JP2000153274A - Electrolytic water generator - Google Patents

Electrolytic water generator

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Publication number
JP2000153274A
JP2000153274A JP10330061A JP33006198A JP2000153274A JP 2000153274 A JP2000153274 A JP 2000153274A JP 10330061 A JP10330061 A JP 10330061A JP 33006198 A JP33006198 A JP 33006198A JP 2000153274 A JP2000153274 A JP 2000153274A
Authority
JP
Japan
Prior art keywords
water
electrolysis
electrodes
electrolytic
electrolytic cell
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.)
Pending
Application number
JP10330061A
Other languages
Japanese (ja)
Inventor
Hiroyuki Seki
裕之 関
Yasuhiro Kumamoto
保弘 熊本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toto Ltd
Original Assignee
Toto Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toto Ltd filed Critical Toto Ltd
Priority to JP10330061A priority Critical patent/JP2000153274A/en
Publication of JP2000153274A publication Critical patent/JP2000153274A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To surely clean electrodes without increasing the cost by judging the state of the electrolytic water remaining between the electrodes based on the detected value of the residual voltage generated between the electrodes while the electrolysis voltage after electrolysis is turned off. SOLUTION: In the electrolytic water generator, when a signal is received from an electrolytic switch or a user detection sensor, a solenoid valve SV1 is opened to start a brine pump 3, city water and A brine stored in a brine tank 2 are supplied to a mixing part 4, the brine is supplied to an electrolytic cell 6 through a filter 5, and electrolysis is conducted. An acidic water contg. hypochlorous acid is discharged and an alkaline water exhausted by a passage switching valve 7. The brine pump and electrolytic cell are turned on or off by a controller 8 based on a signal from a flow sensor 1. The residual voltage generated between the electrodes when the electrolysis is stopped and water supplied is detected, and the water supplying time when electrolysis is stopped is determined from the residual voltage. Consequently, the remaining electrolytic water is surely discharged without increasing the cost.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、電解質を添加した
溶液を電気分解して機能水を生成する電解槽を有する電
解水生成装置に関するものであり、詳しくは、食塩を添
加した上水を電気分解する事で、次亜塩素酸を有する酸
性水を発生させる電解水生成装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolyzed water generating apparatus having an electrolyzer for generating functional water by electrolyzing a solution to which an electrolyte is added. The present invention relates to an electrolyzed water generation device that generates acidic water having hypochlorous acid by being decomposed.

【0002】[0002]

【従来の技術】原水又は電解質を添加した溶液を電気分
解する電解水生成装置(イオン水生成器、酸性水生成器
等)においては、原水又は電解質を添加した溶液を電気
分解する事により生じる酸化還元雰囲気は、電解槽内の
電極に損傷等を与え、電極の耐久性にも影響を与える。
それは、原水又は原水に電解質を添加した溶液を電気分
解することにより生成される酸性水により、電極が酸化
雰囲気にさらされる。また、同様にアルカリ水により電
極へのスケール付着が促進され、電極へ損傷などを与え
るためである。
2. Description of the Related Art In an electrolyzed water generator (ionic water generator, acidic water generator, etc.) for electrolyzing a solution to which raw water or an electrolyte is added, oxidation caused by electrolyzing a solution to which raw water or an electrolyte is added is performed. The reducing atmosphere damages the electrodes in the electrolytic cell and affects the durability of the electrodes.
That is, the electrode is exposed to an oxidizing atmosphere by the acidic water generated by electrolyzing raw water or a solution obtained by adding an electrolyte to raw water. Similarly, the adhesion of scale to the electrode is promoted by the alkaline water, thereby damaging the electrode.

【0003】そこで、従来の電解水生成装置において
は、電気分解後に一定時間又は一定量の無電解通水(電
極へ通電せずに通水のみ行う)を行う事で電解槽内の酸
性水とアルカリ水を排出する様にしている事が多い。
[0003] Therefore, in the conventional electrolyzed water generating apparatus, the electrolyzed water is passed for a certain period of time or for a certain amount of time without electrolysis (only water is passed without energizing the electrodes), thereby reducing the acid water in the electrolyzer. Often, it discharges alkaline water.

【0004】[0004]

【発明が解決しようとする課題】従来のように電気分解
完了後、一定時間又は一定量の無電解通水では、特に流
量が少ない場合においては電解槽内の水の入れ替わりが
悪く電解残留水が完全に排出出来ずに残留する場合があ
り、電極の腐食や損傷等を発生させる等の問題点があっ
た。本発明は、上記課題を解決するためになされたもの
で、本発明の目的は、コストアップせずに確実に電極洗
浄処理を行うシステムを提供することにある。
As in the past, after the completion of electrolysis, if the electroless water is passed for a certain period of time or for a certain amount, particularly in a case where the flow rate is small, the water in the electrolytic cell is not easily replaced and the residual electrolytic water is reduced. In some cases, the electrode may not be completely discharged and may remain, causing problems such as corrosion and damage of the electrode. The present invention has been made to solve the above-described problems, and an object of the present invention is to provide a system for reliably performing an electrode cleaning process without increasing costs.

