排出される排オゾンガスを前記オゾンガス接触機構に供給し、
前記オゾンガス接触機構により供給される純水と前記排オゾンガスを接触させ純水に排オゾンガスを溶解し、
前記オゾンガス接触機構を介して前記排オゾンガスを溶解したオゾン水を前記オゾン水循環ラインに供給することを特徴とすることを特徴とする循環式オゾン水製造装置である。
Invention of Claim 5 has the ozone water circulation line which circulates ozone water with a pump, inject | pours ozone gas and a pure water in the middle, the circulation type ozone water which melt | dissolves ozone gas and produces | generates ozone water In manufacturing equipment,
Apart from the ozone water circulation line that circulates ozone water, it has an ozone gas contact mechanism ,
Supplying exhaust ozone gas discharged by generation of ozone water to the ozone gas contact mechanism;
Dissolving the waste ozone gas in pure water is contacted with the exhaust ozone gas and pure water supplied by the ozone gas contact mechanism,
The circulating ozone water producing apparatus is characterized in that ozone water in which the exhaust ozone gas is dissolved is supplied to the ozone water circulation line through the ozone gas contact mechanism.
請求項6に記載の発明は、前記オゾンガス接触機構を介して前記純水が前記オゾン水となる構造は、フッ素樹脂で形成された膜を有し、
一方に前記純水を、他方に前記排オゾンガスを導入して前記膜を介して前記排オゾンガスが前記純水に溶け込み、前記純水を前記オゾン水にする構造であることを特徴とする請求項5に記載の循環式オゾン水製造装置である。
In the invention according to claim 6 , the structure in which the pure water becomes the ozone water through the ozone gas contact mechanism has a film formed of a fluororesin,
Claim Meanwhile wherein the pure water, and introducing the exhaust ozone gas to the other penetration into the exhaust ozone gas the pure water through the membrane, wherein said a structure pure water to the ozone water 5. The circulating ozone water production apparatus according to 5 .
請求項7に記載の発明は、前記オゾンガス接触機構により前記オゾン水になったオゾン水濃度を測定するオゾン水濃度測定手段と、
前記測定したオゾン水濃度に基づき演算をして前記オゾン水循環ラインに注入されるオゾンガスのオゾンガス量、及び/またはオゾンガス濃度をコントロールする制御手段と、
を有することを特徴とする請求項5または請求項6に記載の循環式オゾン水製造装置である。
The invention according to claim 7 is an ozone water concentration measuring means for measuring the concentration of ozone water that has become the ozone water by the ozone gas contact mechanism,
Control means for controlling the ozone gas amount and / or ozone gas concentration of the ozone gas injected into the ozone water circulation line by calculating based on the measured ozone water concentration;
The circulating ozone water production apparatus according to claim 5 or 6 , characterized by comprising:
請求項8に記載の発明は、前記一度使用されたオゾンガスの排オゾンガス濃度を測定するオゾンガス濃度測定手段と、
前記測定したオゾンガス濃度に基づき演算をして前記オゾン水循環ラインに注入される前記オゾンガスのオゾンガス量、及び/またはオゾンガス濃度をコントロールする制御手段と、
を有することを特徴とする請求項5または請求項6に記載の循環式オゾン水製造装置である。
The invention according to claim 8 is an ozone gas concentration measuring means for measuring the exhaust ozone gas concentration of the ozone gas once used,
Control means for controlling the ozone gas amount and / or ozone gas concentration of the ozone gas injected into the ozone water circulation line by calculating based on the measured ozone gas concentration;
The circulating ozone water production apparatus according to claim 5 or 6, characterized by comprising:
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.
