JP2003236548A - Electrolytic water producing apparatus - Google Patents

Electrolytic water producing apparatus

Info

Publication number
JP2003236548A
JP2003236548A JP2002038227A JP2002038227A JP2003236548A JP 2003236548 A JP2003236548 A JP 2003236548A JP 2002038227 A JP2002038227 A JP 2002038227A JP 2002038227 A JP2002038227 A JP 2002038227A JP 2003236548 A JP2003236548 A JP 2003236548A
Authority
JP
Japan
Prior art keywords
water
electrolytic cell
alkaline
flow path
state
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
JP2002038227A
Other languages
Japanese (ja)
Other versions
JP4002594B2 (en
Inventor
Fumio Suzuki
文夫 鈴木
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.)
Kyushu Hitachi Maxell Ltd
Maxell Holdings Ltd
Original Assignee
Kyushu Hitachi Maxell Ltd
Hitachi Maxell 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 Kyushu Hitachi Maxell Ltd, Hitachi Maxell Ltd filed Critical Kyushu Hitachi Maxell Ltd
Priority to JP2002038227A priority Critical patent/JP4002594B2/en
Publication of JP2003236548A publication Critical patent/JP2003236548A/en
Application granted granted Critical
Publication of JP4002594B2 publication Critical patent/JP4002594B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

<P>PROBLEM TO BE SOLVED: To provide an apparatus for selectively producing water with high hypochlorous acid concentration, acid water and alkaline water, respectively. <P>SOLUTION: The electrolytic water producing apparatus has a water cleaning means 2 and a chloride ion feeding means 8 at the upstream side of an electrolysis vessel 5 provided with an anode plate 52 and a cathode plate 51, an acid stream passage 7 for discharging water of an anode plate side 52, and an alkaline stream passage 6 for discharging water of a cathode plate side 51 are provided at the downstream side of the electrolysis vessel 5. The chloride ion feeding means 8 can freely be switched to be in a state where chloride ion is supplied in the electrolysis vessel 5, or a state where an chloride ion is not supplied in the electrolysis vessel 5. The flow passage of at least one of the acid stream passage 7 or the alkaline stream passage 6 provided at the downstream side of the electrolysis vessel 5 is closed with the switch of the chloride ion into the electrolysis vessel 5. Drainage from the electrolysis vessel 5 is entirely discharged from a single discharge port. All are discharged from the single discharge port. <P>COPYRIGHT: (C)2003,JPO

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】この発明は、水を連続的に電
気分解して次亜塩素酸濃度の高い水と、酸性水とアルカ
リ性水をそれぞれ選択的に生成する装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for continuously electrolyzing water to selectively generate water having a high concentration of hypochlorous acid, and acidic water and alkaline water.

【0002】[0002]

【従来の技術】従来から水を電気分解することにより酸
性水とアルカリ性水を連続的に生成する装置が知られて
いる。電解槽の隔膜を境界として一方の室から排水され
るアルカリ水は健康に良い水として利用され、また同時
に他方の室で生成される酸性水は殺菌性のある水として
利用される。しかしながら一般的に水道水を単に電気分
解するのみでは十分な殺菌性のある水は生成されること
はなく、このような装置において酸性水に殺菌性をもた
せるためには必要に応じて食塩などの電離性無機電解質
を添加し、ペーハー値を下げるようにするのが一般的で
あった。その生成器は家庭でも手軽に利用されている。
従来このような殺菌水は殺菌力は強いが、食品添加物と
して認められておらず、使用されるものが限定されさら
には反面金属への腐食性も強い欠点もある。また、同時
に生成されるアルカリ性水は捨て水として廃棄される無
駄が生じることになる。当然のことながら、食塩等の影
響で酸性度が高い分同時に生成されるアルカリ水もアル
カリ度が高くなっており、飲用に使用するには適してい
ないだけでなく誤飲すると健康を害する虞もあるため殺
菌水生成時には強アルカリ水の誤飲がないように十分注
意する必要がある。
2. Description of the Related Art Conventionally, there has been known a device for continuously producing acidic water and alkaline water by electrolyzing water. The alkaline water drained from one chamber with the diaphragm of the electrolytic cell as a boundary is used as healthy water, and at the same time, the acidic water generated in the other chamber is used as sterilizing water. However, in general, simply electrolyzing tap water does not produce sufficiently sterilizing water, and in order to make acid water sterilizing in such a device, salt water etc. may be added as necessary. It was general to add an ionizing inorganic electrolyte to lower the pH value. The generator is easily used at home.
Conventionally, such sterilizing water has a strong sterilizing power, but it has not been recognized as a food additive, and its use is limited, and on the other hand, it has the drawback of being highly corrosive to metals. Further, the alkaline water generated at the same time is wasted as waste water. As a matter of course, the alkaline water generated at the same time as the acidity is high due to the influence of salt etc. also has a high alkalinity, which is not suitable for drinking and may cause health problems if swallowed accidentally. Therefore, when sterilizing water is generated, it is necessary to pay sufficient attention to avoid accidental ingestion of strong alkaline water.

