JP5102553B2 - Electrolyzed water generator - Google Patents

Electrolyzed water generator Download PDF

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JP5102553B2
JP5102553B2 JP2007193247A JP2007193247A JP5102553B2 JP 5102553 B2 JP5102553 B2 JP 5102553B2 JP 2007193247 A JP2007193247 A JP 2007193247A JP 2007193247 A JP2007193247 A JP 2007193247A JP 5102553 B2 JP5102553 B2 JP 5102553B2
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electrolysis
water
electrode
electrolysis current
current value
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JP2009028598A (en
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久徳 白水
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Panasonic Corp
Panasonic Holdings Corp
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Matsushita Electric Industrial Co Ltd
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本発明は原水を電気分解してイオン水を生成する電解水生成装置に係り、特に、原水の水質の違いや電気伝導度の変化がある場合でも誤った判断をすることなく、確実に精度良く電極寿命を判断し得る電解水生成装置に関する。   The present invention relates to an electrolyzed water generating apparatus that electrolyzes raw water to generate ionic water, and in particular, accurately and accurately without making erroneous judgments even when there is a difference in raw water quality or electrical conductivity. The present invention relates to an electrolyzed water generating apparatus capable of determining an electrode life.

近年の安全な水や健康に対する関心の高まりに伴って、水道水等を原水としてこれを電解槽内で電気分解することでアルカリイオン水と酸性イオン水を生成すると共に、このアルカリイオン水と酸性イオン水の一方を吐出管から利用可能に吐出し、他方を排出管から排出する構成の電解水生成装置が一般家庭にも広く普及するに至っている。   With the recent increase in interest in safe water and health, tap water and other raw water are electrolyzed in an electrolytic cell to produce alkaline ionized water and acidic ionized water. An electrolyzed water generating apparatus having a configuration in which one of ionic water is discharged from a discharge pipe so as to be usable and the other is discharged from a discharge pipe has been widely spread to general households.

このような電解水生成装置では、電解槽内を隔膜によって陰極および陽極の電極室に分割し、それぞれに配置された電極板(陰極および陽極)間に直流電圧を印加して原水を電気分解し、電解イオン水を連続的に供給するが、電気分解する電極板の表面には水に含まれる不純物(カルシウム等のスケール)が析出して堆積するようになり、電気分解が次第に困難となる。この電気分解によって付着する不純物を除去するために、電極板間に印加する直流電圧の極性を反転させて一定時間印加し、電極板表面の不純物を溶出させ洗浄除去することが行われている。   In such an electrolyzed water generating apparatus, the inside of the electrolytic cell is divided into cathode and anode electrode chambers by a diaphragm, and a direct voltage is applied between the electrode plates (cathode and anode) arranged in each to electrolyze the raw water. Although electrolytic ion water is continuously supplied, impurities (scale such as calcium) contained in water are deposited and deposited on the surface of the electrode plate to be electrolyzed, and electrolysis becomes increasingly difficult. In order to remove impurities adhering by this electrolysis, the polarity of the DC voltage applied between the electrode plates is reversed and applied for a predetermined time, and the impurities on the electrode plate surface are eluted and washed away.

この洗浄により電気分解能力は回復するものの、電解および洗浄の繰り返しにより電極板が徐々に劣化して行きイオン水が生成できなくなることから、例えば特開平6−31275号公報に開示された「イオン水生成器の電解槽の電極の寿命表示方法」では、図6に示すように、積算された洗浄回数が8000回以上であり(ステップS101)、積算された電解時間が10年以上であり(ステップS102)、且つ、電極洗浄時の電解電流が使用開始時の電極洗浄電解電流(初期電流値)と比較して50%以下になったとき、電極寿命と判断して、電極が寿命に達している旨の表示を行うようにしている。
特開平6−31275号公報
Although the electrolysis capability is restored by this washing, the electrode plate gradually deteriorates due to repeated electrolysis and washing, so that ionic water cannot be generated. For example, the “ionic water” disclosed in Japanese Patent Application Laid-Open No. 6-3275 is disclosed. As shown in FIG. 6, in the method of displaying the lifetime of the electrode of the electrolytic cell of the generator, the accumulated number of cleanings is 8000 times or more (step S101), and the accumulated electrolysis time is 10 years or more (step S102), and when the electrolysis current at the time of electrode cleaning becomes 50% or less compared to the electrode cleaning electrolysis current (initial current value) at the start of use, it is determined that the electrode has reached the end of its life. Is displayed.
JP-A-6-31275

しかしながら、上述した特許文献1に開示された技術においては、原水の水質の違い、特に電気伝導度の違いにより電極が劣化していないにもかかわらず電極寿命と判断してしまい、また同一の使用場所においても時間の経過による電気伝導度の変化により電極が劣化していないにもかかわらず電極寿命と判断してしまい、或いは、電極が劣化しているにもかかわらず電極寿命と判断しない場合もあるという事情があった。例えば、使用開始時にのみ原水の電気伝導度が高く、その後、電気伝導度が低く推移した場合には、電極が劣化していないにもかかわらず電極寿命の条件を満たして電極寿命と判断してしまうことが考えられる。また、これとは反対に、使用開始時にのみ原水の電気伝導度が低く、その後、電気伝導度が高く推移した場合には、電極が劣化しているにもかかわらず電極寿命の条件を満たさず電極寿命と判断されないことが考えられる。   However, in the technique disclosed in Patent Document 1 described above, the life of the electrode is determined even though the electrode is not deteriorated due to the difference in the quality of raw water, particularly the difference in electrical conductivity, and the same use Even if the electrode is not deteriorated due to changes in electrical conductivity over time, it may be determined that the electrode life is not reached, or the electrode life may not be determined even if the electrode is deteriorated. There was a circumstance that there was. For example, if the electrical conductivity of raw water is high only at the start of use and then the electrical conductivity is low, it is determined that the electrode life is satisfied by satisfying the electrode life conditions even though the electrode is not deteriorated. It is possible to end up. On the other hand, if the electrical conductivity of raw water is low only at the start of use, and then the electrical conductivity remains high, the electrode life condition is not satisfied even though the electrode has deteriorated. It is conceivable that the life of the electrode is not judged.