請求項1及び請求項5に記載の発明では、純水がオゾンガス接触機構を介してオゾン水となって循環するオゾン水に供給されることで、常に安定な濃度のオゾン水を得ることができ、また、安全であり、省エネルギーの高濃度のオゾン水が常に生成できる。更には、長期にわたり安定な濃度のオゾン水を発生する装置を得ることが可能である。また、オゾンガス接触機構に供給されるオゾンガスは、一度使用された排オゾンガスであり、生成したオゾンガスを有効に利用することができ、省エネルギーである。 In the first and fifth aspects of the invention, pure water is supplied to the ozone water that circulates as ozone water through the ozone gas contact mechanism, so that ozone water having a stable concentration can always be obtained. Also, safe and energy-saving high-concentration ozone water can always be produced. Furthermore, it is possible to obtain an apparatus that generates ozone water having a stable concentration over a long period of time. Further, the ozone gas supplied to the ozone gas contact mechanism is exhaust ozone gas that has been used once, and the generated ozone gas can be used effectively, thereby saving energy.
請求項2及び請求項6に記載の発明では、フッ素樹脂で形成された膜を用いる簡単な構造で、オゾンガスが純水に溶け込み、純水をオゾン水にすることができる。 In the second and sixth aspects of the invention, ozone gas can be dissolved in pure water and the pure water can be made into ozone water with a simple structure using a film formed of a fluororesin.
請求項3及び請求項7に記載の発明では、一度使用された排オゾンガスのオゾンガス濃度に基づき、循環するオゾン水に注入されるオゾンガスのオゾンガス量、及び/またはオゾンガス濃度をコントロールすることで、常に安定な濃度のオゾン水を得ることができ、またオゾンガス処理部における異常発生を防止することができ安全対策にもなる。 In the inventions according to claim 3 and claim 7 , by controlling the ozone gas amount and / or ozone gas concentration of ozone gas injected into the circulating ozone water based on the ozone gas concentration of exhaust ozone gas once used, A stable concentration of ozone water can be obtained, and the occurrence of abnormalities in the ozone gas processing section can be prevented, which is also a safety measure.
請求項4及び請求項8に記載の発明では、オゾンガス接触機構によりオゾン水になったオゾン水濃度に基づき、循環するオゾン水に注入されるオゾンガスのオゾンガス量、及び/またはオゾンガス濃度をコントロールすることで、常に安定な濃度のオゾン水を得ることができ、またオゾンガス処理部における異常発生を防止することができ安全対策にもなる。 In the inventions according to claims 4 and 8 , the ozone gas amount and / or the ozone gas concentration of the ozone gas injected into the circulating ozone water is controlled based on the ozone water concentration that has become ozone water by the ozone gas contact mechanism. Therefore, it is possible to obtain ozone water having a stable concentration at all times, and to prevent occurrence of abnormality in the ozone gas processing unit, which is a safety measure.
以下、この発明の循環式オゾン水生成方法及び循環式オゾン水製造装置の実施の形態について説明する。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。
図1は、一般的なポンプによる循環式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循環式オゾン水生成で供給純水にオゾンガス接触機構が組み込まれた概念図である。図3は、この発明の実施の形態に係わる循環式オゾン水生成で供給純水にオゾン水接触機構、及びオゾンガス濃度測定手段、制御手段が組み込まれた概念図である。又、図4は、この発明の実施の形態に係わる循環式オゾン水生成で供給純水にオゾン水接触機構、及びオゾン水濃度測定手段、制御手段が組み込まれた概念図である。
Hereinafter, embodiments of the circulating ozone water generating method and the circulating 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.
FIG. 1 is a conceptual diagram of circulating ozone water generation by a general pump, and FIG. 2 is a conceptual diagram in which an ozone gas contact mechanism is incorporated in pure water supplied by circulating ozone water generation according to an embodiment of the present invention. FIG. FIG. 3 is a conceptual diagram in which an ozone water contact mechanism, ozone gas concentration measuring means, and control means are incorporated in the pure water supplied in the generation of circulating ozone water according to the embodiment of the present invention. FIG. 4 is a conceptual diagram in which the ozone water contact mechanism, the ozone water concentration measuring means, and the control means are incorporated into the pure water supplied in the generation of circulating ozone water according to the embodiment of the present invention.