【0003】[0003]

【発明が解決しようとする課題】このように従来の一般
的なアルカリイオン水整水器においては、健康に適した
アルカリイオン水を得るには適した製品であったが、同
時に生成される酸性水を殺菌水として有効に、安全に利
用するには問題が多いものである。一方、水を電気分解
して次亜塩素酸濃度の高い殺菌水を生成する装置は周知
である。特に簡便に連続して殺菌水を得る装置として特
開平4-330986号が知られている。このような従来の装置
により得られる所謂次亜塩素酸水は食品添加物として認
められており、安全性も高く生成時に同時に強アルカリ
水が生成される虞もないので殺菌水を得る装置としては
適している。
As described above, the conventional general alkaline ionized water conditioner was a product suitable for obtaining alkaline ionized water suitable for health, but the acidic water produced at the same time. There are many problems in using water effectively and safely as sterilizing water. On the other hand, a device for electrolyzing water to generate sterilized water having a high concentration of hypochlorous acid is well known. JP-A-4-330986 is known as a device for obtaining sterilized water in a particularly simple and continuous manner. So-called hypochlorous acid water obtained by such a conventional device is recognized as a food additive, and since it is highly safe and there is no fear of generating strong alkaline water at the same time, it is used as a device for obtaining sterilized water. Are suitable.

【0004】しかしながらこの種の次亜塩素酸濃度の高
い殺菌水を生成する装置においては隔膜が無い構成でな
ければならず、従来の一般的なアルカリイオン整水器と
は構成に差異があるため、両者の装置は別々に製品化さ
れていた。そこでこれら従来の欠点を解消するために特
開2000-117254号に示すように、無隔膜の電解槽を用い
て混合水を得る構成が考えられるが、この従来例におい
ては食塩の添加が自動的になされるため飲用としてのア
ルカリ水の生成が好適に出来ないものである。また、電
解槽も無隔膜であるものの、次亜塩素酸生成時には電極
間の中心を通過した水がそのまま直進して排出されるも
のではないため、良好な次亜塩素酸が生成出来難いもの
であった。
However, this type of device for producing sterilized water having a high concentration of hypochlorous acid must have a structure without a diaphragm, and has a difference in structure from a conventional general alkaline ionized water device. , Both devices were commercialized separately. Therefore, in order to eliminate these conventional drawbacks, as shown in JP-A-2000-117254, it is conceivable to use a diaphragmless electrolytic cell to obtain mixed water, but in this conventional example, addition of salt is automatically performed. Therefore, alkaline water for drinking cannot be suitably produced. Also, the electrolytic cell is also a diaphragm, but when hypochlorous acid is produced, the water that has passed through the center between the electrodes does not go straight and is discharged, so it is difficult to produce good hypochlorous acid. there were.

【0005】[0005]

【課題を解決するための手段】この発明は以上の従来例
の問題点を解消するために、陽極板と陰極板を備えた電
解槽の上流側に浄水手段と塩素イオン供給手段を有し、
上記電解槽の下流側に陽極板側の水を排出する酸性水流
路と陰極板側の水を排出するアルカリ水流路を設けた電
解水生成装置において、上記塩素イオン供給手段は電解
槽内に塩素イオンが供給される状態と電解槽内に塩素イ
オンが供給されない状態に切替え自在であり、塩素イオ
ンを電解槽内に供給する状態に切り替えるのと連動して
電解槽の下流側に設けられた酸性水流路もしくはアルカ
リ水流路の少なくとも一方の流路が実質的に閉塞され、
電解槽からの排水が全て単一の排出口から排出されるよ
うにした。
In order to solve the above-mentioned problems of the conventional example, the present invention has a water purifying means and a chlorine ion supplying means on the upstream side of an electrolytic cell provided with an anode plate and a cathode plate,
In the electrolyzed water generator provided with an acidic water flow path for discharging water on the anode plate side and an alkaline water flow path for discharging water on the cathode plate side on the downstream side of the electrolytic cell, the chlorine ion supply means is chlorine in the electrolytic cell. It is possible to switch between the state in which ions are supplied and the state in which chlorine ions are not supplied in the electrolytic cell, and in conjunction with switching to the state in which chlorine ions are supplied in the electrolytic cell, the acidity provided on the downstream side of the electrolytic cell At least one of the water channel or the alkaline water channel is substantially closed,
All the drainage water from the electrolyzer was discharged from a single outlet.

