JP2010036169A - Method and apparatus for producing strongly alkaline water and strongly oxidized water by using alternating electric current - Google Patents

Method and apparatus for producing strongly alkaline water and strongly oxidized water by using alternating electric current Download PDF

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JP2010036169A
JP2010036169A JP2008205422A JP2008205422A JP2010036169A JP 2010036169 A JP2010036169 A JP 2010036169A JP 2008205422 A JP2008205422 A JP 2008205422A JP 2008205422 A JP2008205422 A JP 2008205422A JP 2010036169 A JP2010036169 A JP 2010036169A
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JP5001236B2 (en
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Hideo Hayakawa
英雄 早川
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KANKYO KANGEN KENKYUSHO KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an apparatus for producing strongly oxidized water and strongly alkaline water. <P>SOLUTION: The apparatus for producing strongly alkaline water and strongly oxidized water by using an alternating electric current is characterized in that a ground electrode and a pair of application electrodes are arranged in a treatment vessel where the water, which is to be treated and is additive-free fresh water, is housed, a ground electrode-arranged area is isolated by a semipermeable member from an area where both the application electrodes are arranged, and a bipolar electrode is arranged at the ground electrode and in the isolated middle for increasing the electric conductivity between both the application electrodes. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、無添加水(井戸水、水道水)と、酸と食塩、岩塩、塩化カリウム及びミネラル塩から選択された塩類の添加された真水又は酸の添加された海水である被処理水に高周波交流電圧を印加することにより強酸化水及び強アルカリ水を製造する方法及びその装置に係る。   The present invention provides high frequency to additive-free water (well water, tap water) and to-be-treated water which is fresh water to which a salt selected from acid and salt, rock salt, potassium chloride and mineral salt is added or seawater to which acid is added. The present invention relates to a method and apparatus for producing strong oxidizing water and strong alkaline water by applying an alternating voltage.

無添加の真水又は酸及びナトリウム含有塩類を添加した真水 (井戸水、水道水等) 又は酸を添加した海水である被処理水に高周波交流電圧を印加して処理すれば、通電後約 10時間で被処理水のpHは13.5を越えアルカリ水が生成する。例えば、塩化カリウムを含有する水を処理すれば、電解により水中に次亜塩素酸 (HClO)が生成し、その濃度は塩化カリウムに依存するが、pH が 2.5 - 3 の条件下において且つ ORP(酸化還元電位)値が 800mV に達すると次亜塩素酸が 5ppm 以上となり、前記ORPが 1000mv以上になると次亜塩素酸が20ppm 以上となるとされており、このような強酸化水は殺菌作用や殺虫作用を呈することが従来から知られている。強アルカリ液はpH12が洗浄用水や機械加工用水として長期にアルカリ性を保持する特徴を利用している。
特開2000−84560号公報
If treated by applying high-frequency AC voltage to untreated fresh water or fresh water (well water, tap water, etc.) to which acid and sodium-containing salts are added, or seawater to which acid has been added, about 10 hours after energization The pH of the water to be treated exceeds 13.5 and alkaline water is generated. For example, when water containing potassium chloride is treated, hypochlorous acid (HC1O) is produced in the water by electrolysis, the concentration of which depends on potassium chloride, but under conditions of pH 2.5-3 and ORP ( It is said that hypochlorite will be 5 ppm or more when the oxidation-reduction potential value reaches 800 mV, and hypochlorite will be 20 ppm or more when the ORP is 1000 mV or more. It is conventionally known to exhibit an action. The strong alkaline solution utilizes the characteristic that pH 12 retains alkalinity for a long period of time as cleaning water or machining water.
JP 2000-84560 A

しかしながら、このようにして調製された強酸化水は、通電を停止すると ORP値が比較的急激に低下してしまい、通電停止から 1 時間程度で 800mV 以下になり、殺菌・殺虫作用が著しく低下し、又、3時間程度で水道水のORP値である500mv 以下になってしまい、更に放置するとORP値はマイナス値に転じ塩素も気散してしまう。従って、既述のようにして調製された強酸化水は殺菌や殺虫目的の場合に調製してから使用までの時間が著しく制限を受ける点に課題がある。尚、ORP値が+350mv程度まで低下した強酸化水であった段階で殺菌され且つ塩素を含有していないために、食品工場等における加工用水としては好適である。アルカリ水は直流分解にて製作可能であるが、アルカリのpHが1ヶ月で低下する。   However, the strong oxidized water prepared in this way has a relatively rapid decrease in the ORP value when energization is stopped, and it becomes 800 mV or less in about 1 hour after the energization is stopped. In addition, it becomes less than 500mv, which is the ORP value of tap water in about 3 hours, and if left untreated, the ORP value will turn negative and chlorine will be diffused. Therefore, the strong oxidation water prepared as described above has a problem in that the time from preparation to use for sterilization and insecticidal purposes is significantly limited. In addition, since it is sterilized at the stage where the ORP value is reduced to about +350 mV and does not contain chlorine, it is suitable as processing water in food factories and the like. Alkaline water can be produced by direct current decomposition, but the pH of the alkali decreases in one month.

