JPH07313981A - Electrolytic water making apparatus - Google Patents

Electrolytic water making apparatus

Info

Publication number
JPH07313981A
JPH07313981A JP11151394A JP11151394A JPH07313981A JP H07313981 A JPH07313981 A JP H07313981A JP 11151394 A JP11151394 A JP 11151394A JP 11151394 A JP11151394 A JP 11151394A JP H07313981 A JPH07313981 A JP H07313981A
Authority
JP
Japan
Prior art keywords
water
electrolytic cell
electrolytic
cation
cathode
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
JP11151394A
Other languages
Japanese (ja)
Inventor
Kazuyoshi Okada
和義 岡田
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 JP11151394A priority Critical patent/JPH07313981A/en
Publication of JPH07313981A publication Critical patent/JPH07313981A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To enhance electrolytic water making efficiency and to suppress the formation of scale to extend the life of an electrode or diaphragm by providing a cation removing device in the vicinity of the inflow port of an electrolytic cell to remove an excessive cation from raw water. CONSTITUTION:When a power supply switch 31 is turned ON, a control unit 30 controls the opening and closing of a solenoid opening and closing valve V1 and a pinch valve V2 to respectively hold the water level and concn. of the dilute salt water in a storage tank 10 to predetermined ranges. At the same time, the control unit 30 controls the driving and stop of an electromotive pump P1 and the cutting-off of the supply of a current to an electrolytic cell 20. In the electrolytic cell 20, an anode 22 and a cathode 23 are arranged in a cell main body 21 in opposed relationship and the cathode and anode chambers R1, R2 respectively receiving the cathode and the anode are demarcated by a diaphragm 24. In this case, a cation removing device 19 is provided in the vicinity of the inflow port of the electrolytic cell 20. By removing an excessive cation from raw water, electrolytic water making efficiency is enhanced and the formation of scale is suppressed.

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、電解水生成装置に関
し、特に、隔膜で内部をプラス電極を収容する陽極室と
マイナス電極を収容する陰極室に区画された電解槽に原
水を供給して電解槽にて電解処理し、電解槽の陽極室出
口から酸性イオン水が得られるとともに陰極室出口から
アルカリ性イオン水が得られるように構成した電解水生
成装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolyzed water producing apparatus, and more particularly, it supplies raw water to an electrolyzer divided into a positive electrode chamber containing a positive electrode and a negative electrode chamber containing a negative electrode by a diaphragm. The present invention relates to an electrolyzed water generator configured to perform electrolytic treatment in an electrolyzer to obtain acidic ionized water from an outlet of an anode chamber of the electrolyzer and alkaline ionized water from an outlet of a cathode chamber.

【0002】[0002]

【従来の技術】この種の電解水生成装置においては、各
電解生成イオン水の製造コストを下げることを目的とし
て、電解槽に供給される原水として水道水または地下水
が使用され、例えば特開平5−115875号公報にて
示されているように、電解槽の流入側に水道水中の残留
塩素を除去するフィルタを設ける場合がある。また、前
記フィルタに代えてまたは前記フィルタに加えてゴミ等
の比較的大きな異物を除去するフィルタを設ける場合が
ある。
2. Description of the Related Art In this type of electrolyzed water producing apparatus, tap water or ground water is used as raw water to be supplied to an electrolyzer for the purpose of reducing the production cost of each electrolyzed ionized water. As disclosed in Japanese Patent Laid-Open No. 115875, a filter for removing residual chlorine in tap water may be provided on the inflow side of the electrolytic cell. Further, instead of the filter or in addition to the filter, a filter for removing relatively large foreign matter such as dust may be provided.

