JPH07328625A - Electrolytic ionized water generator - Google Patents

Electrolytic ionized water generator

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Publication number
JPH07328625A
JPH07328625A JP12040994A JP12040994A JPH07328625A JP H07328625 A JPH07328625 A JP H07328625A JP 12040994 A JP12040994 A JP 12040994A JP 12040994 A JP12040994 A JP 12040994A JP H07328625 A JPH07328625 A JP H07328625A
Authority
JP
Japan
Prior art keywords
electrode
water
reverse
storage tank
electric pump
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.)
Granted
Application number
JP12040994A
Other languages
Japanese (ja)
Other versions
JP3426341B2 (en
Inventor
Yasuo Hara
安夫 原
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.)
Hoshizaki Electric Co Ltd
Original Assignee
Hoshizaki Electric Co 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 Hoshizaki Electric Co Ltd filed Critical Hoshizaki Electric Co Ltd
Priority to JP12040994A priority Critical patent/JP3426341B2/en
Publication of JPH07328625A publication Critical patent/JPH07328625A/en
Application granted granted Critical
Publication of JP3426341B2 publication Critical patent/JP3426341B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To sufficiently conduct reverse-voltage cleaning by providing an operation control means by which an electrode switching means is switched to a reverse-voltage state for a set time almost simultaneously with the stoppage of a motor-driven pump when the operation is suspended. CONSTITUTION:When a stop switch 102 is operated, the motor-driven pump P1, electrode-switching device 110 and power source circuit 120 are controlled by a controller 100. An OFF signal is received by the circuit 120 from the controller 100 to reduce the DC voltage between the minus electrode and plus electrode to zero, and the pump P1 is driven for a set time. Immediately after the stoppage of the pump P1, raw water is supplied to discharge pipes 37 and 38 from an electrolytic cell 30, or the raw water is transiently stopped. The water remaining in the discharge pipes 37 and 38 then flows back to a water storage tank 10. Accordingly, the electrodes 32 and 33 are entirely immersed in water for a sufficient time even without increasing the water remaining in the discharge pipes 37 and 38, the reverse-voltage cleaning time is prolonged, and reverse-voltage cleaning is sufficiently performed.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、水または食塩水等の原
水を電気分解して酸性イオン水とアルカリ性イオン水を
生成する電解イオン水生成装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolytic ionic water producing apparatus for electrolyzing raw water such as water or saline to produce acidic ionic water and alkaline ionic water.

【0002】[0002]

【従来の技術】この種の装置においては、両電極に印加
される直流電圧の正逆を切り換えないで正電状態にて長
時間使用していると、マイナス側電極の表面にカルシウ
ム,ナトリウム等が層状に付着して通電率を低下させ、
所望の電解イオン水が得られなくなる。かかる問題は、
例えば実公平2−7675号公報に示されているよう
に、電解槽への給水停止と略同時に両電極に印加される
直流電圧の正逆を切り換えて逆電状態とし、電解槽の残
水が排出されるまで逆電洗浄する(上記した付着物を電
極から剥離させる)ことにより解消することができる。
2. Description of the Related Art In this type of device, when the DC voltage applied to both electrodes is not switched between positive and negative and is used for a long period of time in a positive electric state, calcium, sodium, etc. will appear on the surface of the negative electrode. Adhere to each other in a layered form to reduce the electrical conductivity,
The desired electrolytic ionized water cannot be obtained. The problem is
For example, as shown in Japanese Utility Model Publication No. 2-7675, when the water supply to the electrolytic cell is stopped, the direct current voltage applied to both electrodes is switched between normal and reverse to make a reverse voltage state, and the residual water in the electrolytic cell is It can be eliminated by performing reverse electrolysis cleaning (peeling the above-mentioned deposits from the electrodes) until the discharge.

【0003】[0003]

【発明が解決しようとする課題】ところで、上記した公
報の電解イオン水生成装置においては、電解槽への給水
停止から電解槽の残水が排出されるまでの時間に逆電洗
浄が行われるものであり、残水の排水に伴って電極が順
次露呈するため、逆電洗浄を十分に行うことができな
い。本発明は、上記した問題に対処すべくなされたもの
であり、その目的は逆電洗浄を十分に行い得る電解イオ
ン水生成装置を提供することにある。
By the way, in the electrolytic ionized water generator of the above-mentioned publication, the reverse electrolysis cleaning is performed during the time from the stop of the water supply to the electrolytic cell until the residual water in the electrolytic cell is discharged. Therefore, since the electrodes are sequentially exposed as the residual water is drained, it is impossible to sufficiently perform the reverse electrolysis cleaning. The present invention has been made to address the above-mentioned problems, and an object thereof is to provide an electrolytic ionized water production apparatus capable of sufficiently performing reverse electrolysis cleaning.

