JP5010037B2 - Method for producing electrolyzed water and composition - Google Patents
Method for producing electrolyzed water and composition Download PDFInfo
- Publication number
- JP5010037B2 JP5010037B2 JP2011023824A JP2011023824A JP5010037B2 JP 5010037 B2 JP5010037 B2 JP 5010037B2 JP 2011023824 A JP2011023824 A JP 2011023824A JP 2011023824 A JP2011023824 A JP 2011023824A JP 5010037 B2 JP5010037 B2 JP 5010037B2
- Authority
- JP
- Japan
- Prior art keywords
- ppm
- hydrochloric acid
- water
- electrolyzed water
- sodium bicarbonate
- 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 - Fee Related
Links
Images
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Description
本発明は希塩酸を電気分解し、水で希釈して微酸性電解水を調製する技術に関する。より詳しくは、電気分解して微酸性の電解水を生成する方法および原料として使用する組成物に関する。 The present invention relates to a technique for preparing slightly acidic electrolyzed water by electrolyzing dilute hydrochloric acid and diluting it with water. More specifically, the present invention relates to a method of electrolyzing to generate slightly acidic electrolyzed water and a composition used as a raw material.
近年の衛生医療分野は、人の移動の激化や、食品や食品材料流通のグローバル化あるいは抗生剤に頼る医療などに見られる社会的変化に伴って、耳慣れない病原体や薬剤耐性の微生物によって引き起こされる大規模感染や難治癒疾病に直面している。それらのニュースに日々接している国民の不安は募り、いきおい衛生対策に対する関心も高まっている。それに伴って、対策としての殺菌剤、殺菌機能付商品の市場は拡大を続けている。そのような中、10数年前に殺菌剤の新顔として登場した、塩素イオンの電解により生成される所謂殺菌用電解水は、厚労省の規格制定などの後押しもあり、国民生活の中に定着しつつある。 In recent years, the field of hygiene and medical care is caused by pathogens and drug-resistant microorganisms that are unfamiliar to ears, due to intensifying human movement, globalization of the distribution of food and food materials, and social changes such as medical care that relies on antibiotics. Facing outbreaks and incurable diseases. The people who are in contact with these news every day are worried and the interest in hygiene measures is growing. Along with this, the market for bactericides as a countermeasure and products with bactericidal functions continues to expand. Under such circumstances, so-called bactericidal electrolyzed water produced by electrolysis of chloride ions, which appeared as a new face of bactericides 10 years ago, has been supported by the establishment of the Ministry of Health, Labor and Welfare standards, Is becoming established.
殺菌用電解水の中の微酸性電解水(食品添加物名「微酸性次亜塩素酸水」)は希塩酸を無隔膜電解槽で電気分解して生成される(特許文献1)。したがって、塩類を殆んど含まず、周囲への影響もないため、通常の殺菌洗浄としての利用法の他、噴霧使用が可能で、環境殺菌、脱臭、安全な加湿など幅広い利用が始まっている。本発明はこの微酸性電解水の生成における便宜性をさらに高め、普及に拍車をかける目的で行われたものである。 Slightly acidic electrolyzed water (name of food additive “slightly acidic hypochlorous acid water”) in the electrolyzed water for sterilization is generated by electrolyzing dilute hydrochloric acid in a non-diaphragm electrolyzer (Patent Document 1). Therefore, it contains almost no salt and has no effect on the surroundings. Therefore, it can be used for spraying in addition to the usual sterilization washing, and has started to be widely used for environmental sterilization, deodorization, safe humidification, etc. . The present invention has been made for the purpose of further enhancing convenience in the production of the slightly acidic electrolyzed water and spurring its spread.
前述のように多くの優れた性質を持った微酸性電解水は徐々に普及しているが、さらに普及を促進するためにはその生成方法において利便性を高めることが求められている。 As described above, slightly acidic electrolyzed water having many excellent properties is gradually spreading, but in order to further promote the spread, it is required to improve convenience in its production method.
