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JPS6320193B2 - - Google Patents
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JPS6320193B2 - - Google Patents

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Publication number
JPS6320193B2
JPS6320193B2 JP11654783A JP11654783A JPS6320193B2 JP S6320193 B2 JPS6320193 B2 JP S6320193B2 JP 11654783 A JP11654783 A JP 11654783A JP 11654783 A JP11654783 A JP 11654783A JP S6320193 B2 JPS6320193 B2 JP S6320193B2
Authority
JP
Japan
Prior art keywords
ozone
purity water
water
purity
sterilization
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
Application number
JP11654783A
Other languages
Japanese (ja)
Other versions
JPS607990A (en
Inventor
Ryuichi Sazuka
Toshiaki Kuwabara
Tsuyoshi Ishikawa
Kyokatsu Ueda
Ryoichi Tamura
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric 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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP11654783A priority Critical patent/JPS607990A/en
Publication of JPS607990A publication Critical patent/JPS607990A/en
Publication of JPS6320193B2 publication Critical patent/JPS6320193B2/ja
Granted legal-status Critical Current

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  • Treatment Of Water By Oxidation Or Reduction (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔発明の属する技術分野〕 本発明は、薬品工業や食品工業などのように高
度に精製された水あるいは蒸溜水といつた所謂高
純度水を多量に使用する分野の高純度水供給シス
テムを無菌状態に保持する殺菌方法に関する。 〔従来技術とその問題点〕 薬品工業や食品工業で使用される水は、製品の
性格上、高純度水であると同時にそれの供給シス
テムは常に無菌状態に保持されることが要求され
る。そして例えば食品工業では、仕込水、容器洗
滌、調合容器洗滌、各種フイルタ洗滌。薬品工業
では調合用水、調合容器洗滌、充填容器洗滌等い
ろいろの面で使用されることから、当然その供給
システムも多岐に亘つており、最近は水の合理的
運用という観点から集中処理が進められ、ますま
す大型化、複雑化していく傾向にある。 このように複雑かつ大型化していく水供給シス
テムでは、沢山のタンク、バルブ、フイルタ、ポ
ンプおよび使用機器あるいはパツキング部等が存
在し、それだけに空気接触部やパツキング部から
の菌の侵入等といつた汚染の恐れがありまたタン
ク滞留中の菌の成長といつた危険があり、そのた
め高純度水供給システム系を無菌状態に保持する
のに非常に高度な管理と費用とを必要としてい
る。 従つて、高純度供給システムは、その使用目的
あるいはシステム構成部材等によつて異るが通常
1〜7日に1回の割合で殺菌処理する例が多い。 殺菌方法としては、熱処理法、紫外線照射法、
薬注法あるいはオゾン注入法等各種の処理方法が
用いられている。これらのうちオゾン注入法は、 (1) 耐薬品性や耐熱性が強く(250℃30分以上又
は180℃120分以上で破壊される)、処理が難し
いとされるところの医薬品工業で問題視されて
いるパイロジエン(細菌性内毒素)も短時間で
処理できる。 (2) 殺菌処理に伴う廃水を発生しない。 (3) 操作が簡便で、自動化が容易である。 (4) 経済的に優れている。 など、多くの優れた特長を持つているため、各分
野で多く採用されている。添付の第1図はオゾン
注入法を適用した従来例のシステム構成図であ
る。第1図において高純度水製造工程1で作られ
た高純度水は貯留槽4を経由し給水装置8を介し
給水されるようになつている。 本システムにおいて殺菌処理をする場合、バル
ブ20を閉じて閉水路系を形成した後循環ポンプ
12を駆動して系内の高純度水を矢印Aの方向に
還流させるとともにオゾン発生器2で生成したオ
ゾンをオゾン注入器3を介して高純度水に溶け込
ませる。こうして作られた含オゾン高純度水を、
閉水路系を循環させることによつて系内殺菌が行
なわれる。一定時間経過し殺菌の終了を確認した
後オゾン発生器2を停止し、紫外線ランプ5を点
灯して系内の循環水に紫外線を照射することによ
り、高純度水中に溶存するオゾンを分解する、オ
ゾンモニタ6によつてオゾン分解の完了を確認し
た後は高純度水の供給が可能となる。 しかし、このオゾン注入法による殺菌法におい
て高純度水に残留するオゾンの分解を紫外線照射
によつて行つているが、紫外線照射は、 (1) オゾンの分解に長時間を必要とする。 添付の第2図は水に溶存するオゾンの紫外線
照射による分解の状況を、縦軸に溶存オゾン濃
度を、横軸に紫外線照射時間をとつて両者の関
係を調べたものである。その結果によれば約2
ppmの溶存オゾンを0.1ppm以下とするのに約1時
間を要し、化学的に検知できない程度にまで分
解するのに約3時間かかつている。 このように紫外線照射によるオゾンの分解に
長時間を必要とすることは、オゾン注入法によ
る高純度水供給システムを用途によつては適用
を不可能となつたり、あるいは殺菌処理システ
ムと連続的システムとする上での難点となる。 (2) 紫外線ランプの寿命が比較的短かく、維持管
理上手数がかかる。 紫外線ランプの寿命は連続点灯で2000〜7000
時間程度であるが、点滅回数が増すと寿命はさ
らに短くなると言われている。従つてオゾンの
分解に紫外線照射を適用した殺菌方法の場合
は、殺菌処理の都度点滅されるわけで、それだ
けに長寿命を期待することは難しく、保守なら
びに経済上の問題となり易い。 等のことが、オゾンによる高純度水供給システム
設計上の難点としてあげられるのである。 〔発明の目的〕 本発明は、上述した諸問題に着目してなされた
もので、紫外線照射による溶存オゾンの分解とい
う工程のもつ欠点を解決すると同時に経済的にす
ぐれた殺菌方法を提供することを目的とする。 〔発明の要点〕 本発明は、高純度水製造工程からの高純度水を
充填器、洗滌器などの給水装置を介し供給するよ
うに構成された高純度水供給システムにおいて、