図1において、循環式オゾン水生成では、オゾン水1を循環するオゾン水循環ラインR1を有し、オゾン水1は循環ポンプ4によって循環される。循環ポンプ4の入り口側には、純水3、オゾンガス7、及びオゾンガス混合機構5が存在し、オゾン水循環ラインR1の途中にオゾンガス7、及び純水3を注入する注入ラインR2,R3を有する。循環されるオゾン水1は、純水3によって希釈されたのち、オゾンガス混合機構5によってオゾンガス7と混合され、循環ポンプ4によって、さらに混合しオゾン水1となった上でガス分離タンク6に導かれる。 In FIG. 1, the circulation type ozone water generation has an ozone water circulation line R <b> 1 for circulating ozone water 1, and the ozone water 1 is circulated by a circulation pump 4. The pure water 3, the ozone gas 7, and the ozone gas mixing mechanism 5 exist on the inlet side of the circulation pump 4, and have injection lines R2 and R3 for injecting the ozone gas 7 and the pure water 3 in the middle of the ozone water circulation line R1. The circulated ozone water 1 is diluted with pure water 3, mixed with ozone gas 7 by the ozone gas mixing mechanism 5, further mixed by the circulation pump 4 to become ozone water 1, and then introduced into the gas separation tank 6. It is burned.
ガス分離タンク6では、オゾン水とオゾンガスに分離され、オゾン水1は循環ポンプ4にてオゾン水循環ラインR1に循環されるもののほか、ガス分離タンク6から吐出され、吐出オゾン水2として供給される。ガス分離タンク6でオゾン水とならなかったオゾンガスは、排オゾンガス1Aとして導管8を経由してオゾンガス処理部9にて処理される。 In the gas separation tank 6, ozone water and ozone gas are separated. The ozone water 1 is circulated to the ozone water circulation line R 1 by the circulation pump 4, and is discharged from the gas separation tank 6 and supplied as discharge ozone water 2. . The ozone gas that has not become ozone water in the gas separation tank 6 is processed in the ozone gas processing section 9 via the conduit 8 as the exhaust ozone gas 1A.
吐出オゾン水2の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。 Naturally, the major factors that determine the ozone water concentration of the discharged ozone water 2 are the amount of ozone gas and the ozone gas concentration, but the quality of pure water is greatly related. 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.
図2において、排オゾンガス1Aの導管8の途中にオゾンガス接触機構10を設け、このオゾンガス接触機構10は注入ラインR3に配置されており、純水3と接触したのち、排オゾンガス1Aはオゾンガス処理部9にて処理され、また、純水3はオゾンガス接触機構10により供給オゾン水11となる。 In FIG. 2, an ozone gas contact mechanism 10 is provided in the middle of the conduit 8 for the exhaust ozone gas 1A. The ozone gas contact mechanism 10 is disposed in the injection line R3. After contacting the pure water 3, the exhaust ozone gas 1A 9, and the pure water 3 becomes supply ozone water 11 by the ozone gas contact mechanism 10.
このようにして、排オゾンガス1A、及び純水3を注入ラインR3のオゾンガス接触機構10に供給し、オゾンガス接触機構10を介して供給オゾン水11となって注入ラインR3からオゾン水循環ラインR1に供給される。このオゾンガス接触機構10に供給される排オゾンガス1Aは、一度使用されたオゾンガスである。この実施の形態では、ガス分離タンク6により分離された排オゾンガス1Aを用いているが、一度使用されたオゾンガスであればガス分離タンク6により分離されたものに限定されない。 In this way, the exhaust ozone gas 1A and the pure water 3 are supplied to the ozone gas contact mechanism 10 of the injection line R3, and the supply ozone water 11 is supplied via the ozone gas contact mechanism 10 from the injection line R3 to the ozone water circulation line R1. Is done. The exhaust ozone gas 1A supplied to the ozone gas contact mechanism 10 is ozone gas that has been used once. In this embodiment, the exhaust ozone gas 1A separated by the gas separation tank 6 is used. However, the ozone gas is not limited to the one separated by the gas separation tank 6 as long as it is once used.