微酸性電解水は希塩酸を無隔膜電解槽で電解し、生成した電解液を水で希釈することによって調製される。希塩酸に含まれる塩素イオンが下記式(1)のように電極酸化されて単体の塩素となり、その塩素が水と反応して下記式(2)のように次亜塩素酸(HOCl)が生成される。 The slightly acidic electrolyzed water is prepared by electrolyzing dilute hydrochloric acid in a non-diaphragm electrolyzer and diluting the produced electrolyte with water. Chlorine ions contained in dilute hydrochloric acid are electrode oxidized as shown in the following formula (1) to form single chlorine, which reacts with water to produce hypochlorous acid (HOCl) as shown in the following formula (2). The
この次亜塩素酸が殺菌成分である。ところが、上記式(2)から分かるように次亜塩素酸と同時に塩酸が発生する。このようにして発生した塩酸の一部はそのまま電解槽から排出されることがある。電解槽を出た後水により希釈されるが、希釈倍率が1000倍以上と極めて高いために、通常は、希釈の効果と希釈水に含まれる硬度成分によって中和され、生成水は名前の通り微酸性領域のpHを示すことになる。 This hypochlorous acid is a bactericidal component. However, as can be seen from the above formula (2), hydrochloric acid is generated simultaneously with hypochlorous acid. Part of the hydrochloric acid generated in this way may be discharged from the electrolytic cell as it is. After leaving the electrolytic cell, it is diluted with water, but since the dilution ratio is extremely high, 1000 times or more, it is usually neutralized by the effect of dilution and the hardness component contained in the diluted water, and the generated water is as the name suggests. It indicates the pH of the slightly acidic region.
しかし、希釈水の硬度が極めて低い場合は、硬度成分による中和作用が低いため、所定のpHを下回ることもあり、その対策として電解条件を調整し、電解槽から排出される塩酸量を減少させる必要があった。又他の対策として、元々の希塩酸の濃度を低くしておくという方法もある。しかし、原料の塩酸の濃度が低くなれば、当然塩素イオン濃度が低下し、電解時の単体塩素の発生効率も低下してしまう。そこで、本発明者は、希塩酸を無隔膜電解槽で電解し微酸性電解水を生成する方法において、電解条件を調整する手間を要せず、かつ単体塩素の発生効率を低下させず、低硬度水を使用したときにも所定のpHの微酸性電解水を生成する方法および組成物を提供することを課題とした。 However, when the hardness of the dilution water is extremely low, the neutralization effect by the hardness component is low, so it may be lower than the predetermined pH. As a countermeasure, the electrolysis conditions are adjusted and the amount of hydrochloric acid discharged from the electrolytic cell is reduced. It was necessary to let them. As another countermeasure, there is a method of reducing the original concentration of dilute hydrochloric acid. However, if the concentration of the hydrochloric acid as the raw material is lowered, the chlorine ion concentration is naturally lowered, and the generation efficiency of simple chlorine during electrolysis is also lowered. Therefore, the present inventor, in a method for producing slightly acidic electrolyzed water by electrolyzing dilute hydrochloric acid in a diaphragmless electrolytic cell, does not require time and effort to adjust electrolysis conditions, does not reduce the generation efficiency of simple chlorine, and has low hardness. An object of the present invention is to provide a method and a composition for producing slightly acidic electrolyzed water having a predetermined pH even when water is used.
多くの優れた性質を持った微酸性電解水の普及を促進するためにはその生成方法において利便性を高めることが必要であり、そのために、本発明者は電解条件を調整せず、かつ単体塩素の発生効率の低下も伴わず、低硬度水を使用したときにも所定のpHの微酸性電解水を調製する方法を提供するための手段の研究を進めた。 In order to promote the widespread use of slightly acidic electrolyzed water having many excellent properties, it is necessary to improve convenience in its production method. For this reason, the present inventor does not adjust the electrolysis conditions and is simple Research was conducted on means for providing a method for preparing slightly acidic electrolyzed water having a predetermined pH even when low hardness water was used without reducing the generation efficiency of chlorine.
