JPH0985244A - Electrolytic water preparation device - Google Patents
Electrolytic water preparation deviceInfo
- Publication number
- JPH0985244A JPH0985244A JP26632495A JP26632495A JPH0985244A JP H0985244 A JPH0985244 A JP H0985244A JP 26632495 A JP26632495 A JP 26632495A JP 26632495 A JP26632495 A JP 26632495A JP H0985244 A JPH0985244 A JP H0985244A
- Authority
- JP
- Japan
- Prior art keywords
- water
- cleaning
- anode
- cathode
- cleaning operation
- 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
Links
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、アルカリイオン
水、酸性水を生成するために用いられる電解水生成器に
関する。TECHNICAL FIELD The present invention relates to an electrolyzed water generator used to generate alkaline ionized water and acidic water.
【0002】[0002]
【従来の技術】近時、飲用に供するアルカリイオン水及
び美容または消毒用等に用いられる酸性水を得るために
電解水生成器が利用されている。この電解水生成器の一
例として、水を電気分解してアルカリイオン水、酸性水
を得る電解槽と、該電解槽内に設けた陽極、陰極への印
加電圧の極性を切替える極性切替手段とを有し、陽極、
陰極に、それぞれプラス、マイナス電圧(以下、正規電
圧という。)を印加して水の電気分解を行う電解水生成
器がある。この電解水生成器は、さらに、通水停止(止
水)した状態で、極性を切換えて陽極、陰極にマイナ
ス、プラス電圧(以下、逆電圧という。)を印加し、さ
らに元の極性に戻して正規電圧を印加することにより、
カルシウム等のスケールを陽極、陰極から除去して洗浄
を行う。前述したように、通水停止して溜り水を用いて
行う洗浄動作を、以下、便宜上、止水洗浄動作という。2. Description of the Related Art Recently, electrolyzed water generators have been used to obtain alkaline ionized water for drinking and acidic water used for beauty or disinfection. As an example of this electrolyzed water generator, an electrolytic cell for electrolyzing water to obtain alkaline ionized water and acidic water, and a polarity switching means for switching the polarity of the voltage applied to the anode and cathode provided in the electrolytic cell are provided. Have, anode,
There is an electrolyzed water generator that electrolyzes water by applying a positive voltage and a negative voltage (hereinafter, referred to as a normal voltage) to the cathode. This electrolyzed water generator further switches the polarity and applies negative and positive voltages (hereinafter, referred to as reverse voltage) to the anode and cathode while the water flow is stopped (stopped), and then returns to the original polarity. By applying a normal voltage,
Cleaning is performed by removing scales such as calcium from the anode and cathode. As described above, the cleaning operation performed by stopping the flow of water and using the accumulated water is hereinafter referred to as a water-stop cleaning operation for convenience.
【0003】また、他のタイプとして、通水状態で洗浄
動作を行うようにした電解水生成器もある。このように
通水状態で行う洗浄動作を、以下、便宜上、通水洗浄動
作という。As another type, there is an electrolyzed water generator adapted to perform a cleaning operation in a water-passing state. Hereinafter, the cleaning operation performed in the water-passing state will be referred to as a water-passing cleaning operation for convenience.
【0004】[0004]
【発明が解決しようとする課題】ところで、通水洗浄動
作を行う電解水生成器では、水が陽極、陰極に接触して
流れるので、スケールの除去は迅速に進み、スケール除
去効率が優れたものになるものの、水が多量に消費され
るという問題点を有する。また、止水洗浄動作を行う電
解水生成器では、消費される水の量は少なくて済むもの
の、スケール除去効率は劣ったものになってしまうとい
う問題点を有する。By the way, in the electrolyzed water generator for carrying out the washing operation with water, water flows in contact with the anode and the cathode, so that the scale can be removed quickly and the scale removal efficiency is excellent. However, there is a problem that a large amount of water is consumed. Further, in the electrolyzed water generator that performs the water washing operation, the amount of water consumed can be small, but the scale removal efficiency is inferior.
【0005】本発明は、上記問題点に鑑みてなされたも
ので、水の使用量を抑えて所望の洗浄効率を達成できる
電解水生成器を提供することを目的とする。The present invention has been made in view of the above problems, and an object of the present invention is to provide an electrolyzed water generator which can reduce the amount of water used and achieve a desired cleaning efficiency.