【0004】[0004]

【課題を解決するための手段】上記した目的を達成する
ために、本発明においては、当該電解イオン水生成装置
を、水または食塩水等の原水を貯溜する貯水タンクと、
第1及び第2の電極を内部に対向配設するとともにこれ
ら両電極間に隔膜を配設して各電極を収容する第1及び
第2の電極室を形成しこれら両電極室に原水が流入・流
出するようにした電解槽と、前記貯水タンクの原水を接
続管を通して前記電解槽の両電極室に圧送する電動ポン
プと、前記貯水タンクの水面より上方に立ち上がる立上
部と大気に連通可能な開口を有して前記第1の電極室に
接続され同電極室にて生成された電解イオン水を排出す
る第1排出管と、前記貯水タンクの水面より上方に立ち
上がる立上部と大気に連通可能な開口を有して前記第2
の電極室に接続され同電極室にて生成された電解イオン
水を排出する第2排出管と、電源回路から前記両電極に
印加される直流電圧の正逆を切り換える電極切換手段
と、前記電動ポンプ及び前記電極切換手段の作動を制御
して、生成運転時に前記電動ポンプを駆動状態に維持す
るとともに前記電極切換手段を正電状態に維持し、また
運転停止時に前記電動ポンプを停止させると略同時に前
記電極切換手段を逆電状態に切り換えて設定時間維持す
る作動制御手段を備える構成とした。
In order to achieve the above-mentioned object, in the present invention, the electrolytic ionized water generator is provided with a water storage tank for storing raw water such as water or saline.
The first and second electrodes are arranged to face each other and a diaphragm is provided between the electrodes to form first and second electrode chambers for accommodating the electrodes, and raw water flows into these electrode chambers. An outflowing electrolyzer, an electric pump for pumping raw water of the water storage tank to both electrode chambers of the electrolyzer through a connecting pipe, and a rising portion rising above the water surface of the water storage tank and the atmosphere. A first discharge pipe that has an opening and is connected to the first electrode chamber and discharges electrolytic ionized water generated in the first electrode chamber; and a rising portion that rises above the water surface of the water storage tank and the atmosphere can be communicated with each other. The second with a large opening
Second discharge pipe connected to the electrode chamber for discharging electrolyzed ionized water generated in the electrode chamber, electrode switching means for switching between direct and reverse of the DC voltage applied to the both electrodes from the power supply circuit, and the electric motor. The operation of the pump and the electrode switching means is controlled to maintain the electric pump in the driving state during the generating operation, maintain the electrode switching means in the positive electric state, and stop the electric pump when the operation is stopped. At the same time, an operation control means for switching the electrode switching means to a reverse electric state and maintaining the set time is provided.

【0005】[0005]

【発明の作用・効果】本発明による電解イオン水生成装
置においては、生成運転時、作動制御手段によって、電
動ポンプが駆動状態に維持され、また電極切換手段が正
電状態に維持されるため、貯水タンク内の原水が接続管
を通して電解槽の両電極室に供給されるとともに、電解
槽の両電極には電源回路からの直流電圧が正電状態にて
印加される。このため、電動ポンプによって貯水タンク
から電解槽の両電極室に供給された原水は電解槽内で電
気分解されて、プラス側電極の電極室からは水素イオン
が増加した酸性イオン水が生成排出され、またマイナス
側電極の電極室からは水酸イオンが増加したアルカリ性
イオン水が生成排出され、各イオン水が各排出管を通し
て所望の箇所に導かれる。
In the electrolytic ionized water producing apparatus according to the present invention, the electric control pump is maintained in the driven state by the operation control means and the electrode switching means is maintained in the positive electric state during the production operation. Raw water in the water storage tank is supplied to both electrode chambers of the electrolytic cell through a connecting pipe, and a DC voltage from a power supply circuit is applied to both electrodes of the electrolytic cell in a positive electric state. For this reason, the raw water supplied from the water storage tank to both electrode chambers of the electrolytic cell is electrolyzed in the electrolytic cell, and acidic ionized water with increased hydrogen ions is generated and discharged from the electrode chamber of the positive electrode. Also, alkaline ionized water with increased hydroxide ions is generated and discharged from the electrode chamber of the negative electrode, and each ionized water is guided to a desired location through each discharge pipe.