本発明は、上記従来の事情に鑑みてなされたものであって、原水の水質の違いや電気伝導度の変化がある場合でも誤った判断をすることなく、確実に精度良く電極寿命を判断し得る電解水生成装置を提供することを目的としている。   The present invention has been made in view of the above-described conventional circumstances, and even when there is a difference in the quality of raw water or a change in electrical conductivity, it is possible to reliably determine the electrode life without making an erroneous determination. It aims at providing the electrolyzed water generating apparatus to obtain.

上記目的を達成するために、本発明に係る電解水生成装置は、隔膜により分割された陰極室と陽極室に各々電極が挿入され、通水された原水を電気分解してアルカリイオン水および酸性イオン水を生成する電解槽と、前記電解槽の電極間に印加する電解電圧を制御する制御部と、を備え、前記電解槽内で生成されたアルカリイオン水および酸性イオン水の一方を吐出管から吐出し、他方を排出管から排出する電解水生成装置において、前記制御部は、前記電極間に流れる電解電流を検出する電解電流検出手段と、前記原水を電気分解するために前記電極間に電解電圧を印加したときの前記電解電流検出手段による正電解電流値と、前記電極間に印加する電解電圧の極性を反転させたときの前記電解電流検出手段による逆電解電流値との差を求める正電解逆電解電流比較手段と、を備え、前記正電解電流値と前記逆電解電流値の差に基づき前記電極の劣化状態を判別することを第1の特徴とする。   In order to achieve the above object, an electrolyzed water generating apparatus according to the present invention includes an electrode inserted into each of a cathode chamber and an anode chamber divided by a diaphragm, and electrolyzes the raw water that has been passed through to alkaline ionized water and acidic water. An electrolytic cell for generating ionic water, and a controller for controlling an electrolysis voltage applied between the electrodes of the electrolytic cell, and discharging one of the alkaline ionic water and acidic ionic water generated in the electrolytic cell. In the electrolyzed water generating apparatus that discharges from the discharge pipe and discharges the other through the discharge pipe, the control unit includes an electrolysis current detecting unit that detects an electrolysis current flowing between the electrodes and an electrode for electrolyzing the raw water. The difference between the positive electrolysis current value by the electrolysis current detection means when an electrolysis voltage is applied and the reverse electrolysis current value by the electrolysis current detection means when the polarity of the electrolysis voltage applied between the electrodes is reversed is obtained. That a positive electrolyte reverse electrolysis current comparator means comprises, a first feature in that to determine the deterioration state of the electrode based on the difference of the reverse electrolysis current value and the positive electrolytic current value.

また、本発明に係る電解水生成装置は、前記制御部は、前記電極間に電解電圧を印加してから所定時間が経過したときに検出した前記正電解電流値と前記逆電解電流値の差に基づき前記電極の劣化状態を判別することを第2の特徴とする。   In the electrolyzed water generating apparatus according to the present invention, the control unit may detect a difference between the positive electrolysis current value and the reverse electrolysis current value detected when a predetermined time elapses after applying an electrolysis voltage between the electrodes. The second feature is that the deterioration state of the electrode is determined based on the above.

さらに、本発明に係る電解水生成装置は、前記制御部は、前記原水の通水が停止しているときに検出した前記正電解電流値と前記逆電解電流値の差に基づき前記電極の劣化状態を判別することを第3の特徴とする。   Furthermore, in the electrolyzed water generating apparatus according to the present invention, the control unit is configured to degrade the electrode based on a difference between the positive electrolysis current value and the reverse electrolysis current value detected when the flow of the raw water is stopped. The third feature is to determine the state.

本発明に係る第1の特徴の電解水生成装置では、原水の水質の違いや電気伝導度の変化がある場合でも誤った判断をすることなく、確実に精度良く電極寿命を判断することができる。   In the electrolyzed water generating apparatus according to the first feature of the present invention, the electrode life can be determined accurately and accurately without making an erroneous determination even when there is a difference in the quality of raw water or a change in electrical conductivity. .

また、本発明に係る第2の特徴の電解水生成装置では、電極からのスケールの溶出による過渡的な電解電流の変化を判別対象から除外して、より精度良く電極寿命を判断することができる。   Moreover, in the electrolyzed water generating apparatus having the second feature according to the present invention, the electrode life can be determined with higher accuracy by excluding the transient electrolysis current change due to the elution of the scale from the electrodes from the determination target. .

さらに、本発明に係る第3の特徴の電解水生成装置では、使用の度毎に流量が変化する場合でも、より精度良く電極寿命を判断し得る電解水生成装置を提供することができる。   Furthermore, in the electrolyzed water generating apparatus of the third feature according to the present invention, an electrolyzed water generating apparatus that can determine the electrode life more accurately even when the flow rate changes with each use can be provided.

以下、本発明の電解水生成装置の実施例について、〔実施例1〕、〔実施例2〕、〔実施例3〕の順に図面を参照して詳細に説明する。   Hereinafter, the Example of the electrolyzed water generating apparatus of this invention is described in detail with reference to drawings in order of [Example 1], [Example 2], and [Example 3].