【0006】[0006]
【課題を解決するための手段】本発明は、水を電気分解
してアルカリイオン水、酸性水を得る電解槽と、該電解
槽内に設けた陽極、陰極への印加電圧の極性を切替える
極性切替手段とを有し、前記陽極、陰極に逆極性電圧を
印加して前記電解槽を洗浄する電解水生成器であって、
前記電解槽への通水及びその停止を行う通水調整手段
と、前記電解槽の洗浄に際し、通水及び通水停止をそれ
ぞれ所定回数、交互に行うように前記通水調整手段を制
御する制御手段とを備えたことを特徴とする。The present invention is directed to an electrolyzer for electrolyzing water to obtain alkaline ionized water and acidic water, and a polarity for switching the polarity of voltage applied to an anode and a cathode provided in the electrolyzer. An electrolytic water generator having a switching means, wherein the anode and the cathode are applied with a reverse polarity voltage to wash the electrolytic cell,
Water flow adjusting means for water flow to the electrolyzer and stop thereof, and control for controlling the water flow adjusting means so that water flow and water flow stop are alternately performed a predetermined number of times when cleaning the electrolyzer. And means.
【0007】[0007]
【発明の実施の形態】以下、本発明の実施の第1形態の
電解水生成器を図1ないし図4に基づいて説明する。図
1において、水道蛇口等の水供給源1には、供給管2を
介して電解槽3が接続されており、電解槽3に水Wが供
給されるようになっている。供給管2には、通水又はそ
の停止を切替えて行う電動式の通水調整弁(通水調整手
段)4、通水流量を調整するための通水量調整機構5、
通水流量を検出するフローメータ6が上流側からこの順
に介装されている。なお、通水量調整機構5は省略して
もよい。BEST MODE FOR CARRYING OUT THE INVENTION An electrolyzed water generator according to a first embodiment of the present invention will be described below with reference to FIGS. 1 to 4. In FIG. 1, an electrolytic bath 3 is connected to a water supply source 1 such as a water faucet via a supply pipe 2, and water W is supplied to the electrolytic bath 3. In the supply pipe 2, an electrically operated water flow adjusting valve (water flow adjusting means) 4 for switching water flow or its stop, a water flow rate adjusting mechanism 5 for adjusting a water flow rate,
A flow meter 6 for detecting the water flow rate is provided in this order from the upstream side. The water flow rate adjusting mechanism 5 may be omitted.
【0008】電解槽3は、水を貯留する槽本体7と、槽
本体7内に配置された陽極8、陰極9と、陽極8が配置
された領域M1 と陰極9が配置された領域M2 を分離す
るように配置した隔膜10とから大略構成されている。
隔膜10はイオンを透過可能な材料で構成されている。
なお、この隔膜10は省略してもよい。The electrolytic cell 3 comprises a tank body 7 for storing water, an anode 8 and a cathode 9 arranged in the tank body 7, a region M 1 in which the anode 8 is arranged and a region M in which the cathode 9 is arranged. It is generally composed of a diaphragm 10 arranged so as to separate the two .
The diaphragm 10 is made of a material that is permeable to ions.
The diaphragm 10 may be omitted.
【0009】槽本体7における前記領域M1 ,M2 に臨
む部分のそれぞれには、酸性水吐出管11、アルカリイ
オン水吐出管12が接続されており、電気分解で得られ
た酸性水D、アルカリイオン水Eをそれぞれ吐出するよ
うになっている。An acidic water discharge pipe 11 and an alkaline ionized water discharge pipe 12 are connected to the portions of the tank body 7 which face the regions M 1 and M 2 , respectively, and the acidic water D obtained by electrolysis, The alkaline ionized water E is discharged respectively.
【0010】陽極8、陰極9は、極性変換回路(極性切
替手段)13を介して直流電源14に接続されている。
極性変換回路13は、スイッチ機構(図示省略)を有し
スイッチ機構の作動により陽極8、陰極9に印加する電
圧の極性を切替えるようになっている。直流電源14
は、例えば交流電源(図示省略)と整流回路(図示省
略)とから構成され、整流回路が制御されることにより
オン、オフを含む出力電流の調整を行えるようになって
いる。The anode 8 and the cathode 9 are connected to a DC power supply 14 via a polarity conversion circuit (polarity switching means) 13.
The polarity conversion circuit 13 has a switch mechanism (not shown) and switches the polarity of the voltage applied to the anode 8 and the cathode 9 by the operation of the switch mechanism. DC power supply 14
Is composed of, for example, an AC power supply (not shown) and a rectifier circuit (not shown), and the output current including ON and OFF can be adjusted by controlling the rectifier circuit.