【0005】[0005]

【課題を解決するための手段および作用・効果】上記目
的を達成するために第1の発明に係る電解水生成装置に
おいては、原水又は原水に電解質を添加した溶液を電極
間に通水して電気分解する電解槽を備えた電解水生成装
置において、電気分解後の電解電圧オフの状態で電極間
に発生する残留電圧の検出値に基づいて、電極間の残留
電解水の状態を判断する事を特徴とする。
In order to achieve the above object, in the electrolyzed water generating apparatus according to the first invention, raw water or a solution obtained by adding an electrolyte to raw water is passed between the electrodes. In an electrolyzed water generator equipped with an electrolyzer for electrolysis, determine the state of the electrolyzed water between the electrodes based on the detected value of the residual voltage generated between the electrodes when the electrolysis voltage is off after electrolysis. It is characterized by.

【0006】このように、電極間残留電圧を電気分解後
に検出する事により、電解槽内にある酸性水、アルカリ
水中のイオン生成物の状態に応じて、電極への通電停止
後に電極間に発生する残留電圧の値が変化する特性を利
用するため、電解残留水の排出状態が確実に判定出来る
様になり、従来の様に電気分解後の電解槽への通水が不
十分にも関わらず、規定した時間又は規定した積算流量
になったことで電解槽への通水処理を完了する方式に比
べ、コストアップせずに確実に電解残留水の排水を行う
事が可能となる。
As described above, by detecting the residual voltage between the electrodes after the electrolysis, the voltage generated between the electrodes after the power supply to the electrodes is stopped according to the state of the ion product in the acidic water or the alkaline water in the electrolytic cell. The characteristic of changing the residual voltage value to be used makes it possible to reliably determine the discharge state of the residual electrolytic water, and despite the insufficient water flow to the electrolytic cell after electrolysis as in the past, In comparison with the method in which the water supply to the electrolytic cell is completed when the specified time or the specified integrated flow rate is reached, it is possible to reliably discharge the residual electrolytic water without increasing the cost.

【0007】また、電気分解後に電解電圧オフの状態で
原水又は原水に電解質を添加した溶液を電解槽に通水す
ると共に、電極間に発生する残留電圧を検出し、この残
留電圧の検出値に基づいて電解槽への通水を停止するよ
うにし、また、電極間に発生する残留電圧が規定電圧以
下になると、電解槽への通水を停止するようにすれば、
電解槽への通水に伴う電解残留水の排出状態を随時検出
して電解槽への通水を停止できるため、電解残留水の排
水に必要最低限な短い時間で排水を完了することができ
る。 更に、従来の課題となっている流量による電解残
留水排出状態への影響についても、電極間に発生する残
留電圧を検出することにより流量変動しても、規定電圧
以下になるまでは、電解槽への通水処理を継続する様に
しておけば確実に電解残留水排出処理を行う事が可能と
なり、電極への損傷が防げ安定した状態での使用が可能
となる。
In addition, after the electrolysis, the raw water or a solution obtained by adding an electrolyte to the raw water is passed through the electrolytic cell in a state where the electrolytic voltage is turned off, and a residual voltage generated between the electrodes is detected. To stop the flow of water to the electrolytic cell based on, if the residual voltage generated between the electrodes is less than the specified voltage, if to stop the flow of water to the electrolytic cell,
Since the state of discharge of the residual electrolytic water accompanying the flow of water into the electrolytic cell can be detected at any time and the flow of water to the electrolytic cell can be stopped, the drainage of the residual electrolytic water can be completed in a minimum required short time. . Furthermore, regarding the influence of the flow rate on the residual water discharge state of the electrolysis, which is a conventional problem, even if the flow rate fluctuates by detecting the residual voltage generated between the electrodes, the electrolytic cell is kept until the voltage falls below the specified voltage. If the water passing treatment is continued, it is possible to reliably carry out the electrolytic residual water discharging treatment, and it is possible to prevent damage to the electrode and to use the electrode in a stable state.

【0008】また、電気分解後の電解電圧オフの状態で
電極間に発生する残留電圧の検出値に応じて、電解電圧
オフの状態で原水又は原水に電解質を添加した溶液を電
解槽に通水する通水時間を演算するようにしても、電解
槽内にある酸性水、アルカリ水中のイオン生成物の状態
に応じて、電極への通電停止後に電極間に発生する残留
電圧の値が変化する特性を利用するため、電解残留水の
排出状態が確実に判定出来る様になり、従来の様に電気
分解後の電解槽への通水が不十分にも関わらず、規定し
た時間又は規定した積算流量になったことで電解槽への
通水処理を完了する方式に比べ、コストアップせずに確
実に電解残留水の排水を行う事が可能となる。
Also, according to the detected value of the residual voltage generated between the electrodes when the electrolysis voltage is off after the electrolysis, raw water or a solution obtained by adding an electrolyte to the raw water is passed through the electrolysis tank with the electrolysis voltage off. The value of the residual voltage generated between the electrodes after the power supply to the electrodes is stopped varies according to the state of the ion product in the acidic water and the alkaline water in the electrolytic cell even if the water supply time to be calculated is calculated. Since the characteristics are used, the discharge state of the residual electrolytic water can be determined with certainty, and the specified time or specified integration can be performed despite insufficient water flow to the electrolytic cell after electrolysis as in the past. As compared with the method in which the flow rate is adjusted to complete the flow of water through the electrolytic cell, it is possible to reliably discharge the residual electrolytic water without increasing the cost.