〔実施例1〕
図1は本発明の実施例に係る電解水生成装置の構成図である。同図において、本実施例の電解水生成装置は、隔膜8により分割された陰極室と陽極室に各々電極板9,10が挿入され、通水された原水を電気分解してアルカリイオン水および酸性イオン水を生成する電解槽7と、電解槽7の電極間に印加する電解電圧を制御する制御部15と、を備え、電解槽7内で生成されたアルカリイオン水および酸性イオン水の一方を吐出管12から吐出し、他方を排出管11から排出するものである。
[Example 1]
FIG. 1 is a configuration diagram of an electrolyzed water generating apparatus according to an embodiment of the present invention. In the figure, the electrolyzed water generating apparatus of the present embodiment has electrode plates 9 and 10 inserted respectively in the cathode chamber and the anode chamber divided by the diaphragm 8, and electrolyzes the raw water that has been passed through to generate alkaline ionized water and An electrolytic cell 7 for generating acidic ion water, and a controller 15 for controlling an electrolysis voltage applied between the electrodes of the electrolytic cell 7, and one of alkaline ion water and acidic ion water generated in the electrolytic cell 7 Is discharged from the discharge pipe 12, and the other is discharged from the discharge pipe 11.

また、図1において、水栓2を介して水道水等の原水管1と接続された電解水生成装置本体3は、浄水部4、流量検知手段5、カルシウム供給部6、電解槽7、排出管11、吐出管12、電源部14、制御部15および操作表示部16を備えて構成されている。   Moreover, in FIG. 1, the electrolyzed water production | generation apparatus main body 3 connected with the raw | natural water pipes 1, such as a tap water, via the water tap 2 is the water purification part 4, the flow volume detection means 5, the calcium supply part 6, the electrolytic cell 7, discharge | emission A pipe 11, a discharge pipe 12, a power supply unit 14, a control unit 15, and an operation display unit 16 are provided.

ここで、浄水部4は、内部に原水中に含まれる残留塩素やトリハロメタン、カビ臭等を吸着する活性炭および一般細菌や不純物を精度良く取り除く中空糸膜等を備えている。また流量検知手段5は、通水を確認して制御部15に制御指示するものである。またカルシウム供給部6は、グリセロリン酸カルシウムや乳酸カルシウム等のカルシウムイオンを原水中に付与して原水の電気伝導度を高めるものである。   Here, the water purification unit 4 is provided with activated carbon that adsorbs residual chlorine, trihalomethane, mold odor, and the like contained in the raw water, and a hollow fiber membrane that accurately removes general bacteria and impurities. The flow rate detecting means 5 confirms water flow and gives a control instruction to the control unit 15. Moreover, the calcium supply part 6 gives calcium ions, such as calcium glycerophosphate and calcium lactate, to raw water, and raises the electrical conductivity of raw water.

また、電解槽7では、流量検知手段5を経由してきた水を電気分解してアルカリイオン水および酸性イオン水を生成する。図中、8は電解槽7を2分して電解室を形成する隔膜であり、9および10は隔膜8で2分されて形成された各電極室に配置された電極板である。なお、相対的にプラス電圧を印加する電極板を陽極、マイナス電圧を印加する電極板を陰極とすると、電解槽7内に隔膜8で仕切られた陽極室と陰極室とが形成されることとなる。なお、後述のアルカリイオン水生成モード時においては電極板10が陽極となり、電極板9が陰極となる。また、酸性イオン水生成モード時においては電極板9が陽極となり、電極板10が陰極となる。   Moreover, in the electrolytic cell 7, the water which passed through the flow volume detection means 5 is electrolyzed, and alkali ion water and acidic ion water are produced | generated. In the figure, 8 is a diaphragm that divides the electrolytic cell 7 into two to form an electrolytic chamber, and 9 and 10 are electrode plates arranged in each electrode chamber formed by being divided into two by the diaphragm 8. If an electrode plate to which a relatively positive voltage is applied is an anode, and an electrode plate to which a minus voltage is applied is a cathode, an anode chamber and a cathode chamber partitioned by a diaphragm 8 are formed in the electrolytic cell 7. Become. In the alkali ion water generation mode described later, the electrode plate 10 serves as an anode and the electrode plate 9 serves as a cathode. In the acidic ion water generation mode, the electrode plate 9 serves as an anode and the electrode plate 10 serves as a cathode.

また、排出管11は電極板10が挿入された電解室の水(電極板10が陽極の場合は酸性イオン水)を排出し、吐出管12は電極板9が挿入された電解室の水(電極板9が陰極の場合はアルカリイオン水)を吐出する。   The discharge pipe 11 discharges water in the electrolytic chamber in which the electrode plate 10 is inserted (acidic ion water when the electrode plate 10 is an anode), and the discharge pipe 12 discharges water in the electrolytic chamber in which the electrode plate 9 is inserted ( When the electrode plate 9 is a cathode, alkali ion water) is discharged.

また、電源部14は、電源投入用プラグ13からの交流電源を直流電源に変換して制御部15に供給する。また操作表示部16は、利用者がイオン水の水質やpH強度、或いは各種機能の選択設定を行うものであり、操作表示部を介して設定された内容は制御部15に通知される。   Further, the power supply unit 14 converts the AC power supplied from the power-on plug 13 into a DC power and supplies it to the control unit 15. The operation display unit 16 is used by the user to select and set the quality and pH strength of ionic water or various functions, and the contents set through the operation display unit are notified to the control unit 15.

さらに、制御部15は、当該電解水生成装置の動作を制御するが、本実施例では特に、電極板9,10間に流れる電解電流を検出する電解電流検出手段17と、原水を電気分解するために電極板9,10間に電解電圧を印加したときの電解電流検出手段17による正電解電流値と、電極間9,10に印加する電解電圧の極性を反転させたときの電解電流検出手段17による逆電解電流値との差を求める正電解逆電解電流比較手段18と、を備えて、正電解電流値と逆電解電流値の差に基づき電極板9,10の劣化状態を判別する点に特徴がある。   Further, the control unit 15 controls the operation of the electrolyzed water generating apparatus. In this embodiment, in particular, the electrolyzed current detecting means 17 for detecting the electrolyzed current flowing between the electrode plates 9 and 10 and the raw water are electrolyzed. Therefore, the electrolysis current detection means when the positive electrolysis current value by the electrolysis current detection means 17 when the electrolysis voltage is applied between the electrode plates 9 and 10 and the polarity of the electrolysis voltage applied between the electrodes 9 and 10 are reversed. And a positive electrolysis reverse electrolysis current comparison means 18 for obtaining a difference from the reverse electrolysis current value by 17, and determining the deterioration state of the electrode plates 9 and 10 based on the difference between the positive electrolysis current value and the reverse electrolysis current value. There is a feature.