【0006】また、運転停止時には、作動制御手段によ
って電動ポンプが停止されると略同時に電極切換手段が
逆電状態に切り換えられて設定時間維持され、電動ポン
プの停止直後から設定時間逆電洗浄が行われる。ところ
で、電動ポンプの停止直後には、電解槽から各排出管に
水が供給される又は水が一時的に止まる作用が得られ、
その後に各排出管内に残留する水が貯水タンクに向けて
逆流する作用が得られる。したがって、両排出管内に残
留する水を多くしなくても、両電極全体が水没した状態
の時間を十分に確保することができ、逆電洗浄時間を長
くすることができて逆電洗浄を十分に行うことができる
とともに、両排出管を小容量化することができて当該装
置を小型化することが可能である。
Further, when the electric pump is stopped by the operation control means at the time of operation stop, the electrode switching means is switched to the reverse charge state and maintained for the set time substantially at the same time, and the reverse charge cleaning is performed immediately after the stop of the electric pump for the set time. Done. By the way, immediately after the stop of the electric pump, water is supplied from the electrolyzer to each discharge pipe, or the water is temporarily stopped,
After that, the effect that the water remaining in each discharge pipe flows backward toward the water storage tank is obtained. Therefore, even if the amount of water remaining in both drain pipes is not increased, it is possible to secure a sufficient period of time in which both electrodes are submerged, and it is possible to lengthen the reverse electrode cleaning time and to perform the reverse electrode cleaning sufficiently. In addition, the capacity of both discharge pipes can be reduced, and the device can be downsized.

【0007】[0007]

【実施例】以下に、本発明の一実施例を図面に基づいて
説明する。図1は本発明による電解イオン水生成装置を
示していて、この電解イオン水生成装置は原水(水道
水)を所要量貯える貯水タンク10を備えている。貯水
タンク10は、制御装置100に接続された水位センサ
11(上限水位と下限水位を検出するもの)を内部に備
えていて、この水位センサ11からの信号により給水管
19(水道に接続されている)に設けた電磁開閉弁V1
が開閉されて貯水タンク10内の水位が所定の範囲に維
持されるように構成されている。また、貯水タンク10
にはオーバーフローパイプ12が設けられるとともに、
電解槽30の両流入口31a,31bに分岐して接続さ
れる接続管13が取付けられており、接続管13には制
御装置100によって作動を制御される電動ポンプP1
と手動で調整可能な流量調整バルブV2,V3がそれぞ
れ介装されていて、略同量の原水が接続管13を通して
電解槽30の両流入口31a,31bに供給されるよう
に構成されている。
An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 shows an electrolytic ion water generator according to the present invention, which is provided with a water storage tank 10 for storing a required amount of raw water (tap water). The water storage tank 10 is internally equipped with a water level sensor 11 (which detects the upper limit water level and the lower limit water level) connected to the control device 100, and a signal from the water level sensor 11 causes a water supply pipe 19 (connected to the water supply). Solenoid valve V1 installed in
Is opened and closed to maintain the water level in the water storage tank 10 within a predetermined range. Also, the water storage tank 10
Is provided with an overflow pipe 12,
A connection pipe 13 that is branched and connected to both inlets 31 a and 31 b of the electrolytic cell 30 is attached, and the connection pipe 13 has an electric pump P 1 whose operation is controlled by the control device 100.
And manually adjustable flow rate adjusting valves V2 and V3 are respectively provided, and it is configured that approximately the same amount of raw water is supplied to both inflow ports 31a and 31b of the electrolytic cell 30 through the connecting pipe 13. .

【0008】電解槽30は、一対の流入口31a,31
bを下部に有しかつ一対の流出口31c,31dを上部
に有する樹脂製(過熱によって変形する)の槽本体31
と、この槽本体31内に対向配設した一対の電極32,
33と、これら両電極32,33間に配設されて各電極
32,33を収容する各電極室34,35を形成する隔
膜36によって構成されていて、各電極32,33とし
てはチタン基材の表面に白金メッキ或いは白金イリジウ
ムを焼成してなるものが採用され、また左方の電極室3
4には流入口31aと流出口31cが連通し、右方の電
極室35には流入口31bと流出口31dが連通してい
る。
The electrolytic cell 30 includes a pair of inlets 31a, 31
A tank body 31 made of resin (deformed by overheating) having b in the lower part and a pair of outlets 31c, 31d in the upper part
And a pair of electrodes 32 disposed opposite to each other in the tank body 31,
33 and a diaphragm 36 disposed between the electrodes 32, 33 to form electrode chambers 34, 35 for accommodating the electrodes 32, 33. The electrodes 32, 33 are made of titanium base material. The surface of the electrode is platinum plated or platinum iridium is fired, and the electrode chamber 3 on the left side is used.
4, an inflow port 31a and an outflow port 31c communicate with each other, and an electrode chamber 35 on the right side communicates with an inflow port 31b and an outflow port 31d.