そこでまず、化1式と化2式をそれぞれの辺どうし足し合わせ整理すると、化3式に示した電解反応全体を通した物質の収支式が得られることに着目した。
First, attention was paid to the fact that the balance equation of the substance through the entire electrolytic reaction shown in the chemical formula 3 can be obtained by adding and organizing the chemical formula 1 and the
上記式(3)は、最初の塩酸が解離して生成した水素イオンが水素ガスとなって系外に出ることによりpHが上昇することを示している。従って、電解液中の塩酸残量を少なくするための他の方法として考えられるのは、電解前の水素イオン濃度を下げておけばよいと考えた。さらに、原液の塩素イオン濃度を下げず、かつ原液の電気伝導度を下げない方法としては、水素イオンの一部を、他の陽イオンで置き換えておけばよいということに着想した。 The above formula (3) shows that the pH rises when hydrogen ions generated by dissociation of the first hydrochloric acid are converted into hydrogen gas and exit from the system. Therefore, as another method for reducing the remaining amount of hydrochloric acid in the electrolytic solution, it was thought that the hydrogen ion concentration before electrolysis should be lowered. Furthermore, as a method for reducing the chlorine ion concentration of the stock solution and not lowering the electrical conductivity of the stock solution, the inventors conceived that some of the hydrogen ions may be replaced with other cations.
そして、本発明者は、塩酸を希釈する水に重炭酸ナトリウムを溶解しておくことで、化4式に示すような反応によって、水素イオンの一部がナトリウムイオンによって置換され、その他の化学成分が塩酸のみを水で希釈したときと同じであることを確認して、これを、課題を解決するための第1の態様とした。
Then, the present inventor dissolved sodium bicarbonate in water for diluting hydrochloric acid, whereby a part of hydrogen ions was replaced by sodium ions by the reaction shown in the
次に、重炭酸ナトリウムの添加量については、原水の硬度に応じて増減する必要があると考えられるが、日本国内の水道水について硬度の調査をした結果、公共水道として最も低硬度と考えられるのが10ppm前後であった。そこで、希塩酸の塩酸濃度を20%以下とするとき、硬度10ppmの水で所定のpH の微酸性電解水を調製することができる塩酸希釈水の重炭酸ナトリウム濃度が700ppmであることを確認し、又、硬度40ppmの水で所定のpHの微酸性電解水を調製することができる塩酸希釈水の重炭酸ナトリウム濃度が300ppmであることも確認するに至り、希釈水の重炭酸ナトリム濃度を0.1ppm以上、700ppm以下、より好ましくは300ppm以上、700ppm以下とすることを、課題を解決するための第2の態様とした。 Next, the amount of sodium bicarbonate added may need to be increased or decreased depending on the hardness of the raw water, but as a result of a survey of the hardness of tap water in Japan, it is considered to have the lowest hardness for public water supply. Was around 10 ppm. Accordingly, when the hydrochloric acid concentration of dilute hydrochloric acid is 20% or less, it is confirmed that the sodium bicarbonate concentration of hydrochloric acid-diluted water capable of preparing a slightly acidic electrolyzed water having a predetermined pH with water having a hardness of 10 ppm is 700 ppm. It has also been confirmed that the sodium bicarbonate concentration of hydrochloric acid-diluted water capable of preparing slightly acidic electrolyzed water having a predetermined pH with water having a hardness of 40 ppm is 300 ppm. The second mode for solving the problem is to set 1 ppm to 700 ppm, more preferably 300 ppm to 700 ppm.
さらに以上のような重炭酸ナトリウム溶液で予め希釈調製した希塩酸は、そのまま軟水を原料とする微酸性電解水の調製に利用できることに着想し、重炭酸ナトリム濃度が0.1ppm以上、700ppm以下、より好ましくは300ppm以上、700ppm以下の重炭酸ナトリウム溶液で希釈調製した希塩酸を課題を解決するための第3の態様としたことにより、本発明を完成させた。 Furthermore, the dilute hydrochloric acid prepared by diluting in advance with the sodium bicarbonate solution as described above can be used as it is for the preparation of slightly acidic electrolyzed water using soft water as a raw material, and the sodium bicarbonate concentration is 0.1 ppm or more and 700 ppm or less. The present invention was completed by using diluted hydrochloric acid diluted with a sodium bicarbonate solution of preferably 300 ppm or more and 700 ppm or less as a third embodiment for solving the problems.