従って、本発明の基本的な目的は殺菌や殺虫目的における可使時間が比較的長い強酸化水の調製法と強アルカリ還元水及びその装置を提供することにある。本発明の付随的な目的は、殺菌・殺虫効果において優れた強酸化水を調製すると同時に ORP 値の極めて低い強アルカリ水を調製することにある。但し、本発明に より調製される強還元水は強アルカリ性を呈しているので食品工場等における加工用水としてではなく、油汚れの洗浄や配管等におけるスケールの除去目的に利用される。   Accordingly, the basic object of the present invention is to provide a method for preparing strongly oxidized water, strongly alkaline reduced water, and an apparatus thereof for relatively long pot life for sterilization and insecticidal purposes. An additional object of the present invention is to prepare strongly alkaline water having an extremely low ORP value while simultaneously preparing strongly oxidized water excellent in bactericidal and insecticidal effects. However, the strongly reduced water prepared according to the present invention exhibits strong alkalinity, so it is used not for processing water in food factories or the like but for the purpose of cleaning oil stains or removing scales in piping.

本発明によれば、上記の目的は、基本的には強酸と強アルカリであり、使用目的により塩,酸化物を入れない方法と、塩化物を入れて酸側に次亜塩素を発生したり、アルカリ側と酸側共にバイポーラ電極の金属イオンを出して、長期にpHを保持する緩衝液として働き、アルカリ洗浄液、塩化物を入れないアルカリ還元水の使い方は、例えば、機械加工の切削液や研削液として、
油性及びクーラント溶液よりも冷却効果が高く、ワーク材の膨張を防ぎ、刃物のダメージが少ない、
摺動効果・潤滑効果は油性及びクーラント溶液にほぼ匹敵する、
菌・バクテリアに依る腐敗臭が無くなり、作業環境が改善される、
切削液・研削液・洗浄液の長寿命化となる、
戻ってきた潤滑油を油水分離と切粉を分離して、アルカリ水生成時にできた酸性水で中和すれば、廃液処理が無くなり環境に優しくコスト軽減のメリットがある、
機械加工の後の脱脂工程がある場合にその必要が無い、
等の作用がある。
本発明では、処理容器内に一対の印加電極を配置し、これらの両印加電極に対して半透過部材を隔て、内側に接地電極を配置し、上記の一対の印加電極に高周波電圧を印加して、印加電極を筒状の半透過部材の外側に、強酸化水が生成されると共に、半透過部材の内側で接地電極が収容されている外側に強アルカリ水が生成されることを特徴とするが、筒状の半透過部材の底に、バイポーラ電極を接地し、外側(A,B電極)と内側の電位差によりバイポーラ電極(例えば、亜鉛の場合)に、
2HO+2e→H+2OH …… (1)
Zn→ Zn2++2e …… (2)
の反応が起こり、pHが上昇し、安定になる。
本発明を実施する場合には、半透過部材の外側(A,B電極)に酸化水を、半透過部材の内側にアルカリ還元水が生成される半透過部材も水の透過が起こることにより、アルカリ側の溶存酸素(DO)が減る。
According to the present invention, the above object is basically a strong acid and a strong alkali. Depending on the purpose of use, a method in which no salt or oxide is added, and a chloride is added to generate hypochlorite on the acid side. The metal ions of the bipolar electrode are released on both the alkali side and the acid side, and serve as a buffer solution that maintains the pH over a long period of time. As grinding fluid
Cooling effect is higher than oiliness and coolant solution, prevents expansion of work material, and damage to the blade is small.
The sliding and lubricating effects are almost comparable to oil and coolant solutions.
There is no rot odor due to bacteria and bacteria, and the working environment is improved.
The service life of cutting fluid, grinding fluid and cleaning fluid will be extended.
If the returned lubricant is separated into oil-water separation and chips, and neutralized with acidic water generated during alkaline water generation, there is no waste liquid treatment and there is a merit of cost reduction that is friendly to the environment.
This is not necessary when there is a degreasing process after machining,
There is an action such as.
In the present invention, a pair of application electrodes are arranged in the processing container, a semi-transmissive member is separated from both the application electrodes, a ground electrode is arranged inside, and a high frequency voltage is applied to the pair of application electrodes. In addition, strong oxidizing water is generated on the outer side of the cylindrical translucent member with the application electrode, and strong alkaline water is generated on the outer side in which the ground electrode is accommodated inside the semipermeable member. However, the bipolar electrode is grounded at the bottom of the cylindrical translucent member, and the bipolar electrode (for example, in the case of zinc) due to the potential difference between the outside (A and B electrodes) and the inside,
2H 2 O + 2e → H 2 + 2OH (1)
Zn → Zn 2+ + 2e (2)
This occurs, and the pH rises and becomes stable.
In the case of carrying out the present invention, the semi-permeable member in which the oxidized water is generated on the outer side (A, B electrodes) of the semi-permeable member and the alkali reduced water is generated on the inner side of the semi-permeable member, The dissolved oxygen (DO) on the alkali side is reduced.

本発明の交流による強アルカリ水及び強酸化水の製造装置の要旨は、無添加の真水である被処理水が収容されている処理容器に接地電極と一対の印加電極を配置し、且つ、前記接地電極が配置されている領域と前記両印加電極が配置されている領域とを半透過性部材により離隔し、更に接地電極と、両印加電極間の導電性を増すために離隔された中間とにバイポーラ電極を配置したことである。
また、前記バイポーラ電極は、溶解性の高い亜鉛、アルミニウム、金、鉄、コバルト、ニッケル、マグネシウム、錫の内のいずれか一つの金属であることであり、
更に、前記半透過性部材が半透膜、逆浸透膜又は素焼きの陶器、布フィルタであることを含むものである。
The gist of the apparatus for producing strong alkaline water and strong oxidized water by alternating current according to the present invention is that a ground electrode and a pair of applied electrodes are arranged in a treatment container in which treated water that is additive-free fresh water is accommodated, and A region where the ground electrode is disposed and a region where the two applied electrodes are disposed are separated by a semi-transmissive member, and further, a ground electrode and a middle portion separated to increase conductivity between the two applied electrodes, The bipolar electrode is arranged in
The bipolar electrode is a highly soluble zinc, aluminum, gold, iron, cobalt, nickel, magnesium, or any one metal of tin,
Furthermore, the semipermeable member includes a semipermeable membrane, a reverse osmosis membrane, an unglazed ceramic, or a cloth filter.