このオゾンガス接触機構10を介して純水3が供給オゾン水11となる構造は、オゾンガス接触機構10がフッ素樹脂で形成された膜10aを有し、この膜10aによって区画された一方の室10bに純水3を、他方の室10cに供給オゾン水11を導入して膜10aを介して排オゾンガス1Aが純水3に溶け込み、純水3を供給オゾン水11にする構造である。 The structure in which the pure water 3 becomes the supply ozone water 11 through the ozone gas contact mechanism 10 has a film 10a in which the ozone gas contact mechanism 10 is formed of a fluororesin, and is in one chamber 10b partitioned by the film 10a. The pure ozone 3 is introduced into the other chamber 10c, and the exhaust ozone gas 1A is dissolved in the pure water 3 through the membrane 10a to make the pure water 3 into the supplied ozone water 11.
このようにして、排オゾンガス1A、及び純水3をオゾンガス接触機構10を介して供給オゾン水11となって注入ラインR3からオゾン水循環ラインR1を循環するオゾン水1に供給されることで、ガス分離タンク6から吐出される吐出オゾン水2は、常に安定な濃度のオゾン水であり、また、安全であり、省エネルギーの高濃度のオゾン水が常に生成できる。更には、長期にわたり安定な濃度のオゾン水を発生する装置を得ることが可能である。 In this way, the exhaust ozone gas 1A and the pure water 3 become the supply ozone water 11 through the ozone gas contact mechanism 10 and are supplied from the injection line R3 to the ozone water 1 circulating through the ozone water circulation line R1, thereby producing the gas. The discharged ozone water 2 discharged from the separation tank 6 is ozone water with a stable concentration at all times, and is safe and energy-saving high-concentration ozone water can always be generated. Furthermore, it is possible to obtain an apparatus that generates ozone water having a stable concentration over a long period of time.
また、オゾンガス接触機構10に供給されるオゾンガスは、ガス分離タンク6でオゾン水とならなかった排オゾンガス1Aで一度使用されたオゾンガスであり、生成したオゾンガスを有効に利用することができ、省エネルギーである。 Further, the ozone gas supplied to the ozone gas contact mechanism 10 is an ozone gas once used with the exhaust ozone gas 1A that has not become ozone water in the gas separation tank 6, and the generated ozone gas can be used effectively, thereby saving energy. is there.
また、オゾンガス接触機構10は、フッ素樹脂で形成された膜10aを用いる簡単な構造で、排オゾンガス1Aが純水3に溶け込み、純水3を供給オゾン水11にすることができる。 Further, the ozone gas contact mechanism 10 has a simple structure using a film 10a formed of a fluororesin, and the exhaust ozone gas 1A can be dissolved in the pure water 3 so that the pure water 3 can be used as the supply ozone water 11.
図3において、排オゾンガスの導管8の途中にオゾンガス接触機構10を設け、純水3と接触したのち、排オゾンガス1Aはオゾンガス処理部9にて処理される。また、純水3はオゾンガス接触機構10により供給オゾン水11となる。 In FIG. 3, an ozone gas contact mechanism 10 is provided in the middle of the exhaust ozone gas conduit 8, and after contacting the pure water 3, the exhaust ozone gas 1 </ b> A is processed by the ozone gas processing unit 9. The pure water 3 becomes supply ozone water 11 by the ozone gas contact mechanism 10.
また、排オゾンガス1Aの導管8にはオゾンガス濃度を測定するオゾンガス濃度測定手段12が取り付けられ、オゾンガス濃度の測定情報を制御手段20に送る。制御手段20では、測定したオゾンガス濃度に基づき演算をしてオゾンガス7のオゾンガス量、及び/またはオゾンガス濃度をコントロールする。 An ozone gas concentration measuring means 12 for measuring the ozone gas concentration is attached to the conduit 8 of the exhaust ozone gas 1A, and the measurement information of the ozone gas concentration is sent to the control means 20. The control means 20 calculates based on the measured ozone gas concentration to control the ozone gas amount and / or the ozone gas concentration of the ozone gas 7.