本発明によって、塩酸を希釈する水に重炭酸ナトリウムを溶解しておくことで、硬度の極端に低い原水を使って微酸性電解水を調製するときにも、電解条件の調整や希塩酸濃度を下げるなどの対策をしないでも所定pHの微酸性電解水を調製することができるようになった。 By dissolving sodium bicarbonate in water for diluting hydrochloric acid according to the present invention, even when preparing slightly acidic electrolyzed water using raw water with extremely low hardness, adjustment of electrolysis conditions and dilute hydrochloric acid concentration are reduced. It is now possible to prepare slightly acidic electrolyzed water having a predetermined pH without taking measures such as the above.
あるいはまた、本発明によれば、希釈水の重炭酸ナトリム濃度を0.1ppm以上、700ppm以下、より好ましくは300ppm以上、700ppm以下とすることによって、硬度が10ppm程度の原水でも適正なpHの微酸性電解水を生成することができるようになった。さらには、重炭酸ナトリム濃度が0.1ppm以上、700ppm以下、より好ましくは300ppm以上、700ppm以下の重炭酸ナトリウム溶液で希釈調製した希塩酸を提供することにより、軟水でも手軽に適正pHの微酸性電解水を精製することが可能になった。 Alternatively, according to the present invention, the concentration of sodium bicarbonate in diluted water is 0.1 ppm or more and 700 ppm or less, more preferably 300 ppm or more and 700 ppm or less. Acidic electrolyzed water can be generated. Furthermore, by providing dilute hydrochloric acid diluted with a sodium bicarbonate solution having a sodium bicarbonate concentration of 0.1 ppm or more and 700 ppm or less, more preferably 300 ppm or more and 700 ppm or less, a slight acidic electrolysis with an appropriate pH can be easily performed even in soft water. It became possible to purify the water.
次に、本発明の理解を確実にするために実施例を元に本発明を実施するための最良の形態の一例を説明する。但し、実施例の記載内容は各実施例に限定されるもので、本特許の請求範囲とは直接の関係は無い。 Next, in order to ensure an understanding of the present invention, an example of the best mode for carrying out the present invention will be described based on the examples. However, the description of the examples is limited to each example, and is not directly related to the claims of this patent.
35%濃度の食品添加物塩酸を、700ppmの重炭酸ナトリウム溶液で希釈し、9%の希塩酸を調製した。この希塩酸を使い、図1にフロー図を示した自作の電解装置を使って微酸性電解水を生成した。電解槽(2)は10×20cmの平板電極で3セルの複極式とした。カルシウム硬度10ppmの原水は定流量弁(3)によって300L/hの一定流量に調整し、電解電圧は2.5Vの定電圧、電解電流は目標30Aとした。希塩酸は、電流値が30Aを切ったとき希塩酸供給ポンプ(1)で電解槽に供給し、30Aを超えたときに供給を停止するように制御し生成した。その結果、有効塩素濃度18ppm、pH5.6の微酸性電解水が300L/hで生成された。 35% strength food additive hydrochloric acid was diluted with 700 ppm sodium bicarbonate solution to prepare 9% dilute hydrochloric acid. Using this dilute hydrochloric acid, slightly acidic electrolyzed water was produced using a self-made electrolyzer whose flow diagram is shown in FIG. The electrolytic cell (2) was a 10 × 20 cm plate electrode and a 3 cell bipolar type. The raw water with a calcium hardness of 10 ppm was adjusted to a constant flow rate of 300 L / h by a constant flow valve (3), the electrolysis voltage was a constant voltage of 2.5 V, and the electrolysis current was a target of 30 A. The dilute hydrochloric acid was generated by supplying the dilute hydrochloric acid supply pump (1) to the electrolytic cell when the current value cuts off 30A, and stopping the supply when the current value exceeded 30A. As a result, slightly acidic electrolyzed water having an effective chlorine concentration of 18 ppm and a pH of 5.6 was produced at 300 L / h.