【0003】[0003]

【発明が解決しようとする課題】上記した従来の電解水
生成装置においては、原水に混入するMgイオン、Ca
イオン、Naイオン等の陽イオン(カチオン)を除去す
ることができない。ところで、Mgイオン、Caイオ
ン、Naイオン等の陽イオンを多く含む原水を電解槽に
供給して電解処理すると、短時間にてマイナス電極の表
面にMg、Ca、Na等が層状に付着しスケールとなっ
て通電率を低下させるばかりか、隔膜に付着してイオン
透過効率を低下させるため、所望のイオン水が得られな
くなる。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、その目的は電解槽に供給される原水から陽
イオンを除去することにある。
In the above-mentioned conventional electrolyzed water generator, Mg ions and Ca mixed in the raw water are used.
It is not possible to remove cations (cations) such as ions and Na ions. By the way, when raw water containing a large amount of cations such as Mg ions, Ca ions, and Na ions is supplied to the electrolytic cell for electrolytic treatment, Mg, Ca, Na, etc. adhere to the surface of the negative electrode in layers in a short time and scale As a result, not only does the current flow rate decrease, but also the ion permeation efficiency decreases by adhering to the diaphragm, so that desired ionized water cannot be obtained. The present invention has been made to address the above-mentioned problems, and an object thereof is to remove cations from raw water supplied to an electrolytic cell.

【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、隔膜で内部をプラス電極を
収容する陽極室とマイナス電極を収容する陰極室に区画
された電解槽に原水を供給して電解槽にて電解処理し、
電解槽の陽極室出口から酸性イオン水が得られるととも
に陰極室出口からアルカリ性イオン水が得られるように
構成した電解水生成装置において、前記電解槽の流入口
近傍に原水から陽イオンを除去する陽イオン除去装置を
設けた。
In order to achieve the above-mentioned object, in the present invention, raw water is supplied to an electrolytic cell divided by a diaphragm into an anode chamber containing a positive electrode and a cathode chamber containing a negative electrode. Is supplied and electrolyzed in an electrolytic cell,
In an electrolyzed water generator configured to obtain acidic ionized water from the outlet of the anode chamber of the electrolytic cell and alkaline ionized water from the outlet of the cathode chamber, a cation for removing cations from raw water in the vicinity of the inlet of the electrolytic cell. An ion removal device was provided.

【0005】[0005]

【発明の作用効果】本発明による電解水生成装置におい
ては、電解槽の流入口近傍に設けた陽イオン除去装置に
より、電解槽に供給される直前の原水から余剰のMgイ
オン、Caイオン、Naイオン等の陽イオンを除去する
ことができるため、電解生成効率が向上するとともに、
マイナス電極及び隔膜でのスケールの生成が抑制される
ため同電極及び隔膜の寿命向上を図ることができる。ま
た、原水として食塩を所定量含む希塩水を使用する場合
において、純度が低くて安価な並塩(純度が95%程度
で不純物としてMg、Ca塩を多く含んでいる)を使用
することができ、ランニングコストを低減することがで
きる。
In the electrolyzed water generator according to the present invention, the excess cations, Mg ions, Ca ions and Na ions from the raw water immediately before being supplied to the electrolytic cell are provided by the cation removing device provided near the inlet of the electrolytic cell. Since cations such as ions can be removed, the efficiency of electrolysis is improved and
Since the generation of scale at the negative electrode and the diaphragm is suppressed, the life of the electrode and the diaphragm can be improved. Further, in the case of using dilute salt water containing a predetermined amount of salt as raw water, low-purity and inexpensive normal salt (purity of about 95% and containing a large amount of Mg and Ca salts as impurities) can be used. The running cost can be reduced.

【0006】[0006]