【0009】なお、電解槽への通水を停止した後、使用
者へ音又は表示又は音声で報知するようにすれば、排水
処理が完了して電解水生成が可能となったことを使用者
が簡単に認識することができる。
If the user is notified by sound, display or voice after stopping the flow of water through the electrolytic cell, the user can be informed that the drainage treatment is completed and the electrolytic water can be generated. Can be easily recognized.

【0010】次に、第2の発明に係る電解水生成装置に
おいては、原水又は原水に電解質を添加した溶液を電気
分解する電解槽を備えた電解水生成装置において、電気
分解後に電解電圧オフの状態で原水又は原水に電解質を
添加した溶液を電解槽に通水させた際の通水流量に基づ
いて、通水時間を演算することを特徴とする。
Next, in an electrolyzed water generating apparatus according to a second aspect of the present invention, an electrolyzed water generating apparatus having an electrolyzer for electrolyzing raw water or a solution obtained by adding an electrolyte to raw water is provided. It is characterized in that the water flow time is calculated based on the flow rate of the raw water or a solution obtained by adding an electrolyte to the raw water in the state when the raw water is passed through the electrolytic cell.

【0011】このように、電気分解後に電解電圧オフの
状態で原水又は原水に電解質を添加した溶液を電解槽に
通水させた際の通水流量に基づいて通水時間を演算する
ことにより、通水流量によって変わる電解残留水の排出
状況に応じた時間だけ排水を行えるため、従来の様に電
気分解後の電解槽への通水が不十分にも関わらず、規定
した時間又は規定した積算流量になったことで電解槽へ
の通水処理を完了する方式に比べ、コストアップせずに
確実に電解残留水の排水を行う事が可能となる。
As described above, by calculating the water flow time based on the flow rate of the raw water or the solution obtained by adding the electrolyte to the raw water in the state where the electrolytic voltage is turned off after the electrolysis, the flow rate is determined based on the flow rate. Drainage can be performed only for the time according to the discharge status of the residual electrolytic water that changes depending on the flow rate of water, so that the water can be supplied to the electrolytic cell after electrolysis as in the past, even if the water flow is insufficient. As compared with the method in which the flow rate is adjusted to complete the flow of water through the electrolytic cell, it is possible to reliably discharge the residual electrolytic water without increasing the cost.

【0012】[0012]

【発明の実施の形態】本発明の一実施例を第1図により
説明する。図1の電解水生成装置は、上水に食塩水を混
合したものを電気分解することによって酸性水(次亜塩
素酸含有水)及びアルカリ水を生成する装置である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described with reference to FIG. The electrolyzed water generating apparatus in FIG. 1 is an apparatus that generates acidic water (hypochlorous acid-containing water) and alkaline water by electrolyzing a mixture of tap water and saline.

【0013】図1の電解水生成装置において、図示しな
い電解スイッチ又は吐水口近傍に設けられた使用者検出
センサーからの信号を受けると、電磁弁SV1が開くと
共に定流量ポンプである食塩水ポンプ3が起動し、上水
及び食塩水タンク2に貯留された食塩水が混合部4に供
給され、所定濃度に調整された食塩水がフィルター5を
経て電解槽6へ供給され電気分解が行われる。そして、
通路切換バルブ7によって、電気分解によって生成され
た次亜塩素酸を含む酸性水は吐水口より手洗用として吐
水され、アルカリ水は吐水洗面器のボール面に排出され
る。なお、これらの食塩水ポンプ3及び電解槽6の動作
は制御装置8によって、電磁弁SV1は、制御装置9に
よって制御されるものである。
In the electrolyzed water generator shown in FIG. 1, when a signal from an electrolysis switch (not shown) or a user detection sensor provided near the water outlet is received, the solenoid valve SV1 is opened and the saline solution pump 3, which is a constant flow pump, is opened. Is activated, the tap water and the salt solution stored in the salt solution tank 2 are supplied to the mixing section 4, and the salt solution adjusted to a predetermined concentration is supplied to the electrolytic cell 6 via the filter 5 to perform electrolysis. And
By the passage switching valve 7, the acidic water containing hypochlorous acid generated by the electrolysis is discharged from the spout for hand washing, and the alkaline water is discharged to the ball surface of the spout basin. The operations of the salt solution pump 3 and the electrolytic cell 6 are controlled by the control device 8, and the solenoid valve SV1 is controlled by the control device 9.

【0014】また、制御装置8は、電気分解に必要な最
低流量が流れているかどうかを流量センサ1からの信号
に基づいて判断し、流量により食塩水ポンプ及び電解槽
への通電ON/OFFを行うものである。
The controller 8 determines whether or not the minimum flow required for electrolysis is flowing based on a signal from the flow sensor 1, and turns ON / OFF current supply to the saline solution pump and the electrolytic cell according to the flow. Is what you do.

【0015】また、電気分解のために電解槽6に通電さ
れるのべ時間が規定した積算時間になると、電極に電圧
を印加しない無電解通水を行う前処理を行った後、電解
槽6に内蔵された電極に電解水生成モード時とは逆極性
の電圧を印加して電極洗浄を行うが、その際には、電磁
弁SV1は閉じ、電磁弁SV2を開き上水を電解槽6へ
供給し、規定時間逆極性の電圧を印加した後、後処理と
して電圧を印加せずに、通水を行う。
When the total time for supplying electricity to the electrolytic cell 6 for electrolysis reaches a specified integration time, a pretreatment for performing electroless water supply without applying a voltage to the electrodes is performed, and then the electrolytic cell 6 A voltage having a polarity opposite to that in the electrolyzed water generation mode is applied to the electrode built in the electrode to perform electrode cleaning. In this case, the solenoid valve SV1 is closed, the solenoid valve SV2 is opened, and water is supplied to the electrolytic cell 6. After supplying and applying a voltage of the opposite polarity for a prescribed time, water is passed without applying a voltage as post-processing.