前記高純度水製造工程から供給された高純度水に
オゾンを注入して前記高純度水供給システム系内
を殺菌したり、パイロジエンを分解処理し、殺菌
処理後の高純度水中に溶存するオゾンを水中に浸
漬した活性炭層を通過させるようにして、上記目
的を達成しようとするものである。 〔発明の実施例〕 本発明について実施例をもとに説明する。第3
図は本発明を適用した高純度水供給システムの殺
菌方法の概念を示すシステム構成図である。第3
図において第1図と同一部分は同一符号を付して
ある。 符号1は高純度水製造工程を示し、この高純度
水製造工程1のあとに、オゾン発生器2より含オ
ゾン空気の供給がうけられるようになつている例
えばラインミキサーのようなオゾン注入器3と、
オゾン注入器3を介して供給される含オゾン高純
度水(以下含オゾン水という)の貯溜槽4と、含
オゾン水のオゾン濃度を検知するためのオゾンモ
ニタ6と、前記貯溜槽4とオゾンモニタ6との間
の経路の途中から分岐し含オゾン水を通過させる
活性炭槽30およびフイルタ31と、充填器ある
いは洗滌器からなる給水装置8及び循環ポンプ1
2を順次パイプによつて連接し水路系を形成、こ
の循環ポンプ12より送り出された水が、前記高
純度製造装置1からオゾン注入器2へ高純度水を
供給するための配管の途中にて合流(合流点2
1)するようにして1つの閉水路を構成してな
る。そして貯溜槽4の下流で、分岐し一方はバル
ブ16を介装してオゾンモニタ6に連接。他方は
分岐点よりやや下流にバルブ15を介装活性炭槽
30へ連接、フイルタ31を経由しバルブ17を
介し終端がオゾンモニタ6の上流部の配管に合流
するように構成されている。またこの閉水路系の
中で給水装置8と循環ポンプ12との間、循環ポ
ンプ12と合流点21との間及び高純度水製造工
程1と合流点21との間に、それぞれバルブ1
8,19,20が介装されている。 なお貯溜槽4には、注入された含オゾン空気の
未溶解分を逃がし、かつ余剰オゾンを無害化する
ための排オゾン処理器10を介装した排出管12
と、貯溜槽4内の空間部が負圧とならぬようにす
るための除菌フイルタ11を介装した給気管13
が設けられている。またオゾン発生装置2は、オ
ゾンモニタ6の測定値をもとに制御されるよう
(図示せず)に構成されている。 以上のように構成される高純度水供給システム
の殺菌方法は次のように稼動する。バルブ20、
および15,17を閉、バルブ18および19を
開とし、オゾン発生装置2と循環ポンプ12を稼
動させ閉水路系内の高純度水を循環させつつオゾ
ン注入器3で該循環水中に含オゾン空気を散気さ
せオゾンを溶解させ含オゾン水で閉水路系内を満
す。そして一定時間含オゾン水を閉水路経由で循
環させることで系内各部を殺菌する。なお殺菌処
理中はオゾンモニタ6によつて水中のオゾン濃度
が殺菌に必要な濃度に常に保たれるよう制御す
る。 所定時間経過し、殺菌の終了を確認したらオゾ
ン発生装置2を停止し、次にバルブ16を絞り、
バルブ15および17を開とし、系中の含オゾン
水が活性炭槽30およびフイルタ31を通過させ
るようにする。こうして系内の高純度水を循環さ
せた後オゾンモニタ6によつて溶存オゾンの分解
の程度を検知し安全が確認された後、バルブ1
8,19および15,17を閉じバルブ16およ
び20を開として、高純度水の供給を始めるので
ある。 オゾンが活性炭によつて分解されることは公知
であり、反応温度が高いと活性炭の消耗と同時に
炭酸ガスが生成すること、反応温度が低いと接触
分解のために酸素のみが生成し活性炭の消耗がな
いことなども公知の事実である。しかしながらこ
れらの事実はいずれも気相における反応であつ
て、水中で同様にオゾンを分解するかどうかは明
らかにされていない。 本願発明者は、第4図に示すような装置を用
い、水中に浸漬した活性炭が溶存オゾンの分解に
有効がどうかの実験をし本願の着想を得たのであ
る。すなわち1つの閉水路中にオゾン注入器3
(オゾン発生装置2より含オゾン空気の供給を受
けられるように構成)と活性炭槽30および循環
ポンプ12を介装させ、活性炭槽30の上流側、
下流側に溶存オゾン濃度測定のための試料採取点
を設けた構成の実験装置によつて、種々の溶存の
含オゾン水の実験を試み、次表に示すような結果
を得たのである。
[Technical field to which the invention pertains] The present invention provides a sterile system for supplying high-purity water in fields such as the pharmaceutical industry and food industry, which use a large amount of so-called high-purity water such as highly purified water or distilled water. This invention relates to a sterilization method that maintains the condition. [Prior art and its problems] Due to the nature of the products, the water used in the pharmaceutical and food industries is required to be highly purified, and at the same time, its supply system must be maintained in a sterile state at all times. For example, in the food industry, it is used for preparing water, cleaning containers, cleaning mixing containers, and cleaning various filters. In the pharmaceutical industry, water is used for various purposes such as mixing water, washing mixing containers, and cleaning filling containers, so naturally the supply systems are diverse, and recently, intensive treatment has been promoted from the perspective of rational water management. , and are becoming increasingly larger and more complex. In water supply systems that are becoming more complex and larger, there are many tanks, valves, filters, pumps, and other equipment or packing parts, which makes it difficult for bacteria to enter from air contact parts or packing parts. There is a risk of contamination and the growth of bacteria during retention in the tank, so maintaining the high purity water supply system in a sterile state requires very sophisticated management and expense. Therefore, high-purity supply systems are often sterilized once every 1 to 7 days, depending on the purpose of use or the system components. Sterilization methods include heat treatment, ultraviolet irradiation,