このように、排オゾンガス1Aのオゾンガス濃度に基づき演算をしてオゾン水循環ラインR1に注入されるオゾンガス7のオゾンガス量、及び/またはオゾンガス濃度をコントロールすることで、ガス分離タンク6から吐出される吐出オゾン水2は、常に安定な濃度のオゾン水であり、また排オゾンガス1Aも安定な濃度であり、オゾンガス処理部9における異常発生を防止することができ安全対策にもなる。 Thus, the discharge discharged from the gas separation tank 6 is performed by calculating the ozone gas concentration of the exhaust ozone gas 1A and controlling the ozone gas amount and / or the ozone gas concentration of the ozone gas 7 injected into the ozone water circulation line R1. The ozone water 2 is always ozone water having a stable concentration, and the exhaust ozone gas 1A also has a stable concentration, so that the occurrence of an abnormality in the ozone gas processing unit 9 can be prevented and also serves as a safety measure.
図4において、排オゾンガス1Aの導管8の途中にオゾンガス接触機構10を設け、純水3と接触したのち、排オゾンガス1Aはオゾンガス処理部9にて処理される。また、オゾンガス接触機構10は、図3の実施の形態と同様に構成され、純水3はオゾンガス接触機構10により供給オゾン水11となる。 In FIG. 4, an ozone gas contact mechanism 10 is provided in the middle of the conduit 8 of the exhaust ozone gas 1 </ b> A, and after contacting the pure water 3, the exhaust ozone gas 1 </ b> A is processed by the ozone gas processing unit 9. The ozone gas contact mechanism 10 is configured in the same manner as the embodiment of FIG. 3, and the pure water 3 becomes the supply ozone water 11 by the ozone gas contact mechanism 10.
また、注入ラインR3には、オゾンガス接触機構10により供給オゾン水11になったオゾン水濃度を測定するオゾン水濃度測定手段13が取り付けられ、オゾン水濃度測定の測定情報を制御手段30に送る。制御手段30は、測定したオゾン水濃度に基づき演算をしてオゾン水循環ラインR1に注入されるオゾンガス7のオゾンガス量、及び/またはオゾンガス濃度をコントロールする。 In addition, ozone water concentration measuring means 13 for measuring the concentration of ozone water that has become the supply ozone water 11 by the ozone gas contact mechanism 10 is attached to the injection line R <b> 3, and the measurement information of the ozone water concentration measurement is sent to the control means 30. The control means 30 calculates based on the measured ozone water concentration and controls the ozone gas amount and / or the ozone gas concentration of the ozone gas 7 injected into the ozone water circulation line R1.
このように、供給オゾン水11になったオゾン水濃度に基づき演算をしてオゾン水循環ラインR1に注入されるオゾンガス7のオゾンガス量、及び/またはオゾンガス濃度をコントロールすることで、ガス分離タンク6から吐出される吐出オゾン水2は、常に安定な濃度のオゾン水であり、また排オゾンガス1Aも安定な濃度であり、オゾンガス処理部9における異常発生を防止することができ安全対策にもなる。 In this way, by calculating based on the ozone water concentration that has become the supply ozone water 11 and controlling the ozone gas amount and / or ozone gas concentration of the ozone gas 7 injected into the ozone water circulation line R1, the gas separation tank 6 The discharged ozone water 2 to be discharged is ozone water having a stable concentration at all times, and the exhaust ozone gas 1A has a stable concentration, so that the occurrence of abnormality in the ozone gas processing section 9 can be prevented, which is also a safety measure.
次に、この発明に係わる循環式オゾン水製造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。 Next, although the Example of the circulation type ozone water manufacturing apparatus concerning this invention is described, this Example does not limit this invention.
(比較例1)
10L/minの純水を供給して、オゾン水生成を行った。供給するオゾンガス量は3L/min、オゾンガス濃度を250mg/Lとした。
( Comparative Example 1 )
10 L / min pure water was supplied to generate ozone water. The amount of ozone gas supplied was 3 L / min, and the ozone gas concentration was 250 mg / L.
供給純水と同量のオゾン水量を取り出したところ、オゾン水濃度は33mg/Lであった。 When the same amount of ozone water as the supplied pure water was taken out, the ozone water concentration was 33 mg / L.