本発明に係る交流による強アルカリ水及び強酸化水の製造方法の要旨は、無添加の真水である被処理水が収容されている処理容器に接地電極と一対の印加電極を配置し、且つ、前記接地電極が配置されている領域と前記両印加電極が配置されている領域とを半透過性部により離隔し、更に接地電極と、両印加電極間の導電性を増すために離隔された中間とにバイポーラ電極を配置して交流による強アルカリ水及び強酸化水の製造装置を形成し、前記両印加電極に交流電圧を印加して当該両印加電圧が配置されている領域に強酸化水を生成させると共に、前記接地電極が接地されている領域に強アルカリ性水を生成させることである。   The gist of the method for producing strong alkaline water and strong oxidized water by alternating current according to the present invention is that a ground electrode and a pair of applied electrodes are arranged in a processing container in which treated water that is additive-free fresh water is housed, and The region in which the ground electrode is disposed and the region in which the two application electrodes are disposed are separated by a semi-transmissive portion, and further, the ground electrode and the intermediate region separated to increase conductivity between the two application electrodes. A bipolar electrode is arranged to form an apparatus for producing strong alkaline water and strong oxidized water by alternating current, and an alternating voltage is applied to both the applied electrodes, and strong oxidized water is applied to a region where both applied voltages are disposed. And generating strongly alkaline water in a region where the ground electrode is grounded.

また、前記真水に上記記載の被処理水および酸,食塩,塩化カリウムを添加して被処理水とし、両印加電極に高周波交流電圧を印可して、当該両印加電圧が配置されている領域に強酸化水を生成させると共に、前記接地電極が接地されている領域に強アルカリ性水を生成させることである。   Further, the water to be treated and the acid, salt, and potassium chloride described above are added to the fresh water to form water to be treated, and a high frequency AC voltage is applied to both applied electrodes, and the areas where both applied voltages are arranged In addition to generating strong oxidized water, strong alkaline water is generated in a region where the ground electrode is grounded.

更に、高周波周波数を制御するFM信号発生器を内蔵しその信号に対応して発振周波数を制御し、なだらかな周波数変動中に急激な上昇又は下降に変化する周波数部分を作成することにより半透過部材内部の水を上昇させ、処理容器内における半透過部材内部の被処理水を排出・取り出すことである。
これは、上記水処理装置において、図2に示すように、直流電源からの出力は、変動信号発生器からの出力制御信号が制御回路から高周波発信器に与えられて発振周波数が制御されて変化させられるとともに、高周波切換指令回路が高周波発信器からの切換指令を第1,第2高周波スイッチに与え、これら第1,第2高周波スイッチがオン、オフされて交流が形成されるとともに変化する周波数の中に急激な下降から急激な上昇へ転ずる部分が作成され、一対の印加電極間にかかる交流電圧が印加されることにより、半透過部材の内側、接地電極側の水位が上昇し、半透過部材の外側の水位より内側の水位は10時間で7cm程度以上上昇することにより、内側から容器外に排水することができる。
この現象は、FM変調波の急速な変動による電流干渉作用があり、周波数変調巾、変動周波数により変わり、電極のプラス側よりマイナス側に流れ込み作用があり、半透過部材の内側と外側との極性を反対にすると、内側の水位が減る。
Further, an FM signal generator for controlling a high frequency is built in, and the oscillation frequency is controlled in accordance with the signal, and a frequency portion that changes suddenly up or down during a gentle frequency fluctuation is created, thereby producing a translucent member. The internal water is raised, and the water to be treated inside the semipermeable member in the treatment container is discharged and taken out.
In the above water treatment apparatus, as shown in FIG. 2, the output from the DC power supply changes when the output control signal from the fluctuation signal generator is supplied from the control circuit to the high frequency oscillator and the oscillation frequency is controlled. The high-frequency switching command circuit gives a switching command from the high-frequency transmitter to the first and second high-frequency switches, and the first and second high-frequency switches are turned on and off to form alternating current and change the frequency. A part that suddenly falls from a sudden rise to a sudden rise is created, and an AC voltage applied between a pair of applied electrodes is applied, so that the water level on the inner side of the semi-transmissive member, the ground electrode side rises, and the semi-transmissive The water level on the inner side of the water level outside the member rises by about 7 cm or more in 10 hours, so that the water can be drained from the inner side to the outside of the container.
This phenomenon has a current interference effect due to a rapid fluctuation of the FM modulated wave, changes depending on the frequency modulation width and the fluctuation frequency, and flows into the negative side from the positive side of the electrode, and the polarity between the inner side and the outer side of the semi-transmissive member If you reverse the, the water level on the inside decreases.

本発明の方法を実施する場合に、酸は酸化水の生成を促進するために添加されるものであり、その種類に格別の制限はなくクエン酸、酢酸、酒石酸、蟻酸等の有機酸や硫酸、硝酸等の無機酸を使用することが可能であるが、本発明は農作物栽培用の殺菌・殺虫用水としての使用を主として企図しており、従って農作物に害を与えないこと並びに価格面等を考慮に入れると塩化カリウムが好ましく、その添加量は被処理水に対して0.1−1重量% 程度である。   When the method of the present invention is carried out, the acid is added to promote the generation of oxidized water, and there is no particular limitation on the type thereof, and organic acids such as citric acid, acetic acid, tartaric acid, formic acid, sulfuric acid It is possible to use inorganic acids such as nitric acid, but the present invention is mainly intended for use as sterilizing / insecticidal water for crop cultivation, and therefore does not cause harm to crops and is price-sensitive. Taking into account, potassium chloride is preferable, and the amount added is about 0.1 to 1% by weight based on the water to be treated.