【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は本発明を実施した電解水生成装置を示
していて、この電解水生成装置は原水(希塩水)を所要
量貯える貯溜タンク10を備えている。貯溜タンク10
は、制御装置30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)と塩濃度センサ12を内
部に備えていて、これら水位センサ11及び塩濃度セン
サ12からの信号により、水道水(地下水の場合もあ
る)供給管13に設けた電磁開閉弁V1が開閉されると
ともに、濃塩水(飽和食塩水)貯蔵タンク14に接続さ
れている濃塩水供給管15に設けたピンチバルブV2が
開閉されて貯溜タンク10内の希塩水の水位及び濃度が
それぞれ所定の範囲に維持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 electrolyzed water producing apparatus embodying the present invention, and this electrolyzed water producing apparatus includes a storage tank 10 for storing a required amount of raw water (diluted salt water). Storage tank 10
Includes a water level sensor 11 (which detects an upper limit water level and a lower limit water level) connected to the control device 30 and a salt concentration sensor 12 inside, and a signal from the water level sensor 11 and the salt concentration sensor 12 causes The electromagnetic on-off valve V1 provided in the water (also groundwater) supply pipe 13 is opened and closed, and the pinch valve V2 provided in the concentrated salt water supply pipe 15 connected to the concentrated salt water (saturated saline) storage tank 14 is opened. Is opened and closed to maintain the water level and concentration of the dilute salt water in the storage tank 10 within predetermined ranges.

【0007】また、貯溜タンク10には、電解槽20の
両流入口21a,21bに分岐して接続される接続管1
6が取付けられていて、接続管16には制御装置30に
よって作動を制御される定流量型の電動ポンプP1が介
装されるとともに糸まきフィルタ18と陽イオン除去装
置19が介装されていて、電動ポンプP1の駆動により
貯溜タンク10内の希塩水が接続管16を通し糸まきフ
ィルタ18(比較的大きな固形物を除去するもの)と陽
イオン除去装置19でそれぞれ浄化処理されて電解槽2
0の両流入口21a,21bに供給されるように構成さ
れている。陽イオン除去装置19は、電解槽20の流入
口近傍に配設されて原水から陽イオンを除去するもので
あり、例えばカチオン交換樹脂が使用される。
The storage tank 10 has a connecting pipe 1 which is branched and connected to both inlets 21a and 21b of the electrolytic cell 20.
6 is attached, a constant flow type electric pump P1 whose operation is controlled by a control device 30 is installed in the connecting pipe 16, and a thread winding filter 18 and a cation removing device 19 are also installed in the connecting pipe 16. When the electric pump P1 is driven, the diluted salt water in the storage tank 10 passes through the connecting pipe 16 and is purified by the thread-winding filter 18 (which removes relatively large solid matter) and the cation removing device 19, respectively, and the electrolytic bath 2
It is configured to be supplied to both inlets 21a and 21b of 0. The cation removing device 19 is arranged near the inflow port of the electrolytic cell 20 and removes cations from the raw water. For example, a cation exchange resin is used.

【0008】電解槽20は、一対の流入口21a,21
bと一対の流出口21c,21dを有する槽本体21
と、この槽本体21内に対向配設したプラス電極22及
びマイナス電極23と、これら両電極22,23間に配
設されて各電極21,23を収容する陰極室R1と陽極
室R2を形成する隔膜24によって構成されていて、陰
極室R1には流入口21aと流出口21cが連通し、陽
極室R2には流入口21bと流出口21dが連通してい
る。また、各流出口21c,21dには電解によって生
成されたアルカリ性イオン水,酸性イオン水をそれぞれ
導出する各導出管25,26が接続されていて、各導出
管25,26は各貯蔵タンク(図示省略)にそれぞれ接
続されている。各電極22,23は、各電線27,28
を介して制御装置30に接続されていて、制御装置30
によって直流印加電圧の通電・遮断が制御されるように
構成されている。なお、図示省略した各貯蔵タンクに
は、貯溜タンク10と同様に水位センサ(上限水位と下
限水位を検出するもの)とオーバーフローパイプがそれ
ぞれ設けられている。
The electrolytic cell 20 includes a pair of inlets 21a, 21a.
tank body 21 having b and a pair of outlets 21c and 21d
A positive electrode 22 and a negative electrode 23, which are arranged to face each other in the tank body 21, and a cathode chamber R1 and an anode chamber R2 which are arranged between the electrodes 22 and 23 and accommodate the electrodes 21 and 23. The cathode chamber R1 is in communication with the inflow port 21a and the outflow port 21c, and the anode chamber R2 is in communication with the inflow port 21b and the outflow port 21d. Further, the outlets 21c and 21d are connected to respective outlet pipes 25 and 26 which lead out alkaline ionized water and acidic ionized water produced by electrolysis, respectively. Omitted) respectively. The electrodes 22 and 23 are connected to the electric wires 27 and 28, respectively.
Connected to the control device 30 via
Is configured to control the energization / interruption of the DC applied voltage. Each storage tank (not shown) is provided with a water level sensor (which detects an upper limit water level and a lower limit water level) and an overflow pipe, like the storage tank 10.