Various treatment methods such as chemical injection method or ozone injection method are used. Of these, the ozone injection method is viewed as a problem in the pharmaceutical industry, where (1) it has strong chemical and heat resistance (destructed in 30 minutes or more at 250°C or 120 minutes or more at 180°C) and is difficult to process; The pyrogens (bacterial endotoxins) that are used can also be treated in a short time. (2) No wastewater is generated during sterilization. (3) It is simple to operate and easy to automate. (4) Economically superior. Because it has many excellent features such as, it is widely used in various fields. The attached FIG. 1 is a diagram showing the configuration of a conventional system to which the ozone injection method is applied. In FIG. 1, high-purity water produced in a high-purity water production process 1 is supplied via a storage tank 4 and a water supply device 8. When performing sterilization treatment in this system, after closing the valve 20 to form a closed channel system, the circulation pump 12 is driven to circulate high-purity water in the system in the direction of arrow A, and the ozone generator 2 generates high-purity water. Ozone is dissolved into high purity water via an ozone injector 3. The ozone-containing high purity water produced in this way is
Sterilization within the system is carried out by circulating the closed water system. After a certain period of time has elapsed and the completion of sterilization is confirmed, the ozone generator 2 is stopped, and the ultraviolet lamp 5 is turned on to irradiate the circulating water in the system with ultraviolet rays, thereby decomposing the ozone dissolved in the high purity water. After the completion of ozone decomposition is confirmed by the ozone monitor 6, supply of high-purity water becomes possible. However, in this ozone injection sterilization method, ozone remaining in high-purity water is decomposed by ultraviolet irradiation, but ultraviolet irradiation (1) requires a long time to decompose ozone. The attached Figure 2 shows the state of decomposition of ozone dissolved in water by ultraviolet irradiation, with the vertical axis representing the dissolved ozone concentration and the horizontal axis representing the ultraviolet irradiation time, and examining the relationship between the two. According to the results, about 2
It takes about one hour to reduce the dissolved ozone level to below 0.1 ppm, and about three hours to decompose it to a level where it cannot be chemically detected. The long time it takes for ozone to decompose due to ultraviolet irradiation makes it impossible to apply high-purity water supply systems using ozone injection methods, or sterilization systems and continuous systems. This is a difficult point in doing so. (2) Ultraviolet lamps have a relatively short lifespan and require a lot of maintenance work. The lifespan of an ultraviolet lamp is 2000 to 7000 when continuously lit.