塩類としては食塩であっても差し支えがないが、農作物への施用を考慮に入れるとミネラル分に富んだ岩塩や、所謂「ミネラル塩」と称されているもの、例えば沖縄県において「青塩」と称されているものが好ましい。   Although salt may be used as the salt, rock salt rich in minerals and so-called “mineral salt” when applied to agricultural products, for example, “blue salt” in Okinawa Prefecture What is called is preferable.

印加電極は耐酸性を有している素材として、チタン,白金,銀,亜鉛,アルミニウム,銅,カーボン,ニッケル,錫,鉄,コバルト等であれば差し支えがないが白金鍍金チタン板が好ましく、殊に電極面積を大にするために梨地加工を施したチタン板に白金を鍍金したものが好ましい。   The applied electrode may be any material having acid resistance, such as titanium, platinum, silver, zinc, aluminum, copper, carbon, nickel, tin, iron, cobalt, etc., but a platinum-plated titanium plate is preferred. In addition, a titanium plate that has been subjected to a satin finish to increase the electrode area is preferably plated with platinum.

接地電極は耐アルカリ性を有している素材のものであれば差し支えがないが、チタン板又はステンレス・スチール板が好ましい。   The ground electrode may be any material having alkali resistance, but a titanium plate or a stainless steel plate is preferable.

半透過性部材としては半透過膜、逆浸透膜、素焼きの陶器等を例示することができる。   Examples of the semipermeable member include a semipermeable membrane, a reverse osmosis membrane, and an unglazed earthenware.

本発明による強酸化水及びアルカリ水の製造装置は、処理容器と、該処理容器内に配置された接地電極及び一対の印加電極と、上記の印加電極が配置されている領域と上記の接地電極が配置されている領域とを隔てる半透過性部材と、直流電源と、該直流電源に可変抵抗を介してそれぞれ接続された第1及び第2の高周波スイッチと、これらの高周波スイッチに抵抗を介して接続されたフリップフロップ回路を有する高周波切換指令回路と、該高周波切換指令回路に接続された高周波発振器と、該高周波発振器に接続された制御回路とを備えており、上記の高周波切換指令回路が切換指令を上記の第 1 及び第 2 高周波スイッチに交互に与え、これら高周波スイッチの高周期オン、オフによる高周波交流電圧を上記の一対の印加電極に印加することを特徴としている。   An apparatus for producing strong oxidizing water and alkaline water according to the present invention includes a processing container, a ground electrode and a pair of application electrodes disposed in the processing container, a region in which the application electrode is disposed, and the ground electrode. A semi-transparent member that separates the region where the two are disposed, a DC power source, first and second high-frequency switches connected to the DC power source via variable resistors, and a resistance to these high-frequency switches. A high-frequency switching command circuit having flip-flop circuits connected to each other, a high-frequency oscillator connected to the high-frequency switching command circuit, and a control circuit connected to the high-frequency oscillator. A switching command is alternately applied to the first and second high-frequency switches, and a high-frequency AC voltage generated by turning on and off the high-frequency switches is applied to the pair of application electrodes. It is characterized by a door.

印加電極と接地電極との間の電気抵抗を低下させるために、バイポーラ電極を設けた。   In order to reduce the electrical resistance between the application electrode and the ground electrode, a bipolar electrode was provided.

本発明による強酸化水及びアルカリ水の製造装置において、電源電圧は 100V であるが、実効値は約半分又はそれ以下であり、電流値も比較的低いので安全性は高く、又高周波発振器から高周波切換指令回路に与えられる信号の周波数は 20 - 50KHz であって、30 - 35KHz が好ましい。   In the apparatus for producing strong oxidizing water and alkaline water according to the present invention, the power supply voltage is 100 V, but the effective value is about half or less, the current value is relatively low, and the safety is high. The frequency of the signal given to the switching command circuit is 20-50 KHz, preferably 30-35 KHz.

本発明によれば、強い殺菌・殺虫作用を有する強酸化水と、油汚れの除去や配管等におけるスケールの除去に利用可能な強還元水とを同時に且つ別個に調製することができる。本発明に使用される装置は酸及び食塩、岩塩及びミネラル塩から選択された塩類とを添加した井戸水、水道水等を被処理水として外槽及び半透過性の内槽内に導入し、外槽内には 1 対の印加電極を且つ内槽内には接地電極を配置し、両印加電極に高周波交流電圧を印加するだけであり、強酸化水及びアルカリ水の製造所要時間も30分−1時間程度であり、比較的短い。   ADVANTAGE OF THE INVENTION According to this invention, the strong oxidation water which has a strong bactericidal and insecticidal action, and the strong reduced water which can be utilized for the removal of oil dirt, the removal of the scale in piping, etc. can be prepared simultaneously and separately. The apparatus used in the present invention introduces well water, tap water, etc. added with acid and salt, salt selected from rock salt and mineral salt into the outer tank and semi-permeable inner tank as treated water, A pair of applied electrodes is placed in the tank, and a ground electrode is placed in the inner tank. A high-frequency AC voltage is simply applied to both applied electrodes, and the time required for producing strong oxidizing water and alkaline water is 30 minutes. It is about 1 hour and is relatively short.