次に、以上の構成を備えた本実施例の電解水生成装置における動作について説明する。利用者は、まず操作表示部16に配してあるモード選択ボタン(図示せず)を操作して、アルカリイオン水生成モード、酸性イオン水生成モードまたは浄水モード等の所望の水質モードを選択し、さらに操作表示部16に配してあるpH調節ボタン(図示せず)を操作して所望のpH値を適宜設定し、その後に水栓2を開いて通水する。   Next, the operation in the electrolyzed water generating apparatus of the present embodiment having the above configuration will be described. The user first operates a mode selection button (not shown) arranged on the operation display unit 16 to select a desired water quality mode such as an alkaline ion water generation mode, an acidic ion water generation mode, or a water purification mode. Further, a desired pH value is appropriately set by operating a pH adjustment button (not shown) arranged on the operation display unit 16, and then the faucet 2 is opened to pass water.

水栓3から導入された原水は、浄水部4により原水中の残留塩素やトリハロメタン、カビ臭、一般細菌等の不純物が取り除かれ、流量検知手段5を経て、カルシウム供給部6によりグリセロリン酸カルシウムや乳酸カルシウム等が溶解されて電気分解容易な水に処理された後、各分岐管を通じて電解槽7内の排出側電解室(電極板10が挿入された電解室)および吐出側電解室(電極板9が挿入された電解室)にそれぞれ供給される。   The raw water introduced from the faucet 3 removes residual chlorine, trihalomethane, musty odor, general bacteria and other impurities in the raw water by the water purification unit 4, passes through the flow rate detection means 5, and is supplied with calcium glycerophosphate and lactic acid by the calcium supply unit 6. After calcium or the like is dissolved and treated with water that is easily electrolyzed, the discharge-side electrolysis chamber (electrolysis chamber in which the electrode plate 10 is inserted) and the discharge-side electrolysis chamber (electrode plate 9) in the electrolytic cell 7 are passed through each branch pipe. Are respectively supplied to the electrolysis chamber in which is inserted.

一方、電源投入用プラグ13からはAC100Vの交流電圧が供給されており、電源部14内のトランスおよび制御用電流電源で電気分解に必要な直流電圧電流を発生させ、制御部15を介して電解槽7内の電極板9,10間に電気分解に必要な電力が給電される。   On the other hand, an AC voltage of 100 V AC is supplied from the power-on plug 13, and a DC voltage current required for electrolysis is generated by a transformer and a control current power source in the power supply unit 14, and electrolysis is performed via the control unit 15. Electric power necessary for electrolysis is fed between the electrode plates 9 and 10 in the tank 7.

制御部15は、通水後に流量検知手段5からの出力信号を読み取り、単位時間当たりに電解水生成装置本体3に流れる流量レベルが一定量を超えたときにその状態が通水中であると判断する。この時、操作表示部16のモード選択ボタン及びpH調節ボタンの操作に応じて既に電気分解条件は設定されており、制御部15はこの条件で電気分解を行わせるように電極板9,10への電力供給を制御する。   The control unit 15 reads the output signal from the flow rate detecting means 5 after passing water, and determines that the state is passing water when the flow level flowing through the electrolyzed water generating device main body 3 exceeds a certain amount per unit time. To do. At this time, the electrolysis conditions have already been set according to the operation of the mode selection button and the pH adjustment button of the operation display unit 16, and the control unit 15 applies the electrode plates 9 and 10 to perform electrolysis under these conditions. To control the power supply.

すなわち、アルカリイオン水生成モード時においては、アルカリ水生成モードにおいては電極板9を陰極、電極板10を陽極として、吐出側電解室から吐出管12を通じてアルカリイオン水を吐出させると共に、排出側電解室から排出管11を通じて酸性イオン水を排出させるように制御し、また、酸性イオン水生成モードにおいては電極板9を陽極、電極板10を陰極として、吐出側電解室から吐出管13を通じて酸性イオン水を吐出させると共に、排出側電解室から排出管11を通じてアルカリイオン水を排出させるように制御する。   That is, in the alkaline ion water generation mode, in the alkaline water generation mode, alkaline ion water is discharged from the discharge side electrolysis chamber through the discharge pipe 12 using the electrode plate 9 as a cathode and the electrode plate 10 as an anode, and discharge side electrolysis is performed. The acidic ion water is controlled to be discharged through the discharge pipe 11 from the chamber. In the acidic ion water generation mode, the acidic ion water is discharged from the discharge side electrolytic chamber through the discharge pipe 13 using the electrode plate 9 as an anode and the electrode plate 10 as a cathode. While discharging water, it controls so that alkali ion water may be discharged from the discharge side electrolysis chamber through the discharge pipe 11.

その後、単位時間当たりに電解水生成装置本体3に流れる流量レベルが一定量を下回ると、この状態を止水と判断し、電解槽7への電力の供給を終了する。このとき、止水直前の水質モードがアルカリイオン水生成モードであった場合には、止水後一定時間、電極板9に相対的にプラス電圧を印加すると共に電極板10にマイナス電圧を印加することにより、電極板9に付着したカルシウム等のスケールを洗浄除去する。また、止水直前の水質モードが酸性イオン水生成モードであった場合には、止水後一定時間、電極板9に相対的にマイナス電圧を印加すると共に電極板10にプラス電圧を印加することにより、電極板10に付着したカルシウム等のスケールを洗浄除去する。   Thereafter, when the flow level flowing through the electrolyzed water generating device main body 3 per unit time falls below a certain amount, this state is determined to be water stop, and the supply of electric power to the electrolyzer 7 is terminated. At this time, when the water quality mode immediately before the water stop is the alkali ion water generation mode, a positive voltage is applied to the electrode plate 9 and a negative voltage is applied to the electrode plate 10 for a certain time after the water stop. As a result, the scale such as calcium adhering to the electrode plate 9 is washed away. In addition, when the water quality mode immediately before the water stop is the acidic ion water generation mode, a negative voltage is applied to the electrode plate 9 and a positive voltage is applied to the electrode plate 10 for a certain time after the water stop. Thus, scales such as calcium adhering to the electrode plate 10 are washed away.