【0006】このように構成することで、塩素イオンが
供給されている時は自動的に電解槽からの排水が分離さ
れることなく全て単一の排水口から排水されるので、極
端にペーハーの偏りのある強アルカリ水や強酸性水が生
成されることはなく、誤飲による健康への悪影響の虞が
ない。なお、塩素イオンが供給された水を分離排水をし
ないで電解した場合、次亜塩素酸水が生成されることが
知られているが、この次亜塩素酸水は食品添加物として
認められているので極端な強アルカリ水や強酸性水に比
べ誤飲による健康上の問題は少ない。また、飲用に適す
るアルカリ水やアストリンゼント水として利用できる酸
性水などを必要とする場合は、塩素イオンの供給が無い
ようにするとともに、酸性水流路とアルカリ性水流路に
分かれて排水される。すなわち、本発明によれば、飲用
に適したアルカリ水と、アストリンゼン効果のある酸性
水と、殺菌効果のある次亜塩素酸水をそれぞれ必要に応
じて確実に得られる効果がある。
With such a structure, when chlorine ions are being supplied, the drainage from the electrolytic cell is not automatically separated, but all is drained from a single drain port, so that the pH is extremely low. Unbiased strong alkaline water or strongly acidic water is not generated, and there is no risk of adverse health effects due to accidental ingestion. It is known that when the water supplied with chlorine ions is electrolyzed without separation and drainage, hypochlorous acid water is generated, but this hypochlorous acid water is recognized as a food additive. Therefore, compared to extremely strong alkaline water or strongly acidic water, there are less health problems due to accidental ingestion. When alkaline water suitable for drinking or acidic water that can be used as astringent water is required, chlorine ion is not supplied and the acidic water channel and the alkaline water channel are separately discharged. That is, according to the present invention, there is an effect that alkaline water suitable for drinking, acidic water having an astringent effect, and hypochlorous acid water having a bactericidal effect can be reliably obtained as needed.

【0007】また、この発明の請求項2によれば、上記
電解槽は陽極板と陰極板を対向させその間に水を通す無
隔膜式とし、酸性水流路は陽極板に形成されたスリット
状の開口と連通せしめ、アルカリ性流路は対向電極間の
端部からの排出口と連通させるとともに、上記酸性流路
の途中に閉塞自在な電磁弁を設けたので、酸性流路の電
磁弁を閉じた状態では、2枚の電極が隔膜なしで対向し
た間を通過した水の全てがどちらの電極にも偏らない位
置で排出される構造となり、極めて効果的に次亜水を生
成出来る。更には、この発明の請求項3によれば、本発
明を実現するために添加筒と電磁弁の構成を追加するの
みで良いため、従来のような食塩水供給のためのポンプ
手段を必要とせず故障の虞を可及的に減少させ、コスト
的にも有利となる。
According to a second aspect of the present invention, the electrolytic cell is of a diaphragm type in which an anode plate and a cathode plate are opposed to each other and water is allowed to pass between them, and the acidic water flow path is a slit-like shape formed in the anode plate. The alkaline flow passage was connected to the discharge port from the end between the counter electrodes, and a solenoid valve that could be closed was provided in the middle of the acid flow passage, so the acid flow passage was closed. In the state, the structure is such that all the water that has passed between the two electrodes facing each other without a diaphragm is discharged at a position that is not biased to either electrode, and hypochlorous water can be generated extremely effectively. Furthermore, according to claim 3 of the present invention, since it is only necessary to add the configuration of the addition cylinder and the solenoid valve in order to realize the present invention, the conventional pump means for supplying saline solution is not required. The risk of failure is reduced as much as possible, which is advantageous in terms of cost.