【0009】また、各流出口31c,31dには各排出
管37,38が接続されていて、各排出管37,38は
上方に立ち上がる立上部37a,38aを有して図2に
て示したように各イオン水の使用場所であるシンクTの
配設位置まで延出配管されており、各排出管37,38
の立上部37a,38aには貯溜タンク部37b,38
bが形成されている。また、各排出管37,38の中間
部位に設けた各立上部37a,38aは上端が各通気細
管37c,38cを通して大気に連通開口していて、各
排出管37,38の流出端部がシンクT内にて水没して
も、不具合(例えば、当該装置の停止時におけるサイフ
ォン現象の発生)が生じないように機能する。また、本
実施例においては、電解槽30の底部が貯水タンク10
に設けたオーバーフローパイプ12の上端より所定量L
1上方に位置するように配置されていて、図示のごとき
当該装置の停止時には各排出管37,38および電解槽
30内に水が溜まらない構成となっている。
Further, discharge pipes 37, 38 are connected to the respective outlets 31c, 31d, and the discharge pipes 37, 38 have rising portions 37a, 38a rising upward, which are shown in FIG. As described above, the pipes are extended to the position where the sink T where each ion water is used is provided, and the discharge pipes 37, 38 are provided.
The storage tanks 37b, 38 are provided on the rising portions 37a, 38a of the
b is formed. Further, the respective rising portions 37a, 38a provided at the intermediate portions of the discharge pipes 37, 38 have upper ends communicating with the atmosphere through the ventilation thin pipes 37c, 38c, and the outlet ends of the discharge pipes 37, 38 are sinks. Even if the device is submerged in T, the function does not occur (for example, a siphon phenomenon occurs when the device is stopped). Further, in this embodiment, the bottom of the electrolytic cell 30 is the water storage tank 10.
A predetermined amount L from the upper end of the overflow pipe 12 provided in
1 is arranged so as to be located above 1, and water is not accumulated in the discharge pipes 37, 38 and the electrolytic cell 30 when the apparatus is stopped as shown in the figure.

【0010】各電極32,33は電極切換器110を介
して電源回路120に接続されている。電極切換器11
0は、制御装置100からの信号に応じて両電極32,
33に印加される直流電圧の正逆を切り換えるものであ
り、図1の仮想線で示した状態にて制御装置100から
正電信号を受けたとき実線の状態に切り替わって電源回
路120のマイナス電極を電極32に接続するとともに
プラス電極を電極33に接続し、また図1の実線で示し
た状態にて制御装置100から逆電信号を受けたときに
仮想線の状態に切り替わって電源回路120のマイナス
電極を電極33に接続するとともにプラス電極を電極3
2に接続するようになっている。電源回路120は交流
電圧を所定値の直流電圧に変換するものであり、制御装
置100からOFF信号を受けたときにはマイナス電極
とプラス電極間の直流電圧がゼロとなるように、また制
御装置100からON信号を受けたときにはマイナス電
極とプラス電極間に所定値の直流電圧が印加されるよう
になっている。
The electrodes 32 and 33 are connected to a power supply circuit 120 via an electrode switch 110. Electrode changer 11
0 represents both electrodes 32, in response to a signal from the control device 100.
The DC voltage applied to the switch 33 is switched between normal and reverse, and when a positive electric signal is received from the control device 100 in the state shown by the virtual line in FIG. Is connected to the electrode 32, the positive electrode is connected to the electrode 33, and when a reverse signal is received from the control device 100 in the state shown by the solid line in FIG. The negative electrode is connected to the electrode 33 and the positive electrode is connected to the electrode 3.
It is designed to connect to 2. The power supply circuit 120 is for converting an AC voltage into a DC voltage having a predetermined value, so that when the OFF signal is received from the control device 100, the DC voltage between the negative electrode and the positive electrode becomes zero, and from the control device 100. When receiving the ON signal, a DC voltage having a predetermined value is applied between the minus electrode and the plus electrode.

【0011】制御装置100は、図2に示したようにシ
ンクTに近接して配設した起動スイッチ101と停止ス
イッチ102の各操作と水位センサ11からの信号に基
づいて電磁開閉弁V1、電動ポンプP1、電極切換器1
10、電源回路120等の作動を制御するようになって
おり、各スイッチ101,102を操作することにより
以下に説明する作動が得られるようになっている。
As shown in FIG. 2, the control device 100 controls the electromagnetic on-off valve V1 and the electric valve based on the signals from the water level sensor 11 and the respective operations of the start switch 101 and the stop switch 102 arranged near the sink T. Pump P1, electrode changer 1
10, the operation of the power supply circuit 120 and the like is controlled, and the operation described below can be obtained by operating the switches 101 and 102.

【0012】上記のように構成した本実施例において
は、起動スイッチ101が操作されると、制御装置10
0が電動ポンプP1と電極切換器110と電源回路12
0を制御し、電動ポンプP1が駆動されるとともに、電
極切換器110が実線状態に維持され電源回路120が
ON信号を受けてマイナス電極とプラス電極間に所定値
Aの直流電圧が印加されて電解槽30の両電極32,3
3に正電状態にて直流電圧が印加される(図3のT1参
照)。
In the present embodiment configured as described above, when the start switch 101 is operated, the control device 10 is activated.
0 is the electric pump P1, the electrode switching device 110, and the power supply circuit 12
0, the electric pump P1 is driven, the electrode switch 110 is maintained in a solid line state, the power supply circuit 120 receives an ON signal, and a DC voltage of a predetermined value A is applied between the negative electrode and the positive electrode. Both electrodes 32, 3 of the electrolytic cell 30
A DC voltage is applied to 3 in the positive electric state (see T1 in FIG. 3).