It is said that the lifespan will be even shorter as the number of flashes increases. Therefore, in the case of a sterilization method in which ultraviolet irradiation is applied to decompose ozone, the light flashes on and off each time the sterilization process is performed, and it is therefore difficult to expect a long service life, which tends to cause maintenance and economic problems. These are some of the difficulties in designing a high-purity water supply system using ozone. [Object of the Invention] The present invention has been made in view of the above-mentioned problems, and aims to provide an economically superior sterilization method that solves the drawbacks of the process of decomposing dissolved ozone by ultraviolet irradiation. purpose. [Summary of the Invention] The present invention provides a high-purity water supply system configured to supply high-purity water from a high-purity water production process through a water supply device such as a filler or a washer.
Ozone is injected into the high-purity water supplied from the high-purity water production process to sterilize the high-purity water supply system, or pyrogen is decomposed and ozone dissolved in the high-purity water after sterilization is removed. The purpose is to achieve the above object by passing through an activated carbon layer immersed in water. [Examples of the Invention] The present invention will be described based on Examples. Third
The figure is a system configuration diagram showing the concept of a sterilization method for a high-purity water supply system to which the present invention is applied. Third
In the figure, the same parts as in FIG. 1 are given the same reference numerals. Reference numeral 1 indicates a high-purity water production process, and after this high-purity water production process 1, an ozone injector 3, such as a line mixer, is configured to receive ozone-containing air from an ozone generator 2. and,
A storage tank 4 for ozone-containing high purity water (hereinafter referred to as ozone-containing water) supplied via an ozone injector 3, an ozone monitor 6 for detecting the ozone concentration of the ozone-containing water, and the storage tank 4 and the ozone An activated carbon tank 30 and a filter 31 that branch off from the middle of the path between the monitor 6 and the ozone-containing water pass therethrough, a water supply device 8 consisting of a filler or a washer, and a circulation pump 1
2 are successively connected by pipes to form a waterway system, and the water sent out from this circulation pump 12 is placed in the middle of the piping for supplying high purity water from the high purity manufacturing device 1 to the ozone injector 2. Confluence (confluence point 2
1) One closed channel is constructed as follows. Then, downstream of the storage tank 4, it is branched and one side is connected to the ozone monitor 6 through a valve 16. On the other hand, a valve 15 is connected to an intervening activated carbon tank 30 slightly downstream of the branch point, and the end is connected to a pipe upstream of the ozone monitor 6 via a filter 31 and a valve 17. Also, in this closed channel system, valves 1 are installed between the water supply device 8 and the circulation pump 12, between the circulation pump 12 and the confluence 21, and between the high purity water production process 1 and the confluence 21.