このような動作を繰り返すことにより、電極板9,10が徐々に劣化して行き、イオン水が生成できなくなるため、電極寿命を判断して利用者に知らせる必要があるが、従来のように、単に使用時間や電極洗浄回数での寿命判断では、原水の水質の違い(特に、電気伝導度の違い)等により電解電流が大きく変動するため、寿命の判断を誤る可能性がある。   By repeating such an operation, the electrode plates 9 and 10 gradually deteriorate and ionic water cannot be generated. Therefore, it is necessary to determine the electrode life and inform the user. If the life is determined simply by the usage time or the number of times of electrode cleaning, the electrolytic current largely fluctuates due to differences in the quality of the raw water (particularly, the difference in electrical conductivity), etc., so there is a possibility that the determination of the life will be erroneous.

そこで本実施例では、通常の正電解時(アルカリイオン水生成モード時)の電解電流と、逆電解時(酸性イオン水生成モード時)の電解電流とを逐次比較して、一定以上の差が生じたときに電極寿命と判断するようにしている。これにより、使用場所の違いによる原水の水質の違い(特に、電気伝導度の違い)があっても、また、同一の場所において時間の経過による電気伝導度の変化が生じても誤った判断をすることなく、確実に精度良く電極寿命を判断することができる。   Therefore, in this embodiment, the electrolytic current during normal forward electrolysis (in the alkaline ion water generation mode) and the electrolysis current during reverse electrolysis (in the acidic ion water generation mode) are sequentially compared, and a difference of a certain level or more is found. When this occurs, the life of the electrode is determined. As a result, even if there is a difference in the quality of the raw water due to the difference in the location of use (especially a difference in electrical conductivity), or even if there is a change in electrical conductivity due to the passage of time in the same location, an incorrect judgment is made. Therefore, it is possible to accurately determine the life of the electrode without having to do so.

図2には、本実施例の電解水生成装置において、電極板9の方が電極板10に対して先に寿命となった場合の正電解時(アルカリイオン水生成モード時)の電解電流と、逆電解時(酸性イオン水生成モード時)の電解電流の総電解時間の経過に対する変化を例示している。図2に例示した特性から、逆電解時の陽極(電極板9)の劣化が先に来て、逆電解時の電解電流が相対的に大きく低下していることが分かる。   In FIG. 2, in the electrolyzed water generating apparatus of the present embodiment, the electrolysis current during positive electrolysis (in the alkaline ion water generating mode) when the electrode plate 9 has reached the end of its life first with respect to the electrode plate 10. The change with respect to progress of the total electrolysis time of the electrolysis electric current at the time of reverse electrolysis (at the time of acidic ion water production | generation mode) is illustrated. From the characteristics illustrated in FIG. 2, it can be seen that the deterioration of the anode (electrode plate 9) during reverse electrolysis comes first, and the electrolysis current during reverse electrolysis is relatively reduced.

また、図3には、本実施例の電解水生成装置において、電極板10の方が電極板9に対して先に寿命となった場合の正電解時(アルカリイオン水生成モード時)の電解電流と、逆電解時(酸性イオン水生成モード時)の電解電流の総電解時間の経過に対する変化を例示している。図3に例示した特性から、正電解時の陽極(電極板10)の劣化が先に来て、正電解時の電解電流が相対的に大きく低下していることが分かる。   FIG. 3 shows the electrolysis during positive electrolysis (in the alkaline ion water generation mode) when the electrode plate 10 has reached the end of its life with respect to the electrode plate 9 in the electrolyzed water generating apparatus of this embodiment. The change with respect to progress of the total electrolysis time of the electric current and the electrolysis current at the time of reverse electrolysis (at the time of acidic ion water production mode) is illustrated. From the characteristics illustrated in FIG. 3, it can be seen that the anode (electrode plate 10) during positive electrolysis deteriorates first, and the electrolysis current during positive electrolysis is relatively reduced.

つまり、逆電解時の陽極(電極板9)の劣化と正電解時の陽極(電極板10)の劣化の速さが完全に一致することはなく、何れか一方の電極板が相対的に早く劣化して正電解時(アルカリイオン水生成モード時)の電解電流と、逆電解時(酸性イオン水生成モード時)の電解電流とに差が生じて来ることとなる。   That is, the deterioration rate of the anode (electrode plate 9) during reverse electrolysis and the deterioration rate of the anode (electrode plate 10) during positive electrolysis do not completely coincide with each other, and one of the electrode plates is relatively fast. As a result of the deterioration, there is a difference between the electrolysis current at the time of positive electrolysis (in the alkaline ionic water production mode) and the electrolysis current at the time of reverse electrolysis (in the acidic ionic water production mode).

したがって、正電解時の電解電流と逆電解時の電解電流との差が所定値に達したときに、制御部15は、何れか一方の電極板が電極寿命に至ったと判断して、例えば、操作表示部16の表示画面上に電極寿命に至った旨のメッセージを表示するか、或いは、予め設定されている電極寿命に至った旨を示す警告灯を点灯することにより、使用者に報知する。   Therefore, when the difference between the electrolysis current during forward electrolysis and the electrolysis current during reverse electrolysis reaches a predetermined value, the control unit 15 determines that one of the electrode plates has reached the electrode life, for example, A message indicating that the electrode life has been reached is displayed on the display screen of the operation display unit 16, or a warning lamp indicating that the electrode life has been set is turned on to notify the user. .