【0016】第1の発明においては、この電極洗浄の前
処理である電解水生成のための通常極性の電圧印加終了
後における無電解通水時、及び、逆極性の電圧印加後の
後処理である無電解通水時に、電極間に発生する残留電
圧を検出する様にし、その残留電圧の値に応じて無電解
通水時間を決めるようにしている。
In the first invention, the electroless water flow after the application of the normal polarity voltage for the generation of the electrolyzed water, which is the pretreatment of the electrode washing, and the post treatment after the application of the opposite polarity voltage are performed. At the time of certain electroless water flow, the residual voltage generated between the electrodes is detected, and the electroless water flow time is determined according to the value of the residual voltage.

【0017】この電極洗浄処理動作について、フローチ
ャート図2,3,4に基づいて具体例を説明する。図2
は、電解水を生成するための電解フローであり、電解ス
イッチ又は吐水口近傍に設けられた使用者検出センサー
からの信号があると(S100Y)、電磁弁SV1を開
弁し(S101)、水量センサー1が規定流量以上を検
出すると(S103Y)、ポンプをONすると共に電極
への通電を開始する(S104,S105)。
A specific example of this electrode cleaning processing operation will be described with reference to FIGS. FIG.
Is an electrolysis flow for generating electrolyzed water. When there is a signal from an electrolysis switch or a user detection sensor provided near the water outlet (S100Y), the solenoid valve SV1 is opened (S101), and the water flow When the sensor 1 detects a flow rate equal to or more than the specified flow rate (S103Y), the pump is turned on and the power supply to the electrodes is started (S104, S105).

【0018】そして、電極へ通電されて電解水を生成し
ている時間はタイマーによって積算されており、この積
算されている電解生成積算時間が予め設定されている規
定時間を超えたと判断されると(S108Y)、電解水
生成処理の終了を判断するために水量センサー1が規定
流量以上であるかどうかを検出し(S109)、規定流
量以上でなくなったことが検出され、電解水生成処理が
終了したと判断されると図3に示す電極洗浄処理フロー
に移行する。
The time during which the electrodes are energized to generate the electrolyzed water is accumulated by a timer, and when it is determined that the accumulated electrolyzed accumulated time exceeds a predetermined time set in advance. (S108Y), the water flow sensor 1 detects whether or not the flow rate is equal to or more than a specified flow rate in order to determine the end of the electrolyzed water generation processing (S109). If it is determined that the process has been performed, the process proceeds to the electrode cleaning process flow shown in FIG.

【0019】電極洗浄処理においては図3のフローのよ
うに、電極への通電を停止して(S211)、逆電解を
行う前処理として、電解水が全てアルカリ側の通路から
出るように通路切換バルブ7を切り換える(S21
2)。そして、食塩水ポンプ3が駆動すると共に電磁弁
SV2が開弁し(S213,S214)、所定濃度の食
塩水が電解槽6に流れ込む。
In the electrode cleaning process, as shown in the flow of FIG. 3, the power supply to the electrodes is stopped (S211), and as a pre-process for performing reverse electrolysis, the passage is switched so that all of the electrolyzed water exits from the passage on the alkali side. Switching the valve 7 (S21)
2). Then, the saline pump 3 is driven and the solenoid valve SV2 is opened (S213, S214), and the saline having a predetermined concentration flows into the electrolytic cell 6.

【0020】そして、所定濃度の食塩水を無電解水とし
て電解槽6に通水した状態で電極間に発生する残留電圧
を検出し、電解残留水が排出されたことを規定電圧V1
以下になったか否かで判定し(S215)、規定電圧V
1以下になると電解残留水が完全に排出されたと判断
し、電解水生成時とは逆極性の一定電流I2(S21
8)を電極に通電することにより電極洗浄を行う。そし
て、電極への通電を一定時間行うと(S219Y)、電
極への通電のみを停止し(S220)、継続して所定濃
度の食塩水を電解槽6に供給する。
Then, a residual voltage generated between the electrodes is detected in a state where a predetermined concentration of saline solution is passed through the electrolytic cell 6 as electroless water, and it is determined that the residual electrolytic water has been discharged by the specified voltage V1.
It is determined whether or not the voltage has become below (S215).
When it becomes 1 or less, it is determined that the residual electrolytic water has been completely discharged, and the constant current I2 (S21
8) The electrode is cleaned by applying a current to the electrode. Then, when the power supply to the electrodes is performed for a certain period of time (S219Y), only the power supply to the electrodes is stopped (S220), and a predetermined concentration of saline solution is continuously supplied to the electrolytic cell 6.