次に、本発明による強酸化水及びアルカリ水の製造装置について添付図面を参照しつつ説明し、又試験例により具体的に説明する。
装置例 1
図 1 は、本発明による強酸化水及びアルカリ水の製造装置の第 1 実施形の概要を示すものである。この装置は被処理水 TW の水処理部31と該被処理水 TWに高周波交流電圧を印加する印加装置30とを備えている。被処理水の水処理部31は外槽21と、該外槽21内に配置された内槽20とを備えており、該内槽20は半透過性部材から構成されており (本例の場合には素焼きの陶器を利用)、その下端の開口部 (底の部分)には、溶解性の高い金属として、例えば、亜鉛板のバイポーラ電極が装着されている。このほか、前記バイポーラ電極は、溶解性の高い亜鉛、アルミニウム、金、コバルト、ニッケル、マグネシウム、の内のいずれか一つの金属とするのが好ましい。
Next, the apparatus for producing strong oxidizing water and alkaline water according to the present invention will be described with reference to the accompanying drawings, and more specifically by test examples.
Example 1
FIG. 1 shows an outline of the first embodiment of the apparatus for producing strong oxidizing water and alkaline water according to the present invention. This apparatus includes a water treatment unit 31 for water to be treated TW and an application device 30 for applying a high-frequency AC voltage to the water to be treated TW. The water treatment section 31 of the water to be treated includes an outer tub 21 and an inner tub 20 disposed in the outer tub 21, and the inner tub 20 is composed of a semi-permeable member (in this example) In some cases, unglazed earthenware is used), and a bipolar electrode made of a zinc plate, for example, is attached to the opening (bottom part) of the lower end as a highly soluble metal. In addition, the bipolar electrode is preferably made of any one of highly soluble zinc, aluminum, gold, cobalt, nickel, and magnesium.

被処理水 TW は酸であり、例えば、クエン酸と、塩類例えばミネラル塩とが添加された真水、又は無添加水道水、井戸水、湧水等であることができ、又塩類を添加した真水を海水に代替することもできる。   The treated water TW is an acid, and can be, for example, fresh water to which citric acid and salts such as mineral salts are added, or non-added tap water, well water, spring water, etc. It can be replaced by seawater.

外槽21内には 2 つの電極2A及び2Bが配置されており、内槽20内には 1 つの電極GE が配置されている。これらの電極の内で、両印加電極2A及び2Bは、チタン,白金,銀,亜鉛,アルミニウム,銅,カーボン,ニッケル,コバルト等を使用する。この一例では、チタン板に白金を鍍金したものであり、一方、電極GEは何等処理されていないチタン板である。内槽20の底部に取り付けられているのはバイポーラ電極の亜鉛19である。電極 2A及び2Bは導線 L1 及び L2により高周波交流電圧印加装置 30 に接続されていて交番的に高周波交流電圧が印加されるようになされており、一方、電極 GE は導線 L3 を介して接地されている。   Two electrodes 2A and 2B are arranged in the outer tank 21, and one electrode GE is arranged in the inner tank 20. Among these electrodes, the application electrodes 2A and 2B use titanium, platinum, silver, zinc, aluminum, copper, carbon, nickel, cobalt, or the like. In this example, platinum is plated on a titanium plate, while the electrode GE is a titanium plate that is not treated at all. Attached to the bottom of the inner tank 20 is a bipolar electrode zinc 19. The electrodes 2A and 2B are connected to the high-frequency AC voltage application device 30 by means of conducting wires L1 and L2, so that a high-frequency AC voltage is applied alternately, while the electrode GE is grounded via the conducting wire L3. Yes.

図1に概略的に示されている高周波交流電圧印加装置30は、電源3と、可変抵抗4を介して接続された第1高周波スイッチ5A及び第 2高周波スイッチ5Bと、高周波発振器11と、フリップフロップ回路 FF から構成されている。上記の高周波発振器により制御される高周波切換指令回路であって、抵抗9Aを介して上記の第1高周波スイッチ5Aに接続され且つ抵抗9Bを介して上記の第2高周波スイッチ5Bに接続されている高周波切換指令回路10と、上記の第1高周波スイッチ5A及び上記の第2高周波スイッチ5Bの出力側において並列に接続されたコンデンサ8とを備えている。上記の高周波スイッチは各々トランジスタ 6A,7A,6B,7Bとを備えている。尚、図 1 に関連して述べたように、導線 L1 及び L2 は印加電極2A及び2Bにそれぞれ接続されており、導線 L3 は接地電極 GE に接続されている。   A high-frequency AC voltage application device 30 schematically shown in FIG. 1 includes a power source 3, a first high-frequency switch 5A and a second high-frequency switch 5B connected via a variable resistor 4, a high-frequency oscillator 11, and a flip-flop. Circuit FF. A high frequency switching command circuit controlled by the high frequency oscillator, which is connected to the first high frequency switch 5A through a resistor 9A and connected to the second high frequency switch 5B through a resistor 9B. A switching command circuit 10 and a capacitor 8 connected in parallel on the output side of the first high frequency switch 5A and the second high frequency switch 5B are provided. Each of the high frequency switches includes transistors 6A, 7A, 6B, and 7B. As described with reference to FIG. 1, the conducting wires L1 and L2 are connected to the application electrodes 2A and 2B, respectively, and the conducting wire L3 is connected to the ground electrode GE.