以上説明したように、本実施例の電解水生成装置では、隔膜8により分割された陰極室と陽極室に各々電極板9,10が挿入され、通水された原水を電気分解してアルカリイオン水および酸性イオン水を生成する電解槽7と、電解槽7の電極間に印加する電解電圧を制御する制御部15と、を備え、電解槽7内で生成されたアルカリイオン水および酸性イオン水の一方を吐出管12から吐出し、他方を排出管11から排出する電解水生成装置において、制御部15に、電極板9,10間に流れる電解電流を検出する電解電流検出手段17と、原水を電気分解するために電極板9,10間に電解電圧を印加したときの電解電流検出手段17による正電解電流値と、電極間9,10に印加する電解電圧の極性を反転させたときの電解電流検出手段17による逆電解電流値との差を求める正電解逆電解電流比較手段18と、を備えて、正電解電流値と逆電解電流値の差に基づき電極板9,10の劣化状態を判別する。   As described above, in the electrolyzed water generating apparatus of the present embodiment, the electrode plates 9 and 10 are inserted into the cathode chamber and the anode chamber divided by the diaphragm 8, respectively, and the raw water passed through is electrolyzed to generate alkali ions. An electrolytic cell 7 for generating water and acidic ion water, and a controller 15 for controlling an electrolysis voltage applied between the electrodes of the electrolytic cell 7, and alkaline ion water and acidic ion water generated in the electrolytic cell 7. In the electrolyzed water generating apparatus that discharges one of these from the discharge pipe 12 and discharges the other from the discharge pipe 11, the control unit 15 has an electrolysis current detection means 17 that detects an electrolysis current flowing between the electrode plates 9 and 10, and raw water When the electrolysis voltage is applied between the electrode plates 9 and 10 to electrolyze the positive electrolysis current value by the electrolysis current detecting means 17 and the polarity of the electrolysis voltage applied between the electrodes 9 and 10 are reversed. Electrolytic current detection means Positive electrolyte reverse electrolysis current comparison means 18 for obtaining a difference between the reverse electrolysis current value by 7, includes a, determines the deterioration state of the electrode plates 9 and 10 based on the difference of the positive electrolytic current value and the reverse electrolysis current value.

このように、正電解電流値と逆電解電流値の差に基づき電極板9,10の劣化状態を判別するので、使用場所の違いによる原水の水質の違い(特に、電気伝導度の違い)があっても、また、同一の場所において時間の経過による電気伝導度の変化が生じても従来のように誤った判断をすることなく、確実に精度良く電極寿命を判断することができる。   Thus, since the deterioration state of the electrode plates 9 and 10 is determined based on the difference between the positive electrolysis current value and the reverse electrolysis current value, the difference in raw water quality (particularly, the difference in electrical conductivity) due to the difference in use place. Even if there is a change in electrical conductivity due to the passage of time at the same place, it is possible to reliably determine the electrode life without making an erroneous determination as in the prior art.

〔実施例2〕
次に、実施例2に係る電解水生成装置について説明する。本実施例の電解水生成装置の構成は、実施例1(図1参照)と同等であり、各構成要素の詳細な説明を省略する。
[Example 2]
Next, the electrolyzed water generating apparatus according to Example 2 will be described. The configuration of the electrolyzed water generating apparatus of this example is the same as that of Example 1 (see FIG. 1), and detailed description of each component is omitted.

なお、本実施例においても、実施例1と同様に、制御部15において、電極板9,10間に流れる電解電流を検出する電解電流検出手段17と、原水を電気分解するために電極板9,10間に電解電圧を印加したときの電解電流検出手段17による正電解電流値と、電極間9,10に印加する電解電圧の極性を反転させたときの電解電流検出手段17による逆電解電流値との差を求める正電解逆電解電流比較手段18と、を備え、正電解電流値と逆電解電流値の差に基づき電極板9,10の劣化状態を判別するが、本実施例では、電極間に電解電圧を印加してから所定時間が経過したときに検出した正電解電流値と逆電解電流値の差に基づき電極板9,10の劣化状態を判別する点に特徴がある。   Also in the present embodiment, as in the first embodiment, the control unit 15 uses the electrolytic current detecting means 17 for detecting the electrolytic current flowing between the electrode plates 9 and 10 and the electrode plate 9 for electrolyzing the raw water. , 10 when the electrolytic voltage is applied between the positive current value by the electrolytic current detection means 17 and the reverse electrolytic current by the electrolytic current detection means 17 when the polarity of the electrolytic voltage applied between the electrodes 9 and 10 is reversed. And a positive electrolysis reverse electrolysis current comparison means 18 for obtaining a difference from the value, and determining the deterioration state of the electrode plates 9 and 10 based on the difference between the positive electrolysis current value and the reverse electrolysis current value. It is characterized in that the deterioration state of the electrode plates 9 and 10 is determined based on the difference between the positive electrolysis current value and the reverse electrolysis current value detected when a predetermined time has passed since the electrolysis voltage was applied between the electrodes.

図4には、本発明の実施例に係る電解水生成装置において、電極板9,10にカルシウム等のスケールが付着している場合に、電解開始直後の時間経過に対する電解電流の変化を例示している。電極板9または10にカルシウム等のスケールが付着している場合には、図4に示すように、電解開始直後に一時的により大きな電流が流れ、その後徐々に低下して一定の電解電流値に落ち着くといった過渡的変化を持つ。これは、陽極に付着していたカルシウム等のスケールが電解開始と共に急激に溶出し、一時的に大きな電流が流れるためである。   FIG. 4 illustrates the change in the electrolysis current with respect to the time immediately after the start of electrolysis when scales such as calcium adhere to the electrode plates 9 and 10 in the electrolyzed water generating apparatus according to the embodiment of the present invention. ing. When a scale such as calcium adheres to the electrode plate 9 or 10, as shown in FIG. 4, a larger current temporarily flows immediately after the start of electrolysis, and then gradually decreases to a constant electrolytic current value. It has a transitional change that calms down. This is because scales such as calcium adhering to the anode are rapidly eluted with the start of electrolysis, and a large current flows temporarily.