【0021】また、逆電解にて生成された電解残留水を
排出するため、S220にて電極への通電を停止した後
における電極間に発生する残留電圧を検出し(S22
1)、あらかじめ設定された規定電圧V2より、電極間
残留電圧が小さくなった場合は(S221Y)、電解残
留水排水処理が完了したと判定し、食塩水ポンプ3の駆
動を停止すると共に電磁弁SV2を閉弁し(S222,
S223)、電解槽6と酸性とアルカリ性両側が連通す
るように通路切換バルブ7を切り換えて、必要に応じて
音,表示、音声等で使用者に次回の電解水吐水開始に備
えた状態での待機が完了した旨を報知し、次回の電解水
吐水を行うべく、電解スイッチ又はセンサーの感知を受
付可能な状態で待機する(S227)。
Further, in order to discharge the electrolytic residual water generated by the reverse electrolysis, the residual voltage generated between the electrodes after the power supply to the electrodes is stopped in S220 is detected (S22).
1) When the inter-electrode residual voltage is lower than the preset specified voltage V2 (S221Y), it is determined that the electrolytic residual water drainage processing is completed, the drive of the saline solution pump 3 is stopped, and the solenoid valve is stopped. SV2 is closed (S222,
S223), the passage switching valve 7 is switched so that the electrolytic cell 6 and both the acidic and alkaline sides communicate with each other, and a sound, a display, a sound, or the like is provided to the user as necessary to prepare for the next start of the electrolytic water discharge. Informing that the standby has been completed, the apparatus waits in a state in which sensing by the electrolytic switch or the sensor can be received in order to perform the next electrolytic water spouting (S227).

【0022】なお、規定電圧と電極間残留電圧との判定
処理(S215,S221)が規定時間以内に完了しな
い場合は(S216Y,S225Y)、何らかの異常が
考えられるので、必要に応じて異常があったことを音、
表示等で使用者に報知して動作を停止すことにより(S
217,S226)、異常時において残留電解水の排出
が無制限に継続されてしまうことを防止すると共に、異
常が生じている装置の使用が継続されてしまうことが防
止できる。
If the process of determining the specified voltage and the residual voltage between the electrodes (S215, S221) is not completed within the specified time (S216Y, S225Y), some abnormality may be considered, and there is an abnormality if necessary. Sound that
By notifying the user with a display or the like and stopping the operation (S
217, S226), it is possible to prevent the discharge of the residual electrolyzed water from being continued indefinitely in the event of an abnormality, and to prevent the device in which the abnormality has occurred from being continued to be used.

【0023】また、図4は図3の電極洗浄処理フローを
一部変更したフローであり、この図4に示すように、規
定電圧と電極間残留電圧との判定処理(S315,S3
20)が規定時間以内に完了しない場合は(S316
Y,S324Y)、動作を停止させるのではなく強制的
に次ステップに移行するようにして、次回の電解水吐水
開始に備えた状態で待機する様にし(S325)、残留
電解水の排出を停止し、電解水の生成を行えるようにし
てもよい。なお、その際には、異常があったことを音、
表示等で使用者に報知するような報知手段を設けておく
ことが好ましい。
FIG. 4 is a partially modified flow of the electrode cleaning process shown in FIG. 3. As shown in FIG. 4, the process of determining the specified voltage and the residual voltage between the electrodes (S315, S3)
If step (20) is not completed within the specified time (S316)
Y, S324Y), instead of stopping the operation, forcibly proceed to the next step, so as to stand by in preparation for the next start of electrolytic water spouting (S325), and stop discharging the residual electrolytic water. Then, the electrolyzed water may be generated. At that time, a sound indicates that there was an abnormality,
It is preferable to provide a notifying means for notifying the user by display or the like.

【0024】次に、今回の発明の手段として利用してい
る、電極間残留電圧について概要を説明する。図5に電
極間残留電圧の放電特性のデータを示しているが、この
データより逆方向への通電完了後、通電を停止すると電
極間に残留電圧が残っていることがわかる。ここでは、
示していないが正方向へ通電した場合ももちろん同じ特
性を示す。さらに、通水した場合と通水しない場合とで
電圧の残留特性に差があることがわかる。これは、電解
槽内に残留している電解生成物、電極表面に付着してい
る不純物の状態により違いが出る事がわかった。すなわ
ち電極間残留電圧を検出することで、電解後の排水処理
(電解槽内の電解生成物排出、電極表面の不純物除去)
が完了したか否かを確実に判別出来る様になるものであ
る。
Next, the outline of the residual voltage between electrodes used as the means of the present invention will be described. FIG. 5 shows the data of the discharge characteristics of the residual voltage between the electrodes. It can be seen from this data that the residual voltage remains between the electrodes when the power supply is stopped after the completion of the power supply in the reverse direction. here,
Although not shown, the same characteristics are of course exhibited when current is supplied in the positive direction. Further, it can be seen that there is a difference in residual voltage characteristics between when water is passed and when water is not passed. This was found to differ depending on the state of the electrolytic product remaining in the electrolytic cell and the impurities attached to the electrode surface. In other words, by detecting the residual voltage between the electrodes, wastewater treatment after electrolysis (discharge of electrolytic products in the electrolytic cell, removal of impurities on the electrode surface)
It is possible to reliably determine whether or not is completed.