【0011】通水調整弁4、フローメータ6、極性変換
回路13、直流電源14に接続してコントローラ(制御
手段)15が設けられている。コントローラ15は、極
性変換回路13を制御して陽極8、陰極9に正規電圧を
印加して水を電気分解してアルカリイオン水E、酸性水
Dを生成させると共に、図2ないし図4に示す処理を行
って洗浄動作するようにしている。A controller (control means) 15 is provided in connection with the water flow regulating valve 4, the flow meter 6, the polarity conversion circuit 13, and the DC power supply 14. The controller 15 controls the polarity conversion circuit 13 to apply a normal voltage to the anode 8 and the cathode 9 to electrolyze water to generate alkaline ionized water E and acidic water D, and as shown in FIGS. 2 to 4. A cleaning operation is performed by performing processing.
【0012】この洗浄動作について、図2ないし図4に
基づいて説明する。まず、図2に示すように洗浄動作が
開始される(ステップS1)と、直流電源14をオフして
電解槽3への電圧印加を停止する(ステップS2)。This cleaning operation will be described with reference to FIGS. First, as shown in FIG. 2, when the cleaning operation is started (step S1), the DC power supply 14 is turned off and the voltage application to the electrolytic cell 3 is stopped (step S2).
【0013】続いて、陽極8、陰極9に印加される電圧
の極性が切り替わるように極性変換回路13のスイッチ
機構を制御し(ステップS3)、直流電源14をオンし、
極性変換回路13を介して陽極8、陰極9に逆電圧を印
加させる(ステップS4)。なお、極性変換回路13のス
イッチ機構を制御する(ステップS3)前に、直流電源1
4をオフして電解槽3への電圧印加を停止する(ステッ
プS2)ようにしているが、前記ステップS2を省略しても
よい。Subsequently, the switch mechanism of the polarity conversion circuit 13 is controlled so that the polarities of the voltages applied to the anode 8 and the cathode 9 are switched (step S3), the DC power supply 14 is turned on,
Reverse voltage is applied to the anode 8 and the cathode 9 via the polarity conversion circuit 13 (step S4). Before controlling the switch mechanism of the polarity conversion circuit 13 (step S3), the DC power source 1
4 is turned off to stop the voltage application to the electrolytic cell 3 (step S2), but the step S2 may be omitted.
【0014】次に、止水洗浄動作(ステップS5)、通水
洗浄動作(ステップS6)を順次行う。止水洗浄動作は、
図3に示すように実行される。まず、ステップS5の開始
(ステップS21 )と同時に、洗浄時間の計測を開始し、
通水調整弁4を閉じて電解槽3への通水を停止し(ステ
ップS22 )、止水状態で陽極8、陰極9に逆電圧を印加
してスケールの除去を行う。次に、前記洗浄時間が所定
時間に達したか否かの比較結果に基づいて止水洗浄動作
の終了判定を行う(ステップS23 )。ステップS23 で前
記洗浄時間が所定時間T1 に達した場合、YES と判定し
て止水洗浄動作を終了し(ステップS24 )、図2のメイ
ンルーチンに戻って処理を進める。Next, a still water washing operation (step S5) and a water passing washing operation (step S6) are sequentially performed. The still water washing operation is
It is executed as shown in FIG. First, at the same time as starting step S5 (step S21), start measuring the cleaning time,
The water flow regulating valve 4 is closed to stop the water flow to the electrolytic cell 3 (step S22), and the reverse voltage is applied to the anode 8 and the cathode 9 in the water stopped state to remove the scale. Next, it is judged whether or not the water-stopping cleaning operation is completed based on the comparison result of whether or not the cleaning time has reached a predetermined time (step S23). If the cleaning time reaches the predetermined time T 1 in step S23, the determination is YES and the water-stop cleaning operation is ended (step S24), and the process returns to the main routine of FIG.