したがって、カルシウム等のスケールの溶出による過渡的な電解電流の変化を除外し、電極間に電解電圧を印加してから所定時間が経過して電解電流が安定状態に至ったときに検出した正電解時の電解電流と逆電解時の電解電流の差に基づき電極寿命を判定するようにすれば、より精度良く電極寿命を判断することができる。   Therefore, the positive electrolysis detected when the electrolysis current reaches a stable state after a predetermined time has elapsed after applying an electrolysis voltage between the electrodes, excluding transient changes in electrolysis current due to elution of scales such as calcium. If the electrode life is determined based on the difference between the electrolytic current during the time and the electrolytic current during the reverse electrolysis, the electrode life can be determined with higher accuracy.

以上説明したように、本実施例の電解水生成装置では、電極間に電解電圧を印加してから所定時間が経過したときに検出した正電解電流値と逆電解電流値の差に基づき電極板9,10の劣化状態を判別するので、電極板9または10からのスケールの溶出による過渡的な電解電流の変化を判別対象から除外して、より精度良く電極寿命を判断し得る電解水生成装置を提供することができる。   As described above, in the electrolyzed water generating apparatus of the present embodiment, the electrode plate is based on the difference between the positive electrolysis current value and the reverse electrolysis current value detected when a predetermined time elapses after the electrolysis voltage is applied between the electrodes. Since the degradation state of 9 and 10 is discriminated, the electrolyzed water generating device that can judge the electrode life more accurately by excluding the transient electrolysis current change due to the elution of the scale from the electrode plate 9 or 10 from the discrimination target. Can be provided.

〔実施例3〕
次に、実施例3に係る電解水生成装置について説明する。本実施例の電解水生成装置の構成は、実施例1(図1参照)と同等であり、各構成要素の詳細な説明を省略する。
Example 3
Next, an electrolyzed water generating apparatus according to Example 3 will be described. The configuration of the electrolyzed water generating apparatus of this example is the same as that of Example 1 (see FIG. 1), and detailed description of each component is omitted.

なお、本実施例においても、実施例1と同様に、制御部15において、電極板9,10間に流れる電解電流を検出する電解電流検出手段17と、原水を電気分解するために電極板9,10間に電解電圧を印加したときの電解電流検出手段17による正電解電流値と、電極間9,10に印加する電解電圧の極性を反転させたときの電解電流検出手段17による逆電解電流値との差を求める正電解逆電解電流比較手段18と、を備え、正電解電流値と逆電解電流値の差に基づき電極板9,10の劣化状態を判別するが、本実施例では、原水の通水が停止しているときに検出した正電解電流値と逆電解電流値の差に基づき電極板9,10の劣化状態を判別する点に特徴がある。   Also in the present embodiment, as in the first embodiment, the control unit 15 uses the electrolytic current detecting means 17 for detecting the electrolytic current flowing between the electrode plates 9 and 10 and the electrode plate 9 for electrolyzing the raw water. , 10 when the electrolytic voltage is applied between the positive current value by the electrolytic current detection means 17 and the reverse electrolytic current by the electrolytic current detection means 17 when the polarity of the electrolytic voltage applied between the electrodes 9 and 10 is reversed. And a positive electrolysis reverse electrolysis current comparison means 18 for obtaining a difference from the value, and determining the deterioration state of the electrode plates 9 and 10 based on the difference between the positive electrolysis current value and the reverse electrolysis current value. It is characterized in that the deterioration state of the electrode plates 9 and 10 is determined based on the difference between the positive electrolysis current value and the reverse electrolysis current value detected when the flow of the raw water is stopped.

図5には、本発明の実施例に係る電解水生成装置において、通水時の流量変化に対する電解電流の変化を例示している。図5に示すように、通水時の流量が少ないほど電解電流が流れ易く相対的に大きな電流が流れ、また流量が多いほど電解電流が流れ難く相対的に小さい電流となることが分かる。また、実際の使用に際しては、水圧の変動や浄水部4の目詰まり等により流量が変動する場合もある。   FIG. 5 illustrates the change in the electrolysis current with respect to the change in the flow rate during water flow in the electrolyzed water generating apparatus according to the embodiment of the present invention. As shown in FIG. 5, it can be seen that the smaller the flow rate during water flow, the easier the electrolysis current flows, and the relatively large current flows, and the greater the flow rate, the less electrolysis current flows and the relatively small current. In actual use, the flow rate may fluctuate due to fluctuations in water pressure or clogging of the water purification unit 4.

しかしながら、本実施例のように、原水の通水が停止しているとき、即ち止水時の電極洗浄時に検出した正電解時の電解電流と逆電解時の電解電流の差に基づき電極寿命を判定するようにすれば、水圧の変動や浄水部4の目詰まり等による流量変動の影響を受けることが無くなり、安定した電解電流の検出により、より精度良く電極寿命を判断することができる。   However, as in this example, when the flow of raw water is stopped, that is, based on the difference between the electrolysis current during positive electrolysis and the electrolysis current during reverse electrolysis detected during electrode cleaning during water stoppage, the electrode life is reduced. If it determines, it will not receive to the influence of the flow volume fluctuation | variation by the fluctuation | variation of a water pressure, the clogging of the water purification part 4, etc., and it can judge an electrode lifetime more accurately by the detection of the stable electrolysis current.