【0009】制御装置30は、電源スイッチ31がON
のとき水位センサ11及び塩濃度センサ12からの信号
により水道水供給管13に設けた電磁開閉弁V1と濃塩
水供給管14に設けたピンチバルブV2を開閉制御して
貯溜タンク10内の希塩水の水位及び濃度をそれぞれ所
定の範囲に維持する原水制御回路を内蔵するとともに、
図示省略した各貯蔵タンクの水位センサからの信号によ
り電動ポンプP1の駆動・停止と電解槽20への通電・
遮断を制御する電解制御回路を内蔵している。
In the control device 30, the power switch 31 is turned on.
At this time, the solenoid valve V1 provided in the tap water supply pipe 13 and the pinch valve V2 provided in the concentrated salt water supply pipe 14 are opened / closed by signals from the water level sensor 11 and the salt concentration sensor 12 to control the diluted salt water in the storage tank 10. With a built-in raw water control circuit that maintains the water level and concentration of
The electric pump P1 is driven / stopped and the electrolyzer 20 is energized by a signal from a water level sensor of each storage tank (not shown).
It has a built-in electrolysis control circuit that controls interruption.

【0010】上記のように構成した本実施例において
は、電源スイッチ31がONされると、制御装置30の
原水制御回路により電磁開閉弁V1とピンチバルブV2
が開閉制御されて、貯溜タンク10内の希塩水の水位及
び濃度がそれぞれ所定の範囲に維持され、また制御装置
30の電解制御回路により電動ポンプP1の駆動・停止
と電解槽20への通電・遮断が制御されて、貯溜タンク
10から電解槽20への希塩水の供給と電解槽20での
電解生成処理が制御され、図示省略した両貯蔵タンクに
それぞれ収容される各電解生成イオン水(アルカリ性イ
オン水、酸性イオン水)の水位がそれぞれ所定の範囲に
維持される。
In the present embodiment constructed as described above, when the power switch 31 is turned on, the raw water control circuit of the control device 30 causes the electromagnetic on-off valve V1 and the pinch valve V2.
Is controlled to be opened and closed to maintain the water level and concentration of the dilute salt water in the storage tank 10 within predetermined ranges, and the electrolysis control circuit of the control device 30 drives / stops the electric pump P1 and energizes the electrolysis tank 20. The shutoff is controlled to control the supply of the dilute salt water from the storage tank 10 to the electrolytic cell 20 and the electrolytic generation process in the electrolytic cell 20, and each electrolytically generated ion water (alkaline The water levels of ionized water and acidic ionized water) are maintained within predetermined ranges.

【0011】ところで、本実施例においては、電解槽2
0の流入口近傍に設けた陽イオン除去装置19により、
電解槽20に供給される直前の原水から余剰のMgイオ
ン、Caイオン、Naイオン等の陽イオンを除去するこ
とができるため、電解生成効率が向上するとともに、マ
イナス電極23及び隔膜24でのスケールの生成が抑制
されるため同電極23及び隔膜24の寿命向上を図るこ
とができる。また、濃塩水貯蔵タンク14に貯える濃塩
水を作る食塩として、純度が低くて安価な並塩(純度が
95%程度で不純物としてMg、Ca塩を多く含んでい
る)を使用することができ、ランニングコストを低減す
ることができる。
By the way, in this embodiment, the electrolytic cell 2
By the cation removing device 19 provided near the inflow port of 0,
Since excess cations such as Mg ions, Ca ions, and Na ions can be removed from the raw water immediately before being supplied to the electrolytic cell 20, the electrolytic generation efficiency is improved and the scale at the negative electrode 23 and the diaphragm 24 is improved. As a result, the life of the electrode 23 and the diaphragm 24 can be improved. Further, as the salt for making the concentrated salt water to be stored in the concentrated salt water storage tank 14, low-purity and inexpensive ordinary salt (purity is about 95% and contains a lot of Mg and Ca salts as impurities) can be used. The running cost can be reduced.