【0025】次に、別の実施例について図6の電極洗浄
処理フローに基づいて説明する。この実施例は電気分解
後の電解電圧オフの状態で電極間に発生する残留電圧の
検出値に応じて、電解電圧オフの状態で原水又は原水に
電解質を添加した溶液を電解槽に通水する通水時間を演
算するようにしたものであり、具体的にはこの図6のフ
ローに示すように、電極への通電を停止して(S51
1)、逆電解を行う前処理として、電解水が全てアルカ
リ側の通路から出るように通路切換バルブ7を切り換え
る(S512)。そして、食塩水ポンプ3が駆動すると
共に電磁弁SV2が開弁し(S513,S514)、所
定濃度の食塩水が電解槽6に流れ込む。
Next, another embodiment will be described based on the electrode cleaning processing flow of FIG. In this embodiment, raw water or a solution obtained by adding an electrolyte to raw water is passed through an electrolytic cell in a state where the electrolytic voltage is off in accordance with a detected value of a residual voltage generated between the electrodes in a state where the electrolytic voltage is off after the electrolysis. The water supply time is calculated. Specifically, as shown in the flow of FIG. 6, the power supply to the electrodes is stopped (S51).
1) As a pre-process for performing reverse electrolysis, the passage switching valve 7 is switched so that all of the electrolyzed water flows out of the passage on the alkali side (S512). Then, the saline pump 3 is driven and the solenoid valve SV2 is opened (S513, S514), and the saline having a predetermined concentration flows into the electrolytic cell 6.

【0026】そして、所定濃度の食塩水を無電解水とし
て電解槽6に通水した状態で一定時間TAが経過すると
(S515Y)、電極間に発生する残留電圧を検出し
(S516)、その時点の検出電圧Vに対応する排水時
間を図7に示すデータテーブルを用いて演算する(S5
17)。そして、電解残留水が排出されたことをS51
1にて電解電流I1オフ後から(TA+t)sec経過
したか否かで判定し(S518)、(TA+t)になる
と電解残留水が完全に排出されたと判断し、電解水生成
時とは逆極性の一定電流I2を電極に通電することによ
り電極洗浄を行う(S519)。そして、電極への逆極
性の通電を一定時間行うと(S520Y)、電極への通
電のみを停止し(S521)、継続して所定濃度の食塩
水を電解槽6に供給する。
When a predetermined time TA elapses (S515Y) while a predetermined concentration of saline solution is passed through the electrolytic cell 6 as electroless water, a residual voltage generated between the electrodes is detected (S516). Is calculated using the data table shown in FIG. 7 (S5).
17). Then, it is determined in S51 that the residual electrolytic water has been discharged.
It is determined whether (TA + t) sec has elapsed since the electrolysis current I1 was turned off at 1 (S518), and when (TA + t) is reached, it is determined that the residual electrolytic water has been completely discharged, and the polarity is opposite to that at the time of electrolytic water generation. The electrode is cleaned by applying a constant current I2 to the electrode (S519). Then, when the application of the reverse polarity to the electrodes is performed for a certain period of time (S520Y), only the application of the current to the electrodes is stopped (S521), and the salt solution of a predetermined concentration is continuously supplied to the electrolytic cell 6.

【0027】また、逆電解にて生成された電解残留水を
排出するため、S521にて電極への通電を停止した後
に一定時間TBが経過すると(S522Y)、電極間に
発生する残留電圧を検出し(S523)、その時点の検
出電圧Vに対応する排水時間を図7に示すデータテーブ
ルを用いて演算する(S524)。そして、電解残留水
が排出されたことをS521にて電解電流I2オフ後か
ら(TB+t)sec経過したか否かで判定し(S52
5)、(TB+t)になると電解残留水が完全に排出さ
れたと判断し、食塩水ポンプ3の駆動を停止すると共に
電磁弁SV2を閉弁し(S526,S527)、電解槽
6と酸性とアルカリ性両側が連通するように通路切換バ
ルブ7を切り換えて(S528)、必要に応じて音,表
示、音声等で使用者に次回の電解水吐水開始に備えた状
態での待機が完了した旨を報知し、次回の電解水吐水を
行うべく、電解スイッチ又はセンサーの感知を受付可能
な状態で待機する(S529)。
In order to discharge the residual electrolytic water generated by the reverse electrolysis, when a certain time TB elapses after the power supply to the electrodes is stopped in S521 (S522Y), the residual voltage generated between the electrodes is detected. Then, the drainage time corresponding to the detected voltage V at that time is calculated using the data table shown in FIG. 7 (S524). Then, it is determined whether or not the electrolytic residual water has been discharged based on whether (TB + t) sec has elapsed since the electrolytic current I2 was turned off in S521 (S52).
5) When (TB + t) is reached, it is determined that the electrolytic residual water has been completely discharged, the drive of the saline solution pump 3 is stopped, and the solenoid valve SV2 is closed (S526, S527). The passage switching valve 7 is switched so that both sides communicate with each other (S528), and the user is notified by sound, display, sound, or the like, as necessary, that the standby in preparation for the next start of electrolytic water discharge is completed. Then, in order to perform the next electrolyzed water spouting, the apparatus stands by in a state where sensing by the electrolysis switch or the sensor can be received (S529).

【0028】次に、第2の発明について、図8のフロー
チャートに基づき説明する。この第2の発明において
は、前記した第1の発明のように電解電圧オフ後に発生
する残留電圧を利用する方法ではなく、別手段で行うも
のである。
Next, the second invention will be described with reference to the flowchart of FIG. In the second invention, a method using a residual voltage generated after the electrolysis voltage is turned off as in the first invention is performed by another means.