上記の電源3の電圧は 100V であるが、高周波交流電圧印加装置30としての実効電圧は 50V 又はそれ以下であり、電流値は0.1−0.6A程度であって、又高周波発振器11から高周波切換指令回路に与えられる信号の周波数は20−50KHz、例えば35KHzである。   The voltage of the power source 3 is 100V, but the effective voltage as the high frequency AC voltage applying device 30 is 50V or less, the current value is about 0.1-0.6A, and the high frequency oscillator 11 The frequency of the signal given to the high frequency switching command circuit is 20-50 KHz, for example 35 KHz.

試験例 1 (強酸化水及びアルカリ水の調製)
図1及び3に示されている通りの装置を使用し、クエン酸を1重量% 及びミネラル塩を2重量%添加した井戸水を被処理水として外槽21及び内槽20内に導入し、10時間通電処理し、次いで放置すると共に外槽内における水溶液の酸化還元電位を経時的に測定した (通電停止後に内槽は装置から抜去した)。
Test Example 1 (Preparation of strong oxidizing water and alkaline water)
Using an apparatus as shown in FIGS. 1 and 3, well water added with 1% by weight of citric acid and 2% by weight of mineral salt is introduced into the outer tank 21 and the inner tank 20 as treated water. The energization treatment was carried out for a period of time and then left standing, and the redox potential of the aqueous solution in the outer tank was measured over time (the inner tank was removed from the apparatus after the energization was stopped).

結果は図3に示されている通りであり、初期値が 30mV であった酸化還元電位は 30 分間で約 800mV になり、通電停止時である 1 時間後には 1150mV に達し、通電停止から 5 時間後においても 900mV 以上であって殺菌・殺虫作用を呈するとされる値である 800mV を上廻り、強酸化水状態を維持していた。このこ とは、外槽内の水溶液を殺菌・殺虫目的で使用する場合の可使時間が 5 時間以上であることを意味している。尚、通電停止時における外槽内水溶液の次亜塩素酸濃度は 35ppm であった。   The results are as shown in Fig. 3. The redox potential, which was 30 mV at the initial value, became approximately 800 mV in 30 minutes, reached 1150 mV after 1 hour when the power supply was stopped, and 5 hours after the power supply was stopped. Later, it was over 900 mV, exceeding the value of 800 mV, which is considered to exhibit bactericidal and insecticidal action, and maintained a strong oxidized water state. This means that the pot life is 5 hours or more when the aqueous solution in the outer tank is used for sterilization and insecticidal purposes. The hypochlorous acid concentration of the aqueous solution in the outer tank when the energization was stopped was 35 ppm.

通電開始前における被処理水のpHは約4であったが、通電停止時における外槽内の水溶液の pH は約3−2.5に低下し、一方内槽内の水溶液はナトリウム分が内槽壁を経て流入することにより pH が約12の強アルカリ性を呈していた。この内槽内水溶液の酸化還元電位は-250mV であり、強還元水状態であった。尚、内槽内の水溶液を抜き出した処、内槽内底部には水酸化ナトリウムと考えられる沈澱が認められた。   The pH of the water to be treated before the start of energization was about 4, but the pH of the aqueous solution in the outer tank dropped to about 3-2.5 when the energization was stopped, while the aqueous solution in the inner tank had a sodium content inside. By flowing through the tank wall, the pH was about 12 which was strongly alkaline. The oxidation-reduction potential of the aqueous solution in the inner tank was −250 mV, and it was in a strongly reduced water state. In addition, the precipitation considered to be sodium hydroxide was recognized by the place which extracted the aqueous solution in an inner tank in the inner tank inner bottom part.

比較試験例 1 (強酸化水の調製)
水溶液の pH 値は初期値が約 4 であり、通電停止時において約 3 であった。
Comparative Test Example 1 (Preparation of strong oxidized water)
The initial pH value of the aqueous solution was about 4, and was about 3 when the power supply was stopped.

試験例 2 及び比較試験例 2 (殺虫試験)
試験例 1 及び比較試験例 1 により得られた強酸化水 (酸化還元電位はそれぞれ 1150mV 及び 1050mV) を被験水 A 及び B として、油虫及び青虫に噴霧し殺 虫効果を調べた。被験水の噴霧から 1 分後の結果は下記の表 1 に示されている通りであり、有効であることが判明した。尚、結果はほぼ同等であるが、被験水A の場合には大きな青虫 (約3cm) に対しても有効であり、1分後に生存していた青虫も15分間経過後には死滅したが、被験水 B の場合には大きな青虫に噴霧すると、弱るが死滅するには至らなかった。
Test example 2 and comparative test example 2 (insecticidal test)
The strong insecticidal water obtained in Test Example 1 and Comparative Test Example 1 (the redox potentials were 1150 mV and 1050 mV, respectively) were used as test waters A and B to spray the oilworms and green worms to examine the insecticidal effect. The result 1 minute after spraying the test water was as shown in Table 1 below and proved to be effective. Although the results are almost the same, test water A is effective against large green caterpillars (about 3 cm), and green caterpillar that survived after 1 minute died after 15 minutes. In the case of water B, spraying on a large green caterpillar weakened but did not die.

[表1]

Figure 2010036169
[Table 1]

Figure 2010036169

試験例 3 及び比較試験例 3
試験例1及び比較試験例1により得られた強酸化水 (酸化還元電位はそれぞれ 1150mV 及び 1050mV) を被験水 C 及び D として青菜に散布して、1日後に観察した結果、若干の変色 (酸焼け) が1部に見られたが、組織的には健常状態であった。
Test Example 3 and Comparative Test Example 3
Strongly oxidized water obtained in Test Example 1 and Comparative Test Example 1 (redox potentials of 1150 mV and 1050 mV, respectively) was sprayed on green vegetables as test waters C and D, and observed one day later. Although burnt) was observed in one part, it was healthy in terms of organization.