また別の実施例で本発明を実施するための別の最良の形態の一例を説明する。35%濃度の食品添加物塩酸を、300ppmの重炭酸ナトリウム溶液で希釈し、9%の希塩酸を調製した。この希塩酸を使い、実施例1と同じ装置を使って微酸性電解水を生成した。カルシウム硬度40ppmの原水流量を300L/hとし、電解電圧2.5V、電解電流30Aで生成した結果、有効塩素濃度20ppm、pH5.8の微酸性電解水が300L/hで生成された。 Another example of another best mode for carrying out the present invention will be described in another example. 35% strength food additive hydrochloric acid was diluted with 300 ppm sodium bicarbonate solution to prepare 9% dilute hydrochloric acid. Using this dilute hydrochloric acid, slightly acidic electrolyzed water was produced using the same apparatus as in Example 1. The raw water flow rate with a calcium hardness of 40 ppm was 300 L / h, and the electrolysis voltage was 2.5 V and the electrolysis current was 30 A. As a result, slightly acidic electrolyzed water having an effective chlorine concentration of 20 ppm and a pH of 5.8 was produced at 300 L / h.
さらに別の実施例で本発明を実施するための又別の最良の形態の一例を説明する。35%濃度の食品添加物塩酸を、700ppmの重炭酸ナトリウム溶液で希釈し、9%の希塩酸を調製した。この希塩酸を使い、実施例1と同じ装置を使って微酸性電解水を生成した。カルシウム硬度110ppmの原水流量を300L/hとし、電解電圧2.2V、電解電流30Aで生成した結果、有効塩素濃度20ppm、pH6.0の微酸性電解水が300L/hで生成された。 Further, another example of another best mode for carrying out the present invention will be described. 35% strength food additive hydrochloric acid was diluted with 700 ppm sodium bicarbonate solution to prepare 9% dilute hydrochloric acid. Using this dilute hydrochloric acid, slightly acidic electrolyzed water was produced using the same apparatus as in Example 1. The raw water flow rate with a calcium hardness of 110 ppm was 300 L / h, and the electrolysis voltage was 2.2 V and the electrolysis current was 30 A. As a result, slightly acidic electrolyzed water having an effective chlorine concentration of 20 ppm and a pH of 6.0 was produced at 300 L / h.
1 希塩酸供給ポンプ
2 電解槽
3 定流量弁
4 直流定電圧電源
5 制御装置
6 希塩酸タンク
DESCRIPTION OF SYMBOLS 1 Dilute hydrochloric
Claims (4)
前記電気分解の生成物をカルシウム硬度を有する水で希釈する工程と
を含む、有効塩素濃度が18ppm〜20ppmであって、pHが5.6〜6.0の範囲である電解水の生成方法。 Electrolyzing dilute hydrochloric acid containing hydrochloric acid and sodium bicarbonate in a non-diaphragm electrolytic cell;
A method for producing electrolyzed water having an effective chlorine concentration of 18 ppm to 20 ppm and a pH of 5.6 to 6.0, comprising a step of diluting the electrolysis product with water having calcium hardness.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2011023824A JP5010037B2 (en) | 2011-02-07 | 2011-02-07 | Method for producing electrolyzed water and composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2011023824A JP5010037B2 (en) | 2011-02-07 | 2011-02-07 | Method for producing electrolyzed water and composition |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2007317785A Division JP2009136814A (en) | 2007-12-08 | 2007-12-08 | Preparation method of weak acidic electrolytic water |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2011088149A JP2011088149A (en) | 2011-05-06 |
JP5010037B2 true JP5010037B2 (en) | 2012-08-29 |
Family
ID=44106899
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2011023824A Expired - Fee Related JP5010037B2 (en) | 2011-02-07 | 2011-02-07 | Method for producing electrolyzed water and composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP5010037B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6051426B2 (en) * | 2011-06-02 | 2016-12-27 | 株式会社ナノジェットジャパン | Bactericidal agent with excellent permeability and sterilizing method |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2627100B2 (en) * | 1990-08-10 | 1997-07-02 | 株式会社オムコ | Method and apparatus for producing sterilized water |
JP2627101B2 (en) * | 1990-09-19 | 1997-07-02 | 株式会社オムコ | Additive chemicals for the production of electrolytic hypochlorous acid sterilized water |
JP3798486B2 (en) * | 1995-11-08 | 2006-07-19 | 森永乳業株式会社 | Disinfectant manufacturing method, manufacturing apparatus and disinfectant, and disinfecting method |
JPH09253650A (en) * | 1996-03-22 | 1997-09-30 | Japan Storage Battery Co Ltd | Sterilized water making apparatus |
JP4056623B2 (en) * | 1998-05-13 | 2008-03-05 | 松下エコシステムズ株式会社 | Electrolytic tank of electrolysis neutral water generator |
GB2348209B (en) * | 1999-03-24 | 2001-05-09 | Ionex Ltd | Water purification process |