【0029】電極への通電を停止して(S411)、逆
電解を行う前の処理として、電解水が全てアルカリ側の
通路から出るように通路切換バルブ7を切り換える(S
412)。また、電磁弁SV2が開弁すると共に食塩水
ポンプ3が駆動し(S413,S414)、所定濃度の
食塩水が電解槽6に流れ込み、電解槽へ流れている流量
を水量センサー1からの信号に基づき検出する(S41
5)。
After the power supply to the electrodes is stopped (S411), as a process before performing reverse electrolysis, the passage switching valve 7 is switched so that all the electrolyzed water flows out of the passage on the alkali side (S411).
412). In addition, the solenoid valve SV2 is opened and the saline solution pump 3 is driven (S413, S414), the saline solution having a predetermined concentration flows into the electrolytic cell 6, and the flow rate flowing into the electrolytic cell is converted into a signal from the water amount sensor 1. (S41)
5).

【0030】通水流量Qが連続5sec間安定して±
0.1L/minであれば流量が安定したと判断し(S
416Y)、その流量を通水流量として確定する(S4
17)。そして、その流量Qに応じた排水処理時間を決
めるため、図9に示したデータより対応する時間を算出
し、排水時間t(説明では、t2)を設定する(S41
8)。
The flow rate Q is stable for 5 seconds continuously
If the flow rate is 0.1 L / min, it is determined that the flow rate is stable (S
416Y), and the flow rate is determined as the flow rate (S4).
17). Then, in order to determine the drainage processing time according to the flow rate Q, a corresponding time is calculated from the data shown in FIG. 9 and a drainage time t (t2 in the description) is set (S41).
8).

【0031】電流I1オフより設定時間経過(説明で
は、t2)すると(S419)、極性を反転させた電流
I2を通電し(S420)、規定時間経過すると(S4
21)、電極への通電のみを停止し(S422)、継続
して所定濃度の食塩水を電解槽6に電流I2オフより図
7のデータより算出された排水時間tsec間(説明で
は、t2)供給する。tsec間の排水完了後、食塩水ポ
ンプ3の駆動を停止すると共に電磁弁SV2を閉弁し
(S425)、電解槽6と酸性とアルカリ性両側が連通
するように通路切換バルブ7を切り換えて(S42
6)、次回の電解水吐水開始に備えた状態で待機する
(S427)。
When a set time elapses after the current I1 is turned off (t2 in the description) (S419), the current I2 whose polarity is inverted is supplied (S420), and after a specified time elapses (S4).
21) Only the current supply to the electrodes is stopped (S422), and a predetermined concentration of saline is continuously supplied to the electrolytic cell 6 with the current I2 turned off for the drainage time tsec calculated from the data in FIG. 7 (t2 in the description). Supply. After the drainage for tsec is completed, the operation of the saline solution pump 3 is stopped, the solenoid valve SV2 is closed (S425), and the passage switching valve 7 is switched so that both the acidic and alkaline sides communicate with the electrolytic cell 6 (S42).
6) Stand by in a state ready for the next start of electrolytic water spouting (S427).

【図面の簡単な説明】[Brief description of the drawings]

【図1】 電解水生成装置の全体構成図。FIG. 1 is an overall configuration diagram of an electrolyzed water generation device.

【図2】 本発明の一実施形態に係わる電解動作フロ
ー。
FIG. 2 is an electrolysis operation flow according to an embodiment of the present invention.

【図3】 第1の発明に係わる電極洗浄処理フロー。FIG. 3 is an electrode cleaning processing flow according to the first invention.

【図4】 図3の一部を変更した電極洗浄処理フロー。FIG. 4 is a flow chart of an electrode cleaning process in which a part of FIG. 3 is modified.

【図5】 電極残留電圧の放電特性データ。FIG. 5 shows discharge characteristic data of electrode residual voltage.

【図6】 第1の発明の更に別実施形態に係る電極洗浄
処理フロー。
FIG. 6 is an electrode cleaning processing flow according to still another embodiment of the first invention.

【図7】 電極間残留電圧と排水時間設定のデータテー
ブル。
FIG. 7 is a data table of residual voltage between electrodes and drainage time setting.

【図8】 第2の発明に係る電極洗浄処理フロー。FIG. 8 is a flowchart of an electrode cleaning process according to the second invention.

【図9】 通水流量と排水時間設定のデータテーブル。FIG. 9 is a data table of water flow rate and drainage time setting.

【符号の説明】[Explanation of symbols]

SV1,SV2…電磁弁 1…水量センサー 2…食塩水タンク 3…食塩水ポンプ 4…混合部 5…フィルタ 6…電解槽 7…通路切換バルブ 8…制御装置1 9…制御装置2 SV1, SV2 ... solenoid valve 1 ... water amount sensor 2 ... salt solution tank 3 ... salt solution pump 4 ... mixing unit 5 ... filter 6 ... electrolytic cell 7 ... passage switching valve 8 ... control device 1 9 ... control device 2