(実施例1)
供給される純水にオゾンガス接触機構を設け、排オゾンガスを導いたこと以外は比較例1と同一条件にてオゾン水生成を行った。
( Example 1 )
Ozone water was generated under the same conditions as in Comparative Example 1 except that an ozone gas contact mechanism was provided in the supplied pure water and exhausted ozone gas was introduced.
オゾン水濃度は45ppmで比較例1に比べてオゾン水濃度は1.3倍に上昇した。 The ozone water concentration was 45 ppm, which was 1.3 times higher than that of Comparative Example 1 .
(比較例2)
比較例1と同様の条件でオゾン水生成を行った。オゾン水濃度は同様に33mg/Lであった。
( Comparative Example 2 )
Ozone water was generated under the same conditions as in Comparative Example 1 . The ozone water concentration was also 33 mg / L.
(実施例2)
比較例1と同様の条件で、排オゾンガスの導管にオゾンガス測定機構を取り付け、オゾン水濃度が比較例1と同じになるように供給されるオゾンガス量を調整した。オゾンガス量は2L/minになり、供給するオゾンガス量を2/3にすることができた。
( Example 2 )
Under the same conditions as in Comparative Example 1, an ozone gas measuring mechanism was attached to the exhaust ozone gas conduit, and the amount of ozone gas supplied was adjusted so that the ozone water concentration was the same as in Comparative Example 1 . The amount of ozone gas was 2 L / min, and the amount of ozone gas supplied could be reduced to 2/3.
前記したように、この発明では、常に安定な濃度のオゾン水を得ることができた。また、安全であり、省エネルギーの高濃度のオゾン水が常に生成できる。更には、長期にわたり安定な濃度のオゾン水を発生する装置を得ることが可能となった。 As described above, according to the present invention, ozone water having a stable concentration can always be obtained. Moreover, it is safe and energy-saving high-concentration ozone water can always be generated. Furthermore, it has become possible to obtain an apparatus that generates ozone water having a stable concentration over a long period of time.
この発明は、ポンプを使った循環式オゾン水生成方法及び循環式オゾン水製造装置に適用でき、生成したオゾンガスを有効に利用することができ、オゾン水濃度をより安定にし、また、オゾン水濃度を高濃度にし、しかも安価である。 The present invention can be applied to a circulating ozone water generation method and a circulating ozone water production apparatus using a pump, can effectively use the generated ozone gas, stabilize the ozone water concentration, Is high in concentration and inexpensive.
1 オゾン水
2 吐出オゾン水
3 純水
4 循環ポンプ
5 オゾンガス混合機構
6 ガス分離タンク
7 オゾンガス
8 導管
9 オゾンガス処理部
10 オゾンガス接触機構
11 供給オゾン水
12 オゾンガス濃度測定手段
13 オゾン水濃度測定手段
20,30 制御手段
DESCRIPTION OF SYMBOLS 1 Ozone water 2 Discharged ozone water 3 Pure water 4 Circulation pump 5 Ozone gas mixing mechanism 6 Gas separation tank 7 Ozone gas 8 Conduit 9 Ozone gas processing part 10 Ozone gas contact mechanism 11 Supply ozone water 12 Ozone gas concentration measurement means 13 Ozone water concentration measurement means 20, 30 Control means
Claims (8)
オゾン水を循環するオゾン水循環ラインとは別にオゾンガス接触機構を備え、
オゾン水の生成により排出される排オゾンガスを前記オゾンガス接触機構に供給し、
前記オゾンガス接触機構により供給される純水と前記排オゾンガスを接触させて純水に排オゾンガスを溶解し、
前記オゾンガス接触機構を介して前記排オゾンガスを溶解したオゾン水を前記オゾン水循環ラインに供給することを特徴とする循環式オゾン水生成方法。 In the circulating ozone water generating method of circulating ozone water with a pump, injecting ozone gas and pure water in the middle to dissolve ozone gas and generating ozone water,
Apart from the ozone water circulation line that circulates ozone water, it has an ozone gas contact mechanism,
Supplying exhaust ozone gas discharged by generation of ozone water to the ozone gas contact mechanism;
The dissolving discharge ozone ozone gas contact mechanism wherein contacting the exhaust ozone gas and pure water supplied by it in pure water,
Circulating ozone water generating method characterized that you supplying ozone water obtained by dissolving the exhaust ozone gas through the ozone gas contact mechanism with the ozone water circulation line.