【0015】ステップS5のサブルーチンに続いて、通水
洗浄動作のサブルーチンを実行する(ステップS6)。通
水洗浄動作は、図4に示すように実行される。まず、ス
テップS6の開始(ステップS31 )と同時に、洗浄時間の
計測を開始し、通水調整弁4を開いて電解槽3への通水
を再開させ(ステップS32 )、通水状態でスケールの除
去を行う。次に、前記洗浄時間が所定時間T2 に達した
か否かの比較結果に基づいて止水洗浄動作の終了判定を
行う(ステップS33 )。ステップS33 で前記洗浄時間が
所定時間T2 に達した場合、YES と判定して通水洗浄動
作を終了し、図2のメインルーチンに戻って処理を進め
る。Subsequent to the sub-routine of step S5, a sub-routine for water flow cleaning operation is executed (step S6). The water washing operation is executed as shown in FIG. First, at the same time as the start of step S6 (step S31), the measurement of the cleaning time is started, and the water flow regulating valve 4 is opened to restart the water flow to the electrolytic cell 3 (step S32). Remove. Next, it is judged whether or not the water-stopping cleaning operation is completed based on the comparison result as to whether or not the cleaning time has reached the predetermined time T 2 (step S33). If the cleaning time reaches the predetermined time T 2 in step S33, it is determined to be YES, the water flow cleaning operation is ended, and the process returns to the main routine of FIG. 2 to proceed.
【0016】ステップS6のサブルーチンに続いて、前記
止水洗浄動作(ステップS5)及び通水洗浄動作(ステッ
プS6)を1回、行ったとして洗浄回数Cを求め、以下、
上記両動作を行う毎に洗浄回数Cを「1」インクリメン
トする(ステップS7)。次に、洗浄回数Cがあらかじめ
設定した基準値Xに達したか否かを判定し(ステップS
8)、洗浄回数Cが基準値Xに達していない場合、NOと
判定して処理をステップS5に戻って行い、止水洗浄動作
(ステップS5)及び通水洗浄動作(ステップS6)をX
回、行う。Subsequent to the subroutine of step S6, the number of washings C is calculated assuming that the above-mentioned water-stopping washing operation (step S5) and water-passage washing operation (step S6) have been performed once.
Each time both of the above operations are performed, the cleaning number C is incremented by "1" (step S7). Next, it is determined whether or not the number of times of cleaning C has reached a preset reference value X (step S
8) If the number of times of cleaning C has not reached the reference value X, it is determined to be NO and the process returns to step S5 to perform the still water cleaning operation (step S5) and the passing water cleaning operation (step S6).
Do it once.
【0017】洗浄回数Cが基準値Xに達してステップS8
でYES と判定すると、直流電源14をオフして電解槽3
への電圧印加を停止する(ステップS9)。次に、陽極
8、陰極9に印加される電圧の極性が切り替わるように
極性変換回路13のスイッチ機構を制御し、かつ直流電
源14をオンし、極性変換回路13を介して陽極8、陰
極9に正規電圧を印加させ、通常の電解処理を行う状態
に復帰させ(ステップS10 )、洗浄処理を終了する(ス
テップS11 )。なお、ステップS9で、直流電源14をオ
フして電解槽3への電圧印加を停止するようにしている
が、このステップS9を省略してもよい。When the cleaning frequency C reaches the reference value X, step S8
If YES is determined, the DC power supply 14 is turned off and the electrolytic cell 3
The voltage application to is stopped (step S9). Next, the switch mechanism of the polarity conversion circuit 13 is controlled so that the polarities of the voltages applied to the anode 8 and the cathode 9 are switched, the DC power supply 14 is turned on, and the anode 8 and the cathode 9 are connected via the polarity conversion circuit 13. A normal voltage is applied to the device to restore the normal electrolytic treatment (step S10), and the cleaning process ends (step S11). In step S9, the DC power supply 14 is turned off to stop the voltage application to the electrolytic cell 3, but step S9 may be omitted.
【0018】上述した電解水生成器では、コントローラ
15が極性変換回路13を制御して、陽極8、陰極9に
逆電圧を印加した状態で、所定時間にわたる通水及び通
水停止を所定回数、交互に行う。このため、通水洗浄動
作を行うことに伴うスケールの除去の迅速化、ひいては
スケール除去効率の向上、及び止水洗浄動作を行うこと
に伴う水消費の抑制を共に果たすことが可能となるの
で、水の消費を抑えた状態で所望のスケール除去効率を
得ることができ、ひいてはランニングコストを低下させ
ることができる。In the above-described electrolyzed water generator, the controller 15 controls the polarity conversion circuit 13 to apply a reverse voltage to the anode 8 and the cathode 9, and water is stopped and water is stopped for a predetermined number of times. Alternate. For this reason, it is possible to speed up scale removal associated with the water-washing operation, improve scale removal efficiency, and reduce water consumption associated with the water-stopping cleaning operation. The desired scale removal efficiency can be obtained with the water consumption suppressed, and the running cost can be reduced.