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 原水又は原水に電解質を添加した溶液を
電極間に通水して電気分解する電解槽を備えた電解水生
成装置において、電気分解後の電解電圧オフの状態で電
極間に発生する残留電圧の検出値に基づいて、電極間の
残留電解水の状態を判断する事を特徴とする電解水生成
装置。
1. An electrolyzed water generating apparatus having an electrolytic cell for electrolysis by passing raw water or a solution obtained by adding an electrolyte to raw water between the electrodes, wherein the electrolysis water is generated between the electrodes in an electrolysis voltage off state after the electrolysis. An electrolyzed water generating apparatus characterized in that a state of electrolyzed water between electrodes is determined based on a detected value of a residual voltage to be generated.
【請求項2】 請求項1記載の電解水生成装置におい
て、電気分解後に電解電圧オフの状態で原水又は原水に
電解質を添加した溶液を電解槽に通水すると共に、電極
間に発生する残留電圧を検出し、この残留電圧の検出値
に基づいて電解槽への通水を停止する事を特徴とする電
解水生成装置。
2. The electrolyzed water generating apparatus according to claim 1, wherein raw water or a solution obtained by adding an electrolyte to raw water is passed through an electrolytic cell in a state where electrolytic voltage is turned off after electrolysis, and a residual voltage generated between electrodes. Wherein the flow of water to the electrolytic cell is stopped based on the detected value of the residual voltage.
【請求項3】 請求項2記載の電解水生成装置におい
て、電極間に発生する残留電圧が規定電圧以下になる
と、電解槽への通水を停止することを特徴とする電解水
生成装置。
3. The electrolyzed water generation apparatus according to claim 2, wherein when the residual voltage generated between the electrodes becomes equal to or lower than a specified voltage, the flow of water to the electrolysis tank is stopped.
【請求項4】 請求項1記載の電解水生成装置におい
て、電気分解後の電解電圧オフの状態で電極間に発生す
る残留電圧の検出値に応じて、電解電圧オフの状態で原
水又は原水に電解質を添加した溶液を電解槽に通水する
通水時間を演算することを特徴とする電解水生成装置。
4. The electrolyzed water generating apparatus according to claim 1, wherein raw water or raw water is supplied with the electrolysis voltage off according to a detected value of a residual voltage generated between the electrodes when the electrolysis voltage is off after electrolysis. An electrolyzed water generating apparatus for calculating a water flow time for flowing a solution to which an electrolyte is added into an electrolytic cell.
【請求項5】 請求項3または請求項4記載の電解水生
成装置において、電解槽への通水を停止した後、使用者
へ音又は表示又は音声で報知することを特徴とする電解
水生成装置。
5. The electrolyzed water generation apparatus according to claim 3, wherein the user is notified by sound, display, or voice after stopping the flow of water to the electrolysis tank. apparatus.
【請求項6】 原水又は原水に電解質を添加した溶液を
電気分解する電解槽を備えた電解水生成装置において、
電気分解後に電解電圧オフの状態で原水又は原水に電解
質を添加した溶液を電解槽に通水させた際の通水流量に
基づいて、通水時間を演算することを特徴とする電解水
生成装置。
6. An electrolyzed water generator comprising an electrolyzer for electrolyzing raw water or a solution obtained by adding an electrolyte to raw water,
An electrolyzed water generating apparatus for calculating a water flow time based on a flow rate of raw water or a solution obtained by adding an electrolyte to raw water in an electrolytic voltage off state after the electrolysis, when the flow rate of the raw water is passed through the electrolytic cell. .
JP10330061A 1998-11-19 1998-11-19 Electrolytic water generator Pending JP2000153274A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10330061A JP2000153274A (en) 1998-11-19 1998-11-19 Electrolytic water generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10330061A JP2000153274A (en) 1998-11-19 1998-11-19 Electrolytic water generator

Publications (1)

Publication Number Publication Date
JP2000153274A true JP2000153274A (en) 2000-06-06

Family

ID=18228353

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2000153274A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003211161A (en) * 2002-01-25 2003-07-29 Kurita Water Ind Ltd Operation method of electrically deionizing apparatus
EP2601143A4 (en) * 2010-08-06 2015-08-05 Miox Corp Electrolytic on-site generator
CN108344772A (en) * 2017-12-29 2018-07-31 宁波欧琳厨具有限公司 A kind of method and system of purification water tank electrolytic strip detection
CN114250830A (en) * 2020-12-10 2022-03-29 佛山市美的清湖净水设备有限公司 Water supply system, control method of water supply system, and readable storage medium

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003211161A (en) * 2002-01-25 2003-07-29 Kurita Water Ind Ltd Operation method of electrically deionizing apparatus
US10400349B2 (en) 2006-11-28 2019-09-03 De Nora Holdings Us, Inc. Electrolytic on-site generator
US11421337B2 (en) 2006-11-28 2022-08-23 De Nora Holdings Us, Inc. Electrolytic on-site generator
EP2601143A4 (en) * 2010-08-06 2015-08-05 Miox Corp Electrolytic on-site generator
EP3257819A1 (en) * 2010-08-06 2017-12-20 Johnson Matthey Public Limited Company Electrolytic on-site generator
CN108344772A (en) * 2017-12-29 2018-07-31 宁波欧琳厨具有限公司 A kind of method and system of purification water tank electrolytic strip detection
CN108344772B (en) * 2017-12-29 2023-07-11 宁波欧琳科技股份有限公司 Method and system for detecting purified water tank electrolyte sheet
CN114250830A (en) * 2020-12-10 2022-03-29 佛山市美的清湖净水设备有限公司 Water supply system, control method of water supply system, and readable storage medium
CN114250830B (en) * 2020-12-10 2023-11-03 佛山市美的清湖净水设备有限公司 Water supply system, control method of water supply system, and readable storage medium

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