装置を電源に接続し、被処理水 (液温 : 20.1℃) を 70 分間に亘って処理し、被処理水の状態を観察しながら経時的に酸化還元電位 (ORP) 及び pH を測定した結果は下記の表 2 に示されている通りであった。装置の消費電力は 300W(6A x 50V) であるが、実効値を初期値は電流が 0.6A に、電圧が 29V に設定されたが、スイッチ操作により外槽内の接地電極を OFF にした時点 (内槽内溶液)のORP が -700mV、pH が 10 - 11 になった時点であり、本試験では電源投入から 15 分間経過した時点) では電流が 5.5A に、電圧が 34V に設定された。   The result of measuring the redox potential (ORP) and pH over time while treating the treated water (liquid temperature: 20.1 ° C) for 70 minutes with the device connected to the power supply and observing the condition of the treated water Was as shown in Table 2 below. The power consumption of the device is 300W (6A x 50V), but the effective value was initially set to 0.6A for current and 29V for voltage, but when the ground electrode in the outer tank was turned off by switch operation. The current was set to 5.5A and the voltage was set to 34V when the ORP of the solution in the inner tank reached -700mV and the pH reached 10-11 (in this test, 15 minutes after the power was turned on). .

[表2]

Figure 2010036169
[Table 2]

Figure 2010036169

上記の表2から明らかなように、外槽内に強酸化水が生成し、内槽内には強還元水が生成する。   As apparent from Table 2 above, strong oxidized water is generated in the outer tank, and strongly reduced water is generated in the inner tank.

試験例 5 (殺虫試験)
試験例において得られた外槽内の溶液を採取し、試験例2と同様に油虫及び青虫に対する殺虫効果を調べた。該溶液の噴霧により油虫 (n = 多数) は1分間以内に完全に死滅し、青虫 (n = 10) も1分後には殆どが死滅し、残余も著しく弱り、5 - 10 分後には完全に死滅した。この結果は試験例2と比較すると、試験例1において得られた強酸化水よりも試験例において得られた強酸化水の方が殺虫力の高いことを示している。尚、試験例において得られた外槽内の強酸化水を殺虫用水として使用する場合の可使時間は試験例1において得られた強酸化水と同様である。
Test Example 5 (Insecticidal test)
The solution in the outer tank obtained in the test example was collected, and the insecticidal effect against oilworms and green worms was examined in the same manner as in Test Example 2. By spraying the solution, oilworms (n = many) are completely killed within 1 minute, green caterpillars (n = 10) are mostly killed after 1 minute, and the remainder is significantly weakened, and after 5 to 10 minutes it is completely Died. This result shows that the strong oxidizing water obtained in the test example is higher in the insecticidal power than the strong oxidizing water obtained in the test example 1 as compared with the test example 2. In addition, the pot life in the case of using the strong oxidation water in the outer tank obtained in the test example as the water for insecticidal use is the same as that of the strong oxidation water obtained in the test example 1.

本発明による強酸化水及び強還元水の製造装置の第 1 実施形を示す概略図である。It is the schematic which shows 1st Embodiment of the manufacturing apparatus of the strong oxidation water and strong reduction water by this invention. 図 1 に示されている装置における高周波交流印加装置部分の回路図である。FIG. 2 is a circuit diagram of a high-frequency AC applying device portion in the apparatus shown in FIG. 図 1 及び 2 に示されている装置を使用して被処理水を処理した場合の処理時間と酸化還元電位との関係及び 1 時間経過後に通電を停止して放置し、経時的に酸化還元電位を測定した結果を示すグラフである。The relationship between the treatment time and redox potential when treated water is treated using the equipment shown in Figs. 1 and 2, and after one hour has elapsed, the energization is stopped and left standing, and the redox potential over time. It is a graph which shows the result of having measured.

符号の説明Explanation of symbols

1 接地電極、
2A、2B 電極板セット、
3 直流電源、
4 可変抵抗、
5A 第1高周波スイッチ、
5B 第2高周波スイッチ、
6A,6B,7A,7B トランジスタ、
8 コンデンサ、
9A,9B 抵抗、
10 高周波切換指令回路、
11 高周波発振器、
12 制御回路、
13 シフトレジスタ、
14 パルス発生器、
15 フリップフロップ回路、
19 バイポーラ電極、
20 内槽、
21 外槽、
30 高周波交流電圧印加装置、
31 水処理部。
1 Ground electrode,
2A, 2B electrode plate set,
3 DC power supply,
4 Variable resistance,
5A 1st high frequency switch,
5B second high frequency switch,
6A, 6B, 7A, 7B transistors,
8 capacitors,
9A, 9B resistance,
10 high frequency switching command circuit,
11 high frequency oscillator,
12 control circuit,
13 Shift register,
14 pulse generator,
15 flip-flop circuit,
19 Bipolar electrodes,
20 inner tank,
21 Outer tank,
30 High-frequency AC voltage application device,
31 Water treatment part.