【0019】なお、上記実施の形態では、図3のステッ
プS23 で、洗浄時間が所定時間T1に達したか否かに基
づいて止水洗浄動作の終了判定を行う場合を例にした
が、これに代えて、電解積算時間、電解積算電流値、又
は電解積算電力値を計測し、この計測データに基づいて
止水洗浄動作の終了判定を行うようにしてもよい。ま
た、図4では通水洗浄動作の終了を洗浄時間に基づいて
行っているが、上述したのと同様に、電解積算時間、電
解積算電流値、又は電解積算電力値に基づいて行うよう
にしてもよい。In the above embodiment, the case where the termination judgment of the water-stopping cleaning operation is determined based on whether or not the cleaning time has reached the predetermined time T 1 in step S23 of FIG. Instead of this, the electrolysis accumulated time, the electrolysis accumulated current value, or the electrolysis accumulated power value may be measured, and the termination determination of the water-stop cleaning operation may be performed based on the measured data. Further, in FIG. 4, the water passing cleaning operation is ended based on the cleaning time, but similarly to the above, it is performed based on the electrolysis integrated time, the electrolysis integrated current value, or the electrolysis integrated power value. Good.
【0020】また、上記実施の形態では、図2のステッ
プS8で、洗浄回数Cがあらかじめ設定した基準値Xに達
したか否かに基づいて洗浄動作の終了判定を行う場合を
例にしたが、これに代えて、電解積算時間、電解積算電
流値、又は電解積算電力値を計測し、各データに基づい
て洗浄動作の終了判定を行うようにしてもよい。Further, in the above embodiment, the case where the end of the cleaning operation is determined based on whether or not the number of times of cleaning C has reached the preset reference value X in step S8 of FIG. 2 has been described as an example. Instead of this, the electrolysis accumulated time, the electrolysis accumulated current value, or the electrolysis accumulated power value may be measured, and the end of the cleaning operation may be determined based on each data.
【0021】次に、本発明の実施の第2形態の電解水生
成器を図5ないし図7に基づいて説明する。この電解水
生成器は、図1ないし図4に示すものに比して、アルカ
リイオン水吐出管12に分岐して第1補助管20を接続
し、第1補助管20にコントローラ15Aに制御されて
開閉する常閉の大気開放制御弁21を介装したこと、供
給管2のフローメータ6の下流側部分に分岐して第2補
助管22を接続し、第2補助管22にコントローラ15
Aに制御されて開閉する常閉の排水制御弁23を介装し
たこと、及びコントローラ15に代えて、図2のステッ
プS5のサブルーチンに代わるステップS5A (止水洗浄動
作)のサブルーチンを有するコントローラ15Aを有す
ることが異なっており、他の部分、部材は、図1ないし
図4に示すものと同等であり、同等の部分、部材につい
ての説明は適宜、省略する。Next, an electrolyzed water generator according to a second embodiment of the present invention will be described with reference to FIGS. This electrolyzed water generator is branched to the alkaline ionized water discharge pipe 12 and connected to the first auxiliary pipe 20 as compared with those shown in FIGS. 1 to 4, and the first auxiliary pipe 20 is controlled by the controller 15A. A normally closed atmosphere opening control valve 21 that opens and closes is installed, and the second auxiliary pipe 22 is connected to the second auxiliary pipe 22 by branching to the downstream side portion of the flow meter 6 of the supply pipe 2.
A controller 15A having a normally closed drainage control valve 23 which is controlled by A and has a subroutine of step S5A (stop water cleaning operation) instead of the subroutine of step S5 of FIG. 2 in place of the controller 15. The other parts and members are the same as those shown in FIGS. 1 to 4, and the description of the same parts and members will be appropriately omitted.
【0022】コントローラ15Aは、ステップS5A で
は、図7に示すように、まず、その処理開始(ステップ
S51 )と同時に、洗浄時間の計測を開始し、通水調整弁
4を閉じて電解槽3への通水を停止し(ステップS52
)、止水状態で陽極8、陰極9に逆電圧を印加してス
ケールの除去を行う。次に、前記洗浄時間が所定時間T
3 に達したか否かの比較結果に基づいて止水洗浄動作の
終了判定を行う(ステップS53 )。なお、本実施の形態
では、図7のステップS53 で、洗浄時間が所定時間T3
に達したか否かに基づいて止水洗浄動作の終了判定を行
う場合を例にしたが、これに代えて、電解積算時間、電
解積算電流値、又は電解積算電力値を計測し、この計測
データに基づいて止水洗浄動作の終了判定を行うように
してもよい。In step S5A, the controller 15A first starts its processing (step S5A), as shown in FIG.