【0013】このため、貯水タンク10内の原水が電動
ポンプP1と接続管13と各流量調整バルブV2,V3
を通して電解槽30の各電極室34,35に供給される
とともに、原水が電解槽30内で電気分解されて、マイ
ナス側電極32の電極室34からは水酸イオンが増加し
た所定PHのアルカリ性イオン水が排出管37を通して
シンクTに導かれ、またプラス側電極33の電極室35
からは水素イオンが増加した所定PHの酸性イオン水が
排出管38を通してシンクTに導かれる。
Therefore, the raw water in the water storage tank 10 is the electric pump P1, the connecting pipe 13, and the flow rate adjusting valves V2 and V3.
Is supplied to each of the electrode chambers 34, 35 of the electrolytic bath 30 and the raw water is electrolyzed in the electrolytic bath 30, and hydroxide ions are increased from the electrode chamber 34 of the negative side electrode 32 to a predetermined pH of alkaline ions. Water is guided to the sink T through the drain pipe 37, and the electrode chamber 35 of the positive electrode 33
From the above, acidic ionized water having a predetermined PH with increased hydrogen ions is introduced to the sink T through the discharge pipe 38.

【0014】上記した正電圧印加によるイオン水生成作
動により貯水タンク10内の水位が設定範囲の下限に達
すると、水位センサ11が作動しこれに基づいて制御装
置100から電磁開閉弁V1に開弁信号が出力され、電
磁開閉弁V1が開かれて水道水が給水管19を通して貯
水タンク10に補給される。かかる水道水の補給により
貯水タンク10内の水位が設定範囲の上限に達すると、
水位センサ11が作動しこれに基づいて制御装置100
から電磁開閉弁V1に閉弁信号が出力され、電磁開閉弁
V1が閉じられ水道水の補給が止まる。
When the water level in the water storage tank 10 reaches the lower limit of the set range due to the ion water generation operation by applying the above-mentioned positive voltage, the water level sensor 11 is activated, and based on this, the control device 100 opens the electromagnetic on-off valve V1. A signal is output, the electromagnetic opening / closing valve V1 is opened, and tap water is supplied to the water storage tank 10 through the water supply pipe 19. When the water level in the water storage tank 10 reaches the upper limit of the set range due to the supply of tap water,
The water level sensor 11 operates, and based on this, the control device 100
Outputs a valve closing signal to the electromagnetic opening / closing valve V1, the electromagnetic opening / closing valve V1 is closed, and the supply of tap water is stopped.

【0015】また、停止スイッチ102が操作される
と、これに基づいて制御装置100が電動ポンプP1と
電極切換器110と電源回路120を制御し、電源回路
120が制御装置100からOFF信号を受けてマイナ
ス電極とプラス電極間の直流電圧をゼロとした状態で電
動ポンプP1の駆動が設定時間(図3のT2〜T3)維
持され、設定時間後に電動ポンプP1が停止されると略
同時に、電極切換器110にて電極の接続が実線状態か
ら仮想線状態に切り換えられて電解槽30の電極32が
電源回路120のプラス電極に接続されるとともに電極
33がマイナス電極に接続され、また電源回路120が
制御装置100からON信号を受けてマイナス電極とプ
ラス電極間に所定値の直流電圧が印加されて、電解槽3
0の両電極32,33に逆電状態にて直流電圧が印加さ
れる(図3のT3参照)。この状態は制御装置100に
より電動ポンプP1の停止後設定時間(図3のT3〜T
4)維持され、その設定時間の経過時には電源回路12
0が制御装置100からOFF信号を受けてマイナス電
極とプラス電極間の直流電圧をゼロとした後、制御装置
100により電極切換器110にて電極の接続が仮想線
状態から実線状態に切り換えられて電解槽30の電極3
2が電源回路120のマイナス電極に接続されるととも
に電極33がプラス電極に接続される。
When the stop switch 102 is operated, the control device 100 controls the electric pump P1, the electrode switching device 110 and the power supply circuit 120 based on the operation, and the power supply circuit 120 receives an OFF signal from the control device 100. The driving of the electric pump P1 is maintained for a set time (T2 to T3 in FIG. 3) in a state where the DC voltage between the negative electrode and the positive electrode is set to zero, and substantially at the same time when the electric pump P1 is stopped after the set time. The switch 110 switches the electrode connection from the solid line state to the phantom line state to connect the electrode 32 of the electrolytic cell 30 to the positive electrode of the power supply circuit 120 and the electrode 33 to the negative electrode of the power supply circuit 120. Receives an ON signal from the control device 100, a DC voltage having a predetermined value is applied between the negative electrode and the positive electrode, and the electrolytic cell 3
A DC voltage is applied to both electrodes 32 and 33 of 0 in a reverse electric state (see T3 in FIG. 3). This state is set by the control device 100 after the electric pump P1 is stopped for a set time (T3 to T in FIG. 3).
4) The power supply circuit 12 is maintained and, when the set time has elapsed,
0 receives the OFF signal from the control device 100 to set the DC voltage between the negative electrode and the positive electrode to zero, and then the control device 100 switches the electrode connection from the virtual line state to the solid line state by the electrode switch 110. Electrode 3 of electrolyzer 30
2 is connected to the negative electrode of the power supply circuit 120, and the electrode 33 is connected to the positive electrode.