【0012】上記実施例においては、希塩水を電解槽2
0にて電解処理する電解水生成装置に本発明を実施した
が、本発明は食塩を加えない原水(水道水または地下水
そのもの)を電解槽20にて電解処理する電解水生成装
置にも同様に実施することができるものである。この場
合には、水道水供給管13と接続管16を直接接続して
貯溜タンク10及び電動ポンプP1を省略することも可
能である。
In the above embodiment, dilute salt water is used for the electrolytic cell 2.
Although the present invention was carried out in an electrolyzed water generator for electrolyzing at 0, the present invention is also applicable to an electrolyzed water generator for electrolyzing raw water (tap water or groundwater itself) without adding salt in the electrolyzer 20. It can be implemented. In this case, the tap water supply pipe 13 and the connection pipe 16 may be directly connected to omit the storage tank 10 and the electric pump P1.

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

【図1】 本発明を実施した電解水生成装置の一実施例
を示す図である。
FIG. 1 is a diagram showing an example of an electrolyzed water generator according to the present invention.

【符号の説明】[Explanation of symbols]

13…水道水供給管、16…接続管、19…陽イオン除
去装置、20…電解槽、21…槽本体、21a,21b
…流入口、21c,21d…流出口、22…プラス電
極、23…マイナス電極、24…隔膜、R1…陰極室、
R2…陽極室。
13 ... Tap water supply pipe, 16 ... Connection pipe, 19 ... Cation removal device, 20 ... Electrolyzer, 21 ... Tank body, 21a, 21b
Inflow port, 21c, 21d ... Outflow port, 22 ... Positive electrode, 23 ... Minus electrode, 24 ... Diaphragm, R1 ... Cathode chamber,
R2 ... Anode chamber.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 隔膜で内部をプラス電極を収容する陽極
室とマイナス電極を収容する陰極室に区画された電解槽
に原水を供給して電解槽にて電解処理し、電解槽の陽極
室出口から酸性イオン水が得られるとともに陰極室出口
からアルカリ性イオン水が得られるように構成した電解
水生成装置において、前記電解槽の流入口近傍に原水か
ら陽イオンを除去する陽イオン除去装置を設けたことを
特徴とする電解水生成装置。
1. Raw water is supplied to an electrolytic cell partitioned by a diaphragm into an anode chamber containing a positive electrode and a cathode chamber containing a negative electrode for electrolytic treatment in the electrolytic cell, and the outlet of the anode chamber of the electrolytic cell. In the electrolyzed water generator configured to obtain alkaline ionized water from the cathode chamber outlet while obtaining acidic ionized water from the cathode chamber, a cation removing device for removing cations from raw water is provided near the inlet of the electrolytic cell. An electrolyzed water generator characterized in that.
JP11151394A 1994-05-25 1994-05-25 Electrolytic water making apparatus Pending JPH07313981A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11151394A JPH07313981A (en) 1994-05-25 1994-05-25 Electrolytic water making apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11151394A JPH07313981A (en) 1994-05-25 1994-05-25 Electrolytic water making apparatus

Publications (1)

Publication Number Publication Date
JPH07313981A true JPH07313981A (en) 1995-12-05

Family

ID=14563222

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11151394A Pending JPH07313981A (en) 1994-05-25 1994-05-25 Electrolytic water making apparatus

Country Status (1)

Country Link
JP (1) JPH07313981A (en)

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