At the same time, the measurement of the cleaning time is started, the water flow adjusting valve 4 is closed, and the water flow to the electrolytic cell 3 is stopped (step S52).
), The scale is removed by applying a reverse voltage to the anode 8 and the cathode 9 in a water-stopped state. Next, the cleaning time is a predetermined time T
Based on the comparison result of whether it has reached 3 , it is judged whether or not the water-stopping cleaning operation is completed (step S53). In the present embodiment, in step S53 of FIG. 7, the cleaning time is the predetermined time T 3
Although the example in which the termination judgment of the water-stopping cleaning operation is performed based on whether or not the value has reached has been taken as an example, instead of this, the electrolytic accumulated time, the electrolytic accumulated current value, or the electrolytic accumulated electric power value is measured, and It may be possible to determine the end of the water-stop cleaning operation based on the data.
【0023】ステップS53 で前記洗浄時間が所定時間T
3 に達した場合、YES と判定して、ステップS54 に進ん
で大気開放制御弁21を開ける。次に、排水制御弁23
を開け、ヘッド圧により電解槽3内部の水を、第2補助
管22から排出させる(ステップS56 )と共に、排水時
間の計測を開始する。続いて、排水時間があらかじめ設
定した時間TB に達したか否かを判定する(ステップS5
7 )。ステップS57 でYES と判定すると、大気開放制御
弁21を閉じて大気開放を終了する(ステップS57 )。
続いて排水制御弁23を閉じてヘッド圧による排水を終
了し(ステップS58 )、止水洗浄処理を終了し(ステッ
プS59 )、図6のメインルーチンのステップS6に進み、
以下、図2で説明したのと同様に処理を進める。In step S53, the cleaning time is a predetermined time T
When it reaches 3 , it is determined to be YES, and the process proceeds to step S54 to open the atmosphere opening control valve 21. Next, the drainage control valve 23
Then, the water inside the electrolytic cell 3 is discharged from the second auxiliary pipe 22 by the head pressure (step S56), and the measurement of the drainage time is started. Subsequently, it is determined whether or not the drainage time has reached a preset time T B (step S5
7). If YES is determined in step S57, the atmosphere release control valve 21 is closed and the atmosphere release is completed (step S57).
Then, the drainage control valve 23 is closed to terminate the drainage by the head pressure (step S58), the water-stop cleaning process is terminated (step S59), and the process proceeds to step S6 of the main routine of FIG.
Hereinafter, the process proceeds in the same manner as described with reference to FIG.
【0024】この電解水生成器も、上述した電解水生成
器と同様に、陽極8、陰極9に逆電圧を印加した状態
で、所定時間にわたる通水及び通水停止を所定回数、交
互に行う。このため、通水洗浄動作を行うことに伴うス
ケールの除去の迅速化、ひいてはスケール除去効率の向
上、及び止水洗浄動作を行うことに伴う水消費の抑制を
共に果たすことが可能となるので、水の消費を抑えた状
態で所望のスケール除去効率を得ることができ、ひいて
はランニングコストを低下させることができる。This electrolyzed water generator, like the electrolyzed water generator described above, alternately conducts water supply and water supply stop for a predetermined time a predetermined number of times with a reverse voltage applied to the anode 8 and the cathode 9. . For this reason, it is possible to speed up scale removal associated with the water-washing operation, improve scale removal efficiency, and reduce water consumption associated with the water-stopping cleaning operation. The desired scale removal efficiency can be obtained with the water consumption suppressed, and the running cost can be reduced.
【0025】また、この電解水生成器は、止水洗浄動作
時に電解槽3内の水を排出しており、洗浄動作に伴い陽
極8、陰極9から除去されるスケールを電解槽3から確
実に流出するので、次の電圧印加の際に当該スケールが
陽極8又は陰極9に付着されることがなく、その分だ
け、スケール除去効率を向上できることになる。This electrolyzed water generator discharges the water in the electrolytic cell 3 during the water-stopping cleaning operation, so that the scale removed from the anode 8 and the cathode 9 by the cleaning operation is surely removed from the electrolytic cell 3. Since it flows out, the scale is not attached to the anode 8 or the cathode 9 when the next voltage is applied, and the scale removal efficiency can be improved accordingly.