【0016】このため、停止スイッチ102が操作され
た時点(図3のT2)から電動ポンプP1が停止される
時点(図3のT3)までに電解槽30と各排出管37,
38内には未電解の原水が圧送され、また電動ポンプP
1の停止直後から各排出管37,38に残留する残留水
が各電極室34,35に落差により自動的に供給される
逆流状態の途中までの設定時間(図3のT3〜T4)
に、いわゆる逆電洗浄が行われ電極32からカルシウ
ム,ナトリウム等付着物が剥離されて逆流水とともに接
続管13と電動ポンプP1を通して貯水タンク10に向
けて電解槽30外に排出される。
Therefore, from the time when the stop switch 102 is operated (T2 in FIG. 3) to the time when the electric pump P1 is stopped (T3 in FIG. 3), the electrolytic cell 30 and each discharge pipe 37,
The unelectrolyzed raw water is pumped into the inside of 38, and the electric pump P
The set time from immediately after the stop of No. 1 to the middle of the backflow state in which the residual water remaining in the discharge pipes 37 and 38 is automatically supplied to the electrode chambers 34 and 35 by the drop (T3 to T4 in FIG. 3).
Then, so-called reverse electrolysis cleaning is performed to remove deposits such as calcium and sodium from the electrode 32, and the backflow water is discharged to the outside of the electrolytic cell 30 toward the water storage tank 10 through the connecting pipe 13 and the electric pump P1.

【0017】ところで、電動ポンプP1の停止直後に
は、電解槽30から各排出管37,38に原水が供給さ
れる又は原水が一時的に止まる作用が得られ、その後に
各排出管37,38内に残留する水が貯水タンク10に
向けて逆流する作用が得られる。したがって、両排出管
37,38内に残留する水を多くしなくても、両電極3
2,33全体が水没した状態の時間を十分に確保するこ
とができ、逆電洗浄時間を長くすることができて逆電洗
浄を十分に行うことができるとともに、両排出管37,
38を小容量化する(例えば、立上部37a,38aを
短くしたり、貯溜タンク部37b,38bを無くしたり
する)ことができて当該装置を小型化することが可能で
ある。
Immediately after the electric pump P1 is stopped, the raw water is supplied from the electrolytic cell 30 to the discharge pipes 37, 38 or the raw water is temporarily stopped, and then the discharge pipes 37, 38 are stopped. The effect that the water remaining inside flows back toward the water storage tank 10 is obtained. Therefore, even if the amount of water remaining in both drain pipes 37 and 38 is not increased, both electrodes 3
It is possible to secure a sufficient time for the whole 2, 33 to be submerged in water, it is possible to lengthen the reverse electrolysis cleaning time, and it is possible to sufficiently perform the reverse electrolysis cleaning.
The capacity of 38 can be reduced (for example, the rising portions 37a and 38a can be shortened or the storage tank portions 37b and 38b can be eliminated), and the device can be downsized.

【0018】また、上記した逆電洗浄は未電解の原水内
での電解反応によって行われるものであるため、水素イ
オンが電極33に吸着されて生じる水素脆性反応が抑制
され、同電極33の損傷が抑制される。また、本実施例
においては、上記した逆電洗浄によって生成される酸性
イオン水とアルカリ性イオン水が接続管13の基部にて
合流混合して中性化され、これが電動ポンプP1を介し
て貯水タンク10に戻る。したがって、電動ポンプP1
に耐触性は要求されず、安価な一般的な電動ポンプを使
用することができる。
Further, since the above-mentioned reverse electrolysis cleaning is performed by the electrolytic reaction in the unelectrolyzed raw water, the hydrogen brittle reaction caused by the adsorption of hydrogen ions on the electrode 33 is suppressed, and the electrode 33 is damaged. Is suppressed. Further, in this embodiment, the acidic ionized water and the alkaline ionized water produced by the above-mentioned reverse electrolysis are merged and mixed at the base of the connecting pipe 13 to be neutralized, and this is neutralized via the electric pump P1. Return to 10. Therefore, the electric pump P1
No touch resistance is required, and an inexpensive general electric pump can be used.