一方に前記純水を、他方に前記排オゾンガスを導入して前記膜を介して前記排オゾンガスが前記純水に溶け込み、前記純水を前記オゾン水にする構造であることを特徴とする請求項1に記載の循環式オゾン水生成方法。 The structure in which the pure water becomes the ozone water through the ozone gas contact mechanism has a film formed of a fluororesin,
Claim Meanwhile wherein the pure water, and introducing the exhaust ozone gas to the other penetration into the exhaust ozone gas the pure water through the membrane, wherein said a structure pure water to the ozone water circulating ozone water generating method according to 1.
オゾン水を循環するオゾン水循環ラインとは別にオゾンガス接触機構を備え、
オゾン水の生成により排出される排オゾンガスを前記オゾンガス接触機構に供給し、
前記オゾンガス接触機構により供給される純水と前記排オゾンガスを接触させ純水に排オゾンガスを溶解し、
前記オゾンガス接触機構を介して前記排オゾンガスを溶解したオゾン水を前記オゾン水循環ラインに供給することを特徴とすることを特徴とする循環式オゾン水製造装置。 In the circulating ozone water production apparatus that has ozone water circulation line that circulates ozone water with a pump, and injects ozone gas and pure water in the middle to dissolve ozone gas and generate ozone water,
Apart from the ozone water circulation line that circulates ozone water, it has an ozone gas contact mechanism ,
Supplying exhaust ozone gas discharged by generation of ozone water to the ozone gas contact mechanism;
Dissolving the waste ozone gas in pure water is contacted with the exhaust ozone gas and pure water supplied by the ozone gas contact mechanism,
A circulating type ozone water production apparatus , wherein ozone water in which the exhaust ozone gas is dissolved is supplied to the ozone water circulation line through the ozone gas contact mechanism.
一方に前記純水を、他方に前記排オゾンガスを導入して前記膜を介して前記排オゾンガスが前記純水に溶け込み、前記純水を前記オゾン水にする構造であることを特徴とする請求項5に記載の循環式オゾン水製造装置。 The structure in which the pure water becomes the ozone water through the ozone gas contact mechanism has a film formed of a fluororesin,
Claim Meanwhile wherein the pure water, and introducing the exhaust ozone gas to the other penetration into the exhaust ozone gas the pure water through the membrane, wherein said a structure pure water to the ozone water 5. The circulating ozone water production apparatus according to 5.
前記測定したオゾン水濃度に基づき演算をして前記オゾン水循環ラインに注入されるオゾンガスのオゾンガス量、及び/またはオゾンガス濃度をコントロールする制御手段と、
を有することを特徴とする請求項5または請求項6に記載の循環式オゾン水製造装置。 Ozone water concentration measuring means for measuring the concentration of ozone water that has become the ozone water by the ozone gas contact mechanism;
Control means for controlling the ozone gas amount and / or ozone gas concentration of the ozone gas injected into the ozone water circulation line by calculating based on the measured ozone water concentration;
The circulating ozone water production apparatus according to claim 5 or 6 , characterized by comprising:
前記測定したオゾンガス濃度に基づき演算をして前記オゾン水循環ラインに注入される 前記オゾンガスのオゾンガス量、及び/またはオゾンガス濃度をコントロールする制御手段と、
を有することを特徴とする請求項5または請求項6に記載の循環式オゾン水製造装置。 Ozone gas concentration measuring means for measuring the ozone gas concentration of the exhaust ozone gas once used;
Control means for controlling the ozone gas amount and / or the ozone gas concentration of the ozone gas to be calculated and injected into the ozone water circulation line based on the measured ozone gas concentration;
The circulating ozone water production apparatus according to claim 5 or 6, characterized by comprising:
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