【0026】[0026]
【発明の効果】本発明は、制御手段が極性切替手段を制
御して、陽極、陰極に逆電圧を印加した状態で、所定時
間にわたる通水及び通水停止を所定回数、交互に行うの
で、通水洗浄動作を行うことに伴うスケールの除去の迅
速化、ひいてはスケール除去効率の向上、及び止水洗浄
動作を行うことに伴う水消費の抑制を共に果たすことが
可能となり、水の消費を抑えた状態で所望のスケール除
去効率を得ることができ、ひいてはランニングコストを
低下させることができる。According to the present invention, the control means controls the polarity switching means to alternately pass water and stop water for a predetermined number of times in a state in which a reverse voltage is applied to the anode and the cathode. It is possible to speed up scale removal associated with the water-through cleaning operation, improve scale removal efficiency, and reduce water consumption associated with the water-stopping cleaning operation. In this state, the desired scale removal efficiency can be obtained, and the running cost can be reduced.
【図1】本発明の実施の第1形態の電解水生成器を模式
的に示す系統図である。FIG. 1 is a system diagram schematically showing an electrolyzed water generator according to a first embodiment of the present invention.
【図2】同電解水生成器のコントローラの処理内容の一
部を示すフローチャートである。FIG. 2 is a flowchart showing a part of processing contents of a controller of the electrolyzed water generator.
【図3】図2のステップS5のサブルーチンの内容を示す
フローチャートである。FIG. 3 is a flowchart showing the contents of a subroutine of step S5 of FIG.
【図4】図2のステップS6のサブルーチンの内容を示す
フローチャートである。4 is a flowchart showing the contents of a subroutine of step S6 of FIG.
【図5】本発明の実施の第2形態の電解水生成器を模式
的に示す系統図である。FIG. 5 is a system diagram schematically showing an electrolyzed water generator according to a second embodiment of the present invention.
【図6】同電解水生成器のコントローラの処理内容の一
部を示すフローチャートである。FIG. 6 is a flowchart showing a part of processing contents of a controller of the electrolyzed water generator.
【図7】図6のステップS5A のサブルーチンの内容を示
すフローチャートである。FIG. 7 is a flowchart showing the contents of a subroutine of step S5A of FIG.
3 電解槽 4 通水調整弁(通水調整手段) 8 陽極 9 陰極 13 極性変換回路(極性切替手段) 15 コントローラ(制御手段) 3 Electrolyzer 4 Water flow adjusting valve (water flow adjusting means) 8 Anode 9 Cathode 13 Polarity conversion circuit (polarity switching means) 15 Controller (controlling means)
Claims (1)
性水を得る電解槽と、該電解槽内に設けた陽極、陰極へ
の印加電圧の極性を切替える極性切替手段とを有し、前
記陽極、陰極に逆極性電圧を印加して前記電解槽を洗浄
する電解水生成器であって、前記電解槽への通水及びそ
の停止を行う通水調整手段と、前記電解槽の洗浄に際
し、通水及び通水停止をそれぞれ所定回数、交互に行う
ように前記通水調整手段を制御する制御手段とを備えた
ことを特徴とする電解水生成器。1. An electrolytic cell for electrolyzing water to obtain alkaline ionized water and acidic water, and a polarity switching means for switching the polarity of voltage applied to an anode and a cathode provided in the electrolytic cell, Anode, an electrolyzed water generator for applying a reverse polarity voltage to the cathode to wash the electrolytic cell, water flow adjusting means for passing water to the electrolytic cell and stopping it, and in cleaning the electrolytic cell, An electrolyzed water generator, comprising: control means for controlling the water flow adjusting means so that water flow and water flow stop are alternately performed a predetermined number of times.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26632495A JPH0985244A (en) | 1995-09-20 | 1995-09-20 | Electrolytic water preparation device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26632495A JPH0985244A (en) | 1995-09-20 | 1995-09-20 | Electrolytic water preparation device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0985244A true JPH0985244A (en) | 1997-03-31 |
Family
ID=17429348
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP26632495A Pending JPH0985244A (en) | 1995-09-20 | 1995-09-20 | Electrolytic water preparation device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0985244A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007107686A (en) * | 2005-10-17 | 2007-04-26 | Hoshizaki Electric Co Ltd | Drive control method of flow regulating valve |