8, 19, and 20 are interposed. Note that the storage tank 4 has a discharge pipe 12 equipped with a discharge ozonator 10 for releasing undissolved parts of the injected ozone-containing air and rendering surplus ozone harmless.
and an air supply pipe 13 interposed with a sterilization filter 11 to prevent the space inside the storage tank 4 from becoming negative pressure.
is provided. Further, the ozone generator 2 is configured to be controlled based on the measured value of the ozone monitor 6 (not shown). The sterilization method for the high-purity water supply system configured as described above operates as follows. valve 20,
15 and 17 are closed, valves 18 and 19 are opened, and the ozone generator 2 and circulation pump 12 are operated to circulate high-purity water in the closed channel system, and the ozone injector 3 is used to inject ozone-containing air into the circulating water. The system is filled with ozone-containing water by dissolving ozone and filling the closed channel system with ozone-containing water. The ozone-containing water is then circulated through a closed channel for a certain period of time to sterilize each part of the system. During the sterilization process, the ozone monitor 6 controls the ozone concentration in the water so that it is always maintained at the concentration necessary for sterilization. After a predetermined period of time has elapsed and the completion of sterilization is confirmed, the ozone generator 2 is stopped, and the valve 16 is then throttled.
Valves 15 and 17 are opened to allow ozone-containing water in the system to pass through activated carbon tank 30 and filter 31. After circulating high-purity water in the system, the degree of decomposition of dissolved ozone is detected by the ozone monitor 6 and safety is confirmed, and then the valve 1
8, 19 and 15, 17 are closed, valves 16 and 20 are opened, and the supply of high-purity water is started. It is well known that ozone is decomposed by activated carbon, and if the reaction temperature is high, carbon dioxide gas is produced at the same time as the activated carbon is consumed, and if the reaction temperature is low, only oxygen is produced due to catalytic decomposition, and the activated carbon is consumed. It is also a well-known fact that there is no such thing. However, all of these facts are reactions in the gas phase, and it is not clear whether ozone is similarly decomposed in water. The inventor of the present invention obtained the idea of the present invention by conducting an experiment to determine whether activated carbon immersed in water is effective in decomposing dissolved ozone using an apparatus as shown in FIG. 4. That is, ozone injector 3 is installed in one closed channel.
(configured so that ozone-containing air can be supplied from the ozone generator 2), an activated carbon tank 30, and a circulation pump 12 are interposed, and the upstream side of the activated carbon tank 30,
Using an experimental device configured with a sampling point for measuring dissolved ozone concentration on the downstream side, experiments were conducted on various types of dissolved ozone-containing water, and the results shown in the following table were obtained.