【0008】[0008]

【発明の実施の形態】図1は、本発明の水路を模式的に
示すものであって、水道蛇口が分岐栓10を介し本体1
と連結されており、基本的には、蛇口を開くと水は分岐
栓10、浄水カートリッジ2、流量センサー3、電解促
進剤としての例えばグリセロリン酸カルシウムを収容可
能な薬剤添加筒4、電解槽5を経て電解水出口のアルカ
リ水流路6、酸性水流路7から排水される。また浄水カ
ートリッジ2と薬剤添加筒4の間には別途、電磁弁A、
食塩添加筒8を経て上記薬剤添加筒4から電解槽5へ通
じる流路9の途中へ合流する塩素イオン供給流路11が
形成されている。上記薬剤添加筒4に入る薬剤は好まし
い実施例としてカルシウム化合物を挙げているが電解促
進剤としての機能を有し、塩素イオンのないものであれ
ば限定されることはない。また、塩素イオン供給手段と
して食塩を添加する手段を例示しているが塩素イオンを
供給可能な手段であれば食塩に限らないことは言うまで
もない。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 schematically shows a water channel according to the present invention, in which a water faucet is connected to a main body 1 through a branch plug 10.
Basically, when the faucet is opened, water basically has a branch plug 10, a water purification cartridge 2, a flow rate sensor 3, a chemical addition cylinder 4 capable of accommodating, for example, calcium glycerophosphate as an electrolysis promoter, and an electrolysis tank 5. After that, the water is discharged from the alkaline water flow path 6 and the acidic water flow path 7 at the electrolyzed water outlet. Separately, a solenoid valve A, between the water purification cartridge 2 and the chemical addition cylinder 4,
A chloride ion supply flow passage 11 is formed which joins the chemical addition pipe 4 through the salt addition pipe 8 to the middle of the flow passage 9 leading to the electrolytic cell 5. Although a calcium compound is cited as a preferred example of the drug that enters the drug adding cylinder 4, the drug is not limited as long as it has a function as an electrolysis accelerator and is free of chloride ions. Further, although a means for adding salt is illustrated as the chlorine ion supply means, it is needless to say that it is not limited to salt as long as it can supply chlorine ions.

【0009】食塩添加筒8は、図2及び図4に示すよう
に本体ケースの上方から着脱自在になっており、必要に
応じて食塩添加筒8を本体ケースから出して蓋14を開
け、食塩を入れることが出来る。食塩添加筒8にはケー
ス内に仕切りのためのプレート13が配設されておりプ
レート13下方方に食塩を置けるようになっている。
As shown in FIGS. 2 and 4, the salt addition cylinder 8 is detachable from the upper part of the main body case. If necessary, the salt addition cylinder 8 is taken out of the main body case and the lid 14 is opened. Can be inserted. A plate 13 for partitioning is arranged in the case of the salt addition cylinder 8 so that salt can be placed below the plate 13.

【0010】ケースには中央に貫通流路15があり、こ
の貫通流路15から上昇した水がプレート13の貫通孔
16から分散して流入し食塩を溶かす。飽和食塩水とな
った水がプレート13の孔からケース下方に形成された
排水孔17を経て薬剤添加筒4から電解槽5へ通じる。
この実施例にかかる電解水生成装置は上述のような基本
構成であり、図示しない本体操作パネルの切替え操作に
より浄水、飲用のアルカリ水、酸性水、殺菌水を簡単に
排出口から選択的に排水出来る。
The case has a through-flow passage 15 in the center, and the water rising from the through-flow passage 15 is dispersed from the through-hole 16 of the plate 13 and flows in to dissolve salt. Water that has become saturated saline flows from the holes of the plate 13 to the electrolytic cell 5 through the drainage holes 17 formed below the case and from the chemical addition cylinder 4.
The electrolyzed water generating apparatus according to this embodiment has the above-described basic configuration, and the purified water, the alkaline water for drinking, the acidic water, and the sterilizing water are easily selectively drained from the outlet by the switching operation of the main body operation panel (not shown). I can.