Claims (6)

無添加の真水である被処理水が収容されている処理容器に接地電極と一対の印加電極を配置し、且つ、前記接地電極が配置されている領域と前記両印加電極が配置されている領域とを半透過性部材により離隔し、更に接地電極と、両印加電極間の導電性を増すために離隔された中間とにバイポーラ電極を配置したこと、
を特徴とする交流による強アルカリ水及び強酸化水の製造装置。
A region where a ground electrode and a pair of application electrodes are arranged in a treatment container containing treated water which is additive-free fresh water, and a region where the ground electrode is arranged and a region where both the application electrodes are arranged And a bipolar electrode arranged between the ground electrode and the middle separated in order to increase the conductivity between the two applied electrodes.
A device for producing strong alkaline water and strong oxidized water by alternating current characterized by the following.
バイポーラ電極は、溶解性の高い亜鉛、アルミニウム、金、鉄、コバルト、ニッケル、マグネシウム、錫の内のいずれか一つの金属であること、
を特徴とする請求項1に記載の交流による強アルカリ水及び強酸化水の製造装置。
The bipolar electrode is made of any one of highly soluble zinc, aluminum, gold, iron, cobalt, nickel, magnesium, tin,
The apparatus for producing strong alkaline water and strong oxidized water by alternating current according to claim 1.
半透過性部材が半透膜、逆浸透膜又は素焼きの陶器、布フィルタであること、
を特徴とする請求項1または2に記載の交流による強アルカリ水及び強酸化水の製造装置。
The semi-permeable member is a semi-permeable membrane, reverse osmosis membrane or unglazed ceramic, cloth filter,
The apparatus for producing strong alkaline water and strong oxidized water by alternating current according to claim 1 or 2.
無添加の真水である被処理水が収容されている処理容器に接地電極と一対の印加電極を配置し、且つ、前記接地電極が配置されている領域と前記両印加電極が配置されている領域とを半透過性部により離隔し、更に接地電極と、両印加電極間の導電性を増すために離隔された中間とにバイポーラ電極を配置して交流による強アルカリ水及び強酸化水の製造装置を形成し、
前記両印加電極に交流電圧を印加して当該両印加電圧が配置されている領域に強酸化水を生成させると共に、前記接地電極が接地されている領域に強アルカリ性水を生成させること、
を特徴とする交流による強アルカリ水及び強酸化水の製造方法。
A region where a ground electrode and a pair of application electrodes are arranged in a treatment container containing treated water which is additive-free fresh water, and a region where the ground electrode is arranged and a region where both the application electrodes are arranged Are separated by a semi-permeable part, and a bipolar electrode is arranged between the ground electrode and the intermediate part separated to increase the conductivity between the two applied electrodes, and an apparatus for producing strong alkaline water and strong oxidized water by alternating current Form the
Applying an alternating voltage to the two applied electrodes to generate strongly oxidized water in a region where the two applied voltages are disposed, and generating strongly alkaline water in a region where the ground electrode is grounded,
A method for producing strong alkaline water and strong oxidized water by alternating current.
真水に請求項4に記載の被処理水および酸,食塩,塩化カリウムを添加して被処理水とし、両印加電極に高周波交流電圧を印可して、当該両印加電圧が配置されている領域に強酸化水を生成させると共に、前記接地電極が接地されている領域に強アルカリ性水を生成させること、
を特徴とする請求項4に記載の交流による強アルカリ水及び強酸化水の製造方法。
The treated water and the acid, salt and potassium chloride according to claim 4 are added to fresh water to form treated water, a high-frequency AC voltage is applied to both applied electrodes, and a region where both applied voltages are arranged Producing strong oxidizing water and producing strongly alkaline water in the area where the ground electrode is grounded;
The method for producing strong alkaline water and strong oxidized water by alternating current according to claim 4.
高周波周波数を制御するFM信号発生器を内蔵しその信号に対応して発振周波数を制御し、なだらかな周波数変動中に急激な上昇又は下降に変化する周波数部分を作成することにより半透過部材内部の水を上昇させ、処理容器内における半透過部材内部の被処理水を排出・取り出すこと、
を特徴とする請求項4または5に記載の交流による強アルカリ水及び強酸化水の製造方法。
An FM signal generator for controlling the high frequency is built in, and the oscillation frequency is controlled in response to the signal, and by creating a frequency portion that changes suddenly during a gentle frequency fluctuation, Raise the water and discharge / take out the water to be treated inside the semi-permeable member in the treatment container;
The method for producing strong alkaline water and strong oxidized water by alternating current according to claim 4 or 5.
JP2008205422A 2008-08-08 2008-08-08 Method and apparatus for producing strong alkaline water and strong oxidized water by alternating current Expired - Fee Related JP5001236B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160355417A1 (en) * 2015-06-08 2016-12-08 Doncreve Co., Ltd. Alternating current electrolysis method for liquid
JP6167391B1 (en) * 2016-09-15 2017-07-26 株式会社環境技研 Hydrogen water generator

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JP2004344746A (en) * 2003-05-21 2004-12-09 Hideo Hayakawa Alternating current electrolysis method and apparatus therefor
JP2005095725A (en) * 2003-09-22 2005-04-14 Denso Corp Electrolytic water generating apparatus
JP2006035053A (en) * 2004-07-23 2006-02-09 Separeetaa Syst Kogyo Kk Oxidation-reduction water making method, oxidation-reduction water and oxidation-reduction water making apparatus

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JP2000084560A (en) * 1998-09-14 2000-03-28 Hideo Hayakawa Preparation of strongly oxidizing water and strongly reducing water and apparatus therefor
JP2004344746A (en) * 2003-05-21 2004-12-09 Hideo Hayakawa Alternating current electrolysis method and apparatus therefor
JP2005095725A (en) * 2003-09-22 2005-04-14 Denso Corp Electrolytic water generating apparatus
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Publication number Priority date Publication date Assignee Title
US20160355417A1 (en) * 2015-06-08 2016-12-08 Doncreve Co., Ltd. Alternating current electrolysis method for liquid
JP6167391B1 (en) * 2016-09-15 2017-07-26 株式会社環境技研 Hydrogen water generator
JP2018043210A (en) * 2016-09-15 2018-03-22 株式会社環境技研 Hydrogen Water Generator

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