〔発明の効果〕〔Effect of the invention〕

以上説明したように本発明は、高純度水供給シ
ステムの殺菌方法として、高純度水に注入され溶
存しているオゾンを水中に浸漬してある活性炭層
を通過させて分解させるようにしたことにより (1) オゾンの分解時間が短時間で済むことから、
殺菌処理時間を大巾に短縮することができる。 (2) 低温での処理であるため、活性炭の消耗が少
なくて済み、維持管理がし易い。 (3) オゾン分解のための電気、水などを特に必要
としない。 等の効果がある。従つて高純度水供給システムの
殺菌方法として、省資源型で低操業コストの達成
が期待され、極めて経済性の高いシステムの設計
が可能となるのである。
As explained above, the present invention is a method for sterilizing a high-purity water supply system, in which dissolved ozone injected into high-purity water is decomposed by passing through an activated carbon layer immersed in the water. (1) Because ozone decomposition time is short,
Sterilization time can be significantly shortened. (2) Because the process is carried out at low temperatures, there is less consumption of activated carbon, and maintenance is easy. (3) There is no particular need for electricity, water, etc. for ozone decomposition. There are other effects. Therefore, as a sterilization method for a high-purity water supply system, it is expected to save resources and achieve low operating costs, making it possible to design an extremely economical system.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はオゾン注入法を適用した高純度水供給
システムの従来例のシステム構成図、第2図は溶
存オゾン濃度と紫外線照射時間との相関を示すグ
ラフ、第3図は本発明を適用した高純度水供給シ
ステムのシステム構成図、第4図は実験装置のシ
ステム構成図、第5図は本発明の他の適用例のシ
ステム構成図である。 1:高純度水製造工程、3:オゾン注入器、
4:貯溜槽、5:紫外線照射器、6:オゾンモニ
タ、8:給水装置、12:循環ポンプ、15,1
6,17,18,19,20:バルブ、30:活
性炭槽、31:フイルタ、32,33:オゾンモ
ニタ。
Figure 1 is a system configuration diagram of a conventional high-purity water supply system using the ozone injection method, Figure 2 is a graph showing the correlation between dissolved ozone concentration and ultraviolet irradiation time, and Figure 3 is a diagram showing the correlation between dissolved ozone concentration and ultraviolet irradiation time. FIG. 4 is a system configuration diagram of a high-purity water supply system, FIG. 4 is a system configuration diagram of an experimental device, and FIG. 5 is a system configuration diagram of another application example of the present invention. 1: High purity water production process, 3: Ozone injector,
4: Storage tank, 5: Ultraviolet irradiator, 6: Ozone monitor, 8: Water supply device, 12: Circulation pump, 15,1
6, 17, 18, 19, 20: valve, 30: activated carbon tank, 31: filter, 32, 33: ozone monitor.

Claims (1)

【特許請求の範囲】[Claims] 1 高純度水製造工程からの高純度水を充填器、
洗滌器などの給水装置を介し供給するように構成
された高純度水供給システムにおいて、前記高純
度水製造工程から供給された高純度水にオゾンを
注入して前記高純度水供給システム系内を殺菌
し、殺菌処理後の高純度水中に溶存するオゾンを
水中に浸漬した活性炭層を通過させて分解するよ
うにしたことを特徴とする高純度水供給システム
の殺菌方法。
1 Filler with high-purity water from the high-purity water production process,
In a high-purity water supply system configured to be supplied via a water supply device such as a washer, ozone is injected into the high-purity water supplied from the high-purity water production process to cause the inside of the high-purity water supply system to flow. A method for sterilizing a high-purity water supply system, characterized in that ozone dissolved in the high-purity water after sterilization is decomposed by passing through an activated carbon layer immersed in the water.
JP11654783A 1983-06-28 1983-06-28 Sterilization method of feeding system of high-purity water Granted JPS607990A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11654783A JPS607990A (en) 1983-06-28 1983-06-28 Sterilization method of feeding system of high-purity water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11654783A JPS607990A (en) 1983-06-28 1983-06-28 Sterilization method of feeding system of high-purity water

Publications (2)

Publication Number Publication Date
JPS607990A JPS607990A (en) 1985-01-16
JPS6320193B2 true JPS6320193B2 (en) 1988-04-26

Family

ID=14689813

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11654783A Granted JPS607990A (en) 1983-06-28 1983-06-28 Sterilization method of feeding system of high-purity water

Country Status (1)

Country Link
JP (1) JPS607990A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63171694A (en) * 1986-12-29 1988-07-15 Katsumi Takao Ozonized water feeder

Also Published As

Publication number Publication date
JPS607990A (en) 1985-01-16

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