【0019】なお、上記した設定時間(逆電洗浄時間)
は、通常、数秒〜数十秒の範囲内で適宜設定されてい
て、本実施例においては逆流水を生じさせる水面が各貯
溜タンク部37b,38bの下端に下降した時点(逆流
状態の途中)で逆電洗浄が終了するように設定されてい
る。このため、本実施例においては、逆流終了時に接続
管13の両分岐部には未電解の水が溜まることとなり、
次回の生成運転開始時に電極32が水素イオンと反応す
ることがない。また、本実施例においては、電解槽30
の底部が貯水タンク10に設けたオーバーフローパイプ
12の上端より所定量L1上方に位置するように配置さ
れているため、逆流の終了時に電解槽30内から水を完
全に排出することができて、仮に逆電洗浄終了後に電解
槽30の両電極が逆電状態にて印加されることがあって
も、両電極32,33間を電流は流れず止水状態での通
電による電解槽30の過熱は発生しない。
The above set time (reverse electrolysis cleaning time)
Is usually set appropriately within a range of several seconds to several tens of seconds, and in the present embodiment, the time when the water surface that causes backflow water descends to the lower end of each storage tank part 37b, 38b (during the backflow state). Is set so that the back electrolysis cleaning ends. Therefore, in this embodiment, unelectrolyzed water accumulates in both branch portions of the connecting pipe 13 at the end of the backflow,
The electrode 32 does not react with hydrogen ions at the start of the next generation operation. In addition, in this embodiment, the electrolytic cell 30 is used.
Since the bottom part of the above is arranged so as to be located above the upper end of the overflow pipe 12 provided in the water storage tank 10 by a predetermined amount L1, water can be completely discharged from the electrolytic cell 30 at the end of the backflow, Even if both electrodes of the electrolytic cell 30 are applied in a reversely charged state after the completion of reverse electrolysis cleaning, no current flows between the electrodes 32 and 33, and the electrolytic cell 30 is overheated due to energization in a water-stopped state. Does not occur.

【0020】上記実施例においては、停止スイッチ10
2の操作と略同時に得られる生成運転の停止時(図3の
T2)から電動ポンプP1の停止と略同時に得られる逆
電洗浄の開始時(図3のT3)までの間にタイムラグを
設けて、逆電洗浄が未電解の原水内で開始されるように
し、水素イオンが電極33に吸着されて生じる水素脆性
反応が抑制されるようにしたが、当該装置によって生成
されるイオン水のイオン化濃度が低くて上記した水素脆
性反応が問題とならない場合には、停止スイッチ102
の操作と略同時に得られる生成運転の停止時(図3のT
2)に電動ポンプP1が停止されて略同時に逆電洗浄が
開始されるように構成して実施することも可能である。
In the above embodiment, the stop switch 10
A time lag is provided between the time when the production operation is stopped (T2 in FIG. 3), which is obtained almost simultaneously with the operation of 2, and the start of the reverse cleaning (T3, which is obtained), which is obtained almost simultaneously with the stop of the electric pump P1. The reverse electrolysis cleaning was started in the unelectrolyzed raw water, and the hydrogen embrittlement reaction caused by the adsorption of hydrogen ions on the electrode 33 was suppressed, but the ionization concentration of the ion water produced by the device was suppressed. If the hydrogen embrittlement reaction is low and the above hydrogen embrittlement reaction is not a problem, the stop switch 102
When the production operation is stopped, which can be obtained almost simultaneously with the operation of
In 2), the electric pump P1 may be stopped and the reverse electric cleaning may be started at substantially the same time.

【0021】また上記実施例においては、水道水を原水
として本発明を実施したが、例えば特開平4−7557
6号公報に示されている装置によって得られる食塩水を
原水として本発明を実施することも可能である。また、
上記実施例において分岐した接続管13と単一の電動ポ
ンプP1により電解槽30の各電極室34,35に原水
がそれぞれ供給されるように構成して本発明を実施した
が、一対の接続管とこれら各接続管にそれぞれ介装した
電動ポンプにより電解槽30の各電極室34,35に原
水がそれぞれ供給されるように構成して本発明を実施す
ることも可能である。
In the above embodiment, the present invention was carried out by using tap water as raw water.
It is also possible to carry out the present invention using saline solution obtained by the device shown in Japanese Patent Publication No. 6 as raw water. Also,
The present invention was carried out in such a manner that the raw water is supplied to the electrode chambers 34 and 35 of the electrolytic cell 30 by the branched connecting pipe 13 and the single electric pump P1 in the above-described embodiment. It is also possible to implement the present invention by configuring so that the raw water is supplied to the electrode chambers 34, 35 of the electrolytic cell 30 by electric pumps respectively interposed in the connection pipes.