JP2003010852A (en) * | 2001-07-02 | 2003-01-14 | Morinaga Milk Ind Co Ltd | Method for operating diaphragm-free electrolytic cell and method for making electrolytic water |
JP2004298807A (en) * | 2003-03-31 | 2004-10-28 | Toto Ltd | Electrolytic cel |
JP2004314049A (en) * | 2003-04-04 | 2004-11-11 | Mitsubishi Electric Corp | Regeneration apparatus for adsorbent adsorbed with ammonia and regenerating method |
JP2009136814A (en) * | 2007-12-08 | 2009-06-25 | Toyohiko Doi | Preparation method of weak acidic electrolytic water |
US20130112571A1 (en) * | 2010-06-14 | 2013-05-09 | Hocl Inc. | Electrolytic apparatus and method for producing slightly acidic electrolyzed water |
-
2011
- 2011-02-07 JP JP2011023824A patent/JP5010037B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JP2011088149A (en) | 2011-05-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2892547C (en) | An electrolyzed water generating method and a generator | |
JP6457737B2 (en) | Acid electrolyzed water and method for producing the same, bactericide and cleaning agent containing the acid electrolyzed water, sterilizing method using the acid electrolyzed water, and apparatus for producing acid electrolyzed water | |
JP2009136814A (en) | Preparation method of weak acidic electrolytic water | |
NZ613038A (en) | Compact closed-loop electrolyzing process and apparatus | |
WO2004080901A1 (en) | Process for producing mixed electrolytic water | |
JP6268383B2 (en) | ELECTROLYTIC WATER GENERATION DEVICE AND METHOD FOR OPERATING THE SAME | |
KR101145326B1 (en) | Sterile water producing method and apparatus | |
CN103774172A (en) | Production method and device of high-stability hypochlorous acid | |
JP5010037B2 (en) | Method for producing electrolyzed water and composition | |
JP2007301541A (en) | Slightly acidic electrolyzed water generation method and apparatus | |
CN203653706U (en) | Hypochlorous acid solution generator and electrolyzer thereof | |
CN1753838A (en) | Method for producing mixed electrolyzed water | |
WO2013068599A2 (en) | Process for producing an anolyte composition | |
KR101346551B1 (en) | Manufacturing method of weak acidic hypochlorous acid water and hypochlorous acid water manufactured by the same that | |
JP2014148526A (en) | Method for producing disinfectant antiseptic solution | |
JP2017087084A (en) | Acidic electrolytic water and method for producing the same, bactericide and detergent comprising acidic electrolytic water, and device for producing acidic electrolytic water | |
JP5711945B2 (en) | Electrolyzer for generating hypochlorous acid water and method for generating hypochlorous acid water | |
WO2013064695A2 (en) | Process for preparing an anolyte liquid | |
KR20130103875A (en) | Manufacturing method of weak-acidic hypochlorous acid water and system thereof | |
KR101436111B1 (en) | Method and device for generating sterilizing agent | |
JP2005125276A (en) | Sterilizing electrolytic water making apparatus | |
RU2012113272A (en) | METHOD OF ELECTROCHEMICAL WATER TREATMENT AND DEVICE | |
CN110065998A (en) | A kind of drinking water electrochemical disinfection method for inhibiting bromine class by-product to generate | |
EE05823B1 (en) | Diaphragm-electrolyser | |
WO2013064688A2 (en) | Process for preparing an electrochemically activated water-based solution |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20111102 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20111122 |
|
A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20120118 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20120522 |
|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20120531 |
|
R150 | Certificate of patent or registration of utility model |
Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20150608 Year of fee payment: 3 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
S533 | Written request for registration of change of name |
Free format text: JAPANESE INTERMEDIATE CODE: R313533 |
|
R350 | Written notification of registration of transfer |
Free format text: JAPANESE INTERMEDIATE CODE: R350 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
LAPS | Cancellation because of no payment of annual fees |