以上説明したように、本実施例の電解水生成装置では、原水の通水が停止しているときに検出した正電解電流値と逆電解電流値の差に基づき電極板9,10の劣化状態を判別するので、使用の度毎に流量が変化する場合でも、より精度良く電極寿命を判断し得る電解水生成装置を提供することができる。   As described above, in the electrolyzed water generating apparatus of the present embodiment, the deterioration state of the electrode plates 9 and 10 based on the difference between the positive electrolysis current value and the reverse electrolysis current value detected when the flow of raw water is stopped. Therefore, it is possible to provide an electrolyzed water generating apparatus that can determine the electrode life more accurately even when the flow rate changes with each use.

本発明の実施例に係る電解水生成装置の構成図である。It is a block diagram of the electrolyzed water generating apparatus which concerns on the Example of this invention. 実施例1の電解水生成装置において電極板9の方が電極板10に対して先に寿命となった場合の正電解時の電解電流と逆電解時の電解電流の総電解時間の経過に対する変化を例示する説明図である。In the electrolyzed water generating apparatus of Example 1, when the electrode plate 9 has reached the end of its life with respect to the electrode plate 10, the change of the electrolysis current during the positive electrolysis and the electrolysis current during the reverse electrolysis with the passage of the total electrolysis time It is explanatory drawing which illustrates this. 実施例1の電解水生成装置において電極板10の方が電極板9に対して先に寿命となった場合の正電解時の電解電流と逆電解時の電解電流の総電解時間の経過に対する変化を例示する説明図である。In the electrolyzed water generating apparatus of Example 1, when the electrode plate 10 reaches the end of its life before the electrode plate 9, changes in the electrolysis current during the positive electrolysis and the electrolysis current during the reverse electrolysis with the passage of the total electrolysis time It is explanatory drawing which illustrates this. 実施例2の電解水生成装置において電極板9,10にスケールが付着している場合に電解開始直後の時間経過に対する電解電流の変化を例示する説明図である。In the electrolyzed water generating apparatus of Example 2, it is explanatory drawing which illustrates the change of the electrolysis electric current with respect to time passage immediately after electrolysis start, when the scale has adhered to the electrode plates 9 and 10. FIG. 実施例3の電解水生成装置において通水時の流量変化に対する電解電流の変化を例示する説明図である。In the electrolyzed water generating apparatus of Example 3, it is explanatory drawing which illustrates the change of the electrolysis current with respect to the flow volume change at the time of water flow. 従来の電解水生成装置における電極寿命の判定処理を説明するフローチャートである。It is a flowchart explaining the determination process of the electrode lifetime in the conventional electrolyzed water generating apparatus.

符号の説明Explanation of symbols

1 原水管
2 水栓
3 電解水生成装置本体
4 浄水部
5 流量検知手段
6 カルシウム供給部
7 電解槽
8 隔膜
9,10 電極板
11 排出管
12 吐出管
13 電源投入用プラグ
14 電源部
15 制御部
16 操作表示部
17 電解電流検出手段
18 正電解逆電解電流比較手段
DESCRIPTION OF SYMBOLS 1 Raw water pipe 2 Water faucet 3 Electrolyzed water production | generation apparatus main body 4 Water purification part 5 Flow rate detection means 6 Calcium supply part 7 Electrolysis tank 8 Diaphragm 9,10 Electrode plate 11 Discharge pipe 12 Discharge pipe 13 Power supply plug 14 Power supply part 15 Control part 16 Operation display section 17 Electrolytic current detection means 18 Positive electrolysis reverse electrolysis current comparison means

Claims (2)

隔膜により分割された陰極室と陽極室に各々電極が挿入され、通水された原水を電気分解してアルカリイオン水および酸性イオン水を生成する電解槽と、前記電解槽の電極間に印加する電解電圧を制御する制御部と、を備え、前記電解槽内で生成されたアルカリイオン水および酸性イオン水の一方を吐出管から吐出し、他方を排出管から排出する電解水生成装置において、
前記制御部は、
前記電極間に流れる電解電流を検出する電解電流検出手段と、
前記原水を電気分解するために前記電極間に電解電圧を印加したときの前記電解電流検出手段による正電解電流値と、前記電極間に印加する電解電圧の極性を反転させたときの前記電解電流検出手段による逆電解電流値との差を求める正電解逆電解電流比較手段と、を有し、
前記原水の通水が停止しているときに検出した前記正電解電流値と前記逆電解電流値の差に基づき前記電極の劣化状態を判別することを特徴とする電解水生成装置。
An electrode is inserted into each of the cathode chamber and the anode chamber divided by the diaphragm, and the raw water passed through is electrolyzed to generate alkaline ionized water and acidic ionized water, and applied between the electrodes of the electrolytic cell. An electrolyzed water generating device that controls the electrolysis voltage, discharges one of alkaline ion water and acidic ion water generated in the electrolytic cell from a discharge pipe, and discharges the other from a discharge pipe.
The controller is
An electrolytic current detecting means for detecting an electrolytic current flowing between the electrodes;
A positive electrolysis current value by the electrolysis current detection means when an electrolysis voltage is applied between the electrodes to electrolyze the raw water, and the electrolysis current when the polarity of the electrolysis voltage applied between the electrodes is reversed Positive electrolysis reverse electrolysis current comparison means for obtaining a difference from the reverse electrolysis current value by the detection means,
An electrolyzed water generating apparatus, wherein the deterioration state of the electrode is determined based on a difference between the positive electrolysis current value and the reverse electrolysis current value detected when water flow of the raw water is stopped .
前記制御部は、前記電極間に電解電圧を印加してから所定時間が経過したときに検出した前記正電解電流値と前記逆電解電流値の差に基づき前記電極の劣化状態を判別することを特徴とする請求項1に記載の電解水生成装置。   The control unit determines a deterioration state of the electrode based on a difference between the positive electrolysis current value and the reverse electrolysis current value detected when a predetermined time has elapsed after applying an electrolytic voltage between the electrodes. The electrolyzed water generating apparatus according to claim 1, wherein
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