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

【図1】 本発明による電解イオン水生成装置の一実施
例を示す全体構成図である。
FIG. 1 is an overall configuration diagram showing an embodiment of an electrolytic ionized water generator according to the present invention.

【図2】 図1に示した電解イオン水生成装置の使用状
態を概略的に示す図である。
FIG. 2 is a diagram schematically showing a use state of the electrolytic ionized water generator shown in FIG.

【図3】 図1及び図2に示した電解イオン水生成装置
の作動説明図である。
FIG. 3 is an operation explanatory diagram of the electrolytic ionized water generator shown in FIGS. 1 and 2.

【符号の説明】[Explanation of symbols]

10…貯水タンク、13…接続管、30…電解槽、3
2,33…電極、34,35…電極室、36…隔膜、3
7…第1排出管、38…第2排出管、37a,38a…
立上部、110…電極切換器、120…電源回路、10
0…制御装置、P1…電動ポンプ。
10 ... Water tank, 13 ... Connection pipe, 30 ... Electrolyzer, 3
2, 33 ... Electrodes, 34, 35 ... Electrode chambers, 36 ... Diaphragm, 3
7 ... 1st discharge pipe, 38 ... 2nd discharge pipe, 37a, 38a ...
Rise, 110 ... Electrode changer, 120 ... Power circuit, 10
0 ... Control device, P1 ... Electric pump.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 水または食塩水等の原水を貯溜する貯水
タンクと、第1及び第2の電極を内部に対向配設すると
ともにこれら両電極間に隔膜を配設して各電極を収容す
る第1及び第2の電極室を形成しこれら両電極室に原水
が流入・流出するようにした電解槽と、前記貯水タンク
の原水を接続管を通して前記電解槽の両電極室に圧送す
る電動ポンプと、前記貯水タンクの水面より上方に立ち
上がる立上部と大気に連通可能な開口を有して前記第1
の電極室に接続され同電極室にて生成された電解イオン
水を排出する第1排出管と、前記貯水タンクの水面より
上方に立ち上がる立上部と大気に連通可能な開口を有し
て前記第2の電極室に接続され同電極室にて生成された
電解イオン水を排出する第2排出管と、電源回路から前
記両電極に印加される直流電圧の正逆を切り換える電極
切換手段と、前記電動ポンプ及び前記電極切換手段の作
動を制御して、生成運転時に前記電動ポンプを駆動状態
に維持するとともに前記電極切換手段を正電状態に維持
し、また運転停止時に前記電動ポンプを停止させると略
同時に前記電極切換手段を逆電状態に切り換えて設定時
間維持する作動制御手段を備えた電解イオン水生成装
置。
1. A water storage tank for storing raw water such as water or salt water, and a first and a second electrode which are arranged facing each other inside, and a diaphragm is arranged between these two electrodes to accommodate each electrode. An electrolysis tank in which first and second electrode chambers are formed so that raw water can flow into and out of the two electrode chambers, and an electric pump for pressure-feeding raw water in the water storage tank to both electrode chambers in the electrolysis tank through a connecting pipe. And a first upper portion that rises above the water surface of the water storage tank and an opening that can communicate with the atmosphere.
A first discharge pipe connected to the electrode chamber for discharging electrolytic ionized water generated in the electrode chamber, a rising portion rising above the water surface of the water storage tank, and an opening communicating with the atmosphere. A second discharge pipe connected to the second electrode chamber for discharging electrolytic ionized water generated in the electrode chamber; electrode switching means for switching between direct and reverse of the DC voltage applied from the power supply circuit to the both electrodes; When the operation of the electric pump and the electrode switching means is controlled to maintain the electric pump in the driving state during the generating operation, the electrode switching means is maintained in the positive electric state, and the electric pump is stopped when the operation is stopped. An electrolyzed ionized water production apparatus comprising operation control means for switching the electrode switching means to a reverse electric state at substantially the same time and maintaining the set time.
JP12040994A 1994-06-01 1994-06-01 Electrolytic ionic water generator Expired - Fee Related JP3426341B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12040994A JP3426341B2 (en) 1994-06-01 1994-06-01 Electrolytic ionic water generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12040994A JP3426341B2 (en) 1994-06-01 1994-06-01 Electrolytic ionic water generator

Publications (2)

Publication Number Publication Date
JPH07328625A true JPH07328625A (en) 1995-12-19
JP3426341B2 JP3426341B2 (en) 2003-07-14

Family

ID=14785512

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12040994A Expired - Fee Related JP3426341B2 (en) 1994-06-01 1994-06-01 Electrolytic ionic water generator

Country Status (1)

Country Link
JP (1) JP3426341B2 (en)

Also Published As

Publication number Publication date
JP3426341B2 (en) 2003-07-14

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