JP2009028598A (en) * | 2007-07-25 | 2009-02-12 | Panasonic Electric Works Co Ltd | Electrolyzed water generating apparatus |
JP2011167671A (en) * | 2010-02-22 | 2011-09-01 | Hoshizaki Electric Co Ltd | Electrolytic operation method for electrolyzed water generator of diaphragm electrolysis type |
JP6209256B1 (en) * | 2016-07-21 | 2017-10-04 | 株式会社日本トリム | Electrolyzed water generator |
JP6209254B1 (en) * | 2016-07-21 | 2017-10-04 | 株式会社日本トリム | Electrolyzed water generator |
JP6209255B1 (en) * | 2016-07-21 | 2017-10-04 | 株式会社日本トリム | Electrolyzed water generator |
-
1995
- 1995-09-20 JP JP26632495A patent/JPH0985244A/en active Pending
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007107686A (en) * | 2005-10-17 | 2007-04-26 | Hoshizaki Electric Co Ltd | Drive control method of flow regulating valve |
JP2009028598A (en) * | 2007-07-25 | 2009-02-12 | Panasonic Electric Works Co Ltd | Electrolyzed water generating apparatus |
JP2011167671A (en) * | 2010-02-22 | 2011-09-01 | Hoshizaki Electric Co Ltd | Electrolytic operation method for electrolyzed water generator of diaphragm electrolysis type |
JP6209256B1 (en) * | 2016-07-21 | 2017-10-04 | 株式会社日本トリム | Electrolyzed water generator |
JP6209254B1 (en) * | 2016-07-21 | 2017-10-04 | 株式会社日本トリム | Electrolyzed water generator |
JP6209255B1 (en) * | 2016-07-21 | 2017-10-04 | 株式会社日本トリム | Electrolyzed water generator |
JP2018012075A (en) * | 2016-07-21 | 2018-01-25 | 株式会社日本トリム | Electrolytic water generator |
WO2018016577A1 (en) * | 2016-07-21 | 2018-01-25 | 株式会社日本トリム | Electrolyzed water generation device |
WO2018016575A1 (en) * | 2016-07-21 | 2018-01-25 | 株式会社日本トリム | Electrolyzed water generation device |
WO2018016576A1 (en) * | 2016-07-21 | 2018-01-25 | 株式会社日本トリム | Electrolyzed water generation device |
JP2018012077A (en) * | 2016-07-21 | 2018-01-25 | 株式会社日本トリム | Electrolytic water generator |
JP2018012076A (en) * | 2016-07-21 | 2018-01-25 | 株式会社日本トリム | Electrolytic water generator |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPH0985244A (en) | Electrolytic water preparation device | |
JP3694107B2 (en) | Electrolyzed water generator | |
JP3653135B2 (en) | Electrolyzed water generator | |
JP3991484B2 (en) | Control method of alkaline ionized water apparatus | |
JP2810247B2 (en) | Continuous electrolytic ionized water generator | |
JP3587289B2 (en) | Ion water generator | |
JP3426344B2 (en) | Electrolyzed water generator | |
JPH06335681A (en) | Alkaline ion water regulator | |
JP3736051B2 (en) | Ion water conditioner | |
JP3887882B2 (en) | Alkaline ion water conditioner | |
JPH06178980A (en) | Electrolytically ionized water forming device | |
JP3601011B2 (en) | Electrolyzed water generator | |
JPH10235353A (en) | Electrolytic water making apparatus | |
JP3479372B2 (en) | Electrolyzed water generator | |
JP2001353488A (en) | Device for producing electrolytic water | |
JPH06328072A (en) | Electrolyzed ionic water generation device | |
JP2001113277A (en) | Continuous electrolytic water maker | |
JPH08206657A (en) | Continuous electrolytic ion water making apparatus and removal of scale in electrolytic chamber thereof | |
JPH0847688A (en) | Electrolytic water generator | |
JP2003251347A (en) | Ionized water generating device | |
JPH0866683A (en) | Electrolyzed water forming device | |
JP2001070939A (en) | Alkali ion water conditioner | |
JPH07136659A (en) | Continuous electrolytic water making apparatus | |
JPH07204650A (en) | Electrolytic water generation device | |
JPH0985246A (en) | Electrolytic water preparation device |