【0011】以下各選択されたモードにつき説明をす
る。 (飲用アルカリ水、酸性水モード)本体の操作スイッチ
によりアルカリ水が選択され分岐栓10から水が流入さ
れると、制御部12により電磁弁Aが閉じられるととも
に電磁弁Bが開く。電磁弁Aが閉じられることにより水
は浄水カートリッジ2から流量センサー3、薬剤添加筒
4を経て電解槽5へ流入される。電解槽5には所定の電
圧が印加され、複数のアルカリ濃度を選択出来るように
している。本実施例では強アルカリ濃度と中アルカリ濃
度及び弱アルカリ濃度を選択自在としそれに合わせて電
圧が制御される。電解槽5は隔膜を有す既存のものでも
ちろん適用可能であるが、本実施例においては下記する
次亜塩素酸水モードにおいてより望ましいとされる無隔
膜方式の電解槽を例示する。無隔膜方式の電解槽は図3
に示すように、陰極板51と陽極板52が対向し、スペ
ーサ54により形成された通水路55を水が通過し、電
極の対向領域の端部からアルカリ水流路6側へ排出され
る構成となっている。この通水路55は図1においては
模式的に大きな間隙として開示しているが、実際にはス
ペーサ54の厚みで決定され、0.5ミリから数ミリ程
度である。また、陽極板52の一部にスリット状の開口
53を設けることで陽極板52のごく近傍を通過する水
のみが酸性水として開口53から酸性水流路7へ流れ残
りの水がアルカリ水としてアルカリ水流路6へ流れる。
アルカリ水流路6から排出された水がアルカリイオン水
として飲用される。
The selected modes will be described below. (Drinking alkaline water, acidic water mode) When alkaline water is selected by the operation switch of the main body and water flows in from the branch tap 10, the control unit 12 closes the solenoid valve A and opens the solenoid valve B. When the electromagnetic valve A is closed, water flows from the water purification cartridge 2 into the electrolytic cell 5 through the flow rate sensor 3 and the chemical addition cylinder 4. A predetermined voltage is applied to the electrolytic cell 5 so that a plurality of alkali concentrations can be selected. In this embodiment, the strong alkali concentration, the medium alkali concentration, and the weak alkali concentration are selectable, and the voltage is controlled in accordance therewith. The electrolytic cell 5 is of course applicable to an existing one having a diaphragm, but in this embodiment, a non-diaphragm type electrolytic cell which is more preferable in the hypochlorous acid water mode described below is exemplified. Fig. 3 shows a diaphragmless electrolytic cell.
As shown in FIG. 3, the cathode plate 51 and the anode plate 52 are opposed to each other, water passes through the water passage 55 formed by the spacer 54, and the water is discharged from the end of the facing region of the electrode to the alkaline water flow path 6 side. Has become. Although this water passage 55 is schematically disclosed as a large gap in FIG. 1, it is actually determined by the thickness of the spacer 54 and is about 0.5 mm to several mm. Further, by providing the slit-shaped opening 53 in a part of the anode plate 52, only the water that passes in the vicinity of the anode plate 52 flows as acidic water from the opening 53 to the acidic water flow path 7, and the remaining water is alkaline water that is alkaline water. It flows to the water channel 6.
The water discharged from the alkaline water flow path 6 is drunk as alkaline ionized water.

【0012】なお、薬剤添加筒4内の薬剤は電解促進の
ためであるので水質条件等により電解促進の必要性のな
い場合は薬剤は空でも良い。同時に生成される酸性水は
酸性水流路から排出され、必要に応じてアストリンゼン
水として利用される。もちろん、電界強度や流量調節な
どでペーハー値を殺菌作用のある程度まで調節すること
も可能である。但し酸性水の取り扱いと同時に発生する
アルカリ度の高い水の誤飲に注意する必要がある。な
お、電磁弁Cは浄水カートリッジ2、電解槽5等に溜ま
った水を自然排水するためのボール弁であり、水圧のか
かっている状態では閉じられ、所定の水圧が無くなると
開き、酸性水流路7から水が排出されるようにしてい
る。
Since the chemical in the chemical addition cylinder 4 is for promoting electrolysis, the chemical may be empty when there is no need to promote electrolysis due to water quality conditions or the like. The acidic water produced at the same time is discharged from the acidic water flow path and used as astringent water as needed. Of course, it is also possible to adjust the pH value to some extent of the bactericidal action by adjusting the electric field strength and the flow rate. However, it is necessary to be careful of accidental ingestion of highly alkaline water that occurs at the same time as handling acidic water. The electromagnetic valve C is a ball valve for naturally draining water accumulated in the water purification cartridge 2, the electrolytic cell 5, etc., and is closed when water pressure is applied, and opens when the predetermined water pressure is lost, and the acidic water flow path is opened. Water is discharged from 7.

【0013】(次亜塩素酸水モード)本体の操作スイッ
チにより次亜塩素酸水が選択され分岐栓から水が流入さ
れると、制御部12により電磁弁Bが閉じられるととも
に電磁弁Aが開く。電磁弁Aが開かれることにより水は
浄水カートリッジ2から流量センサー3、薬剤添加筒4
を経て電解槽5へ流入される流路と電磁弁Aから食塩添
加筒8を経て電解槽5への流入前段で合流する流路に分
岐される。食塩添加筒8は図2に示すように下方から流
入され上部からプレート13を経て下方の食塩溜りへ到
達する。食塩は十分な量充填されているので食塩溜りを
通過した水は飽和濃度に達しており、したがって合流時
に流量の比を設定すれば正確な濃度を設定可能となる。
本実施例では合流直前にオリフィス15を設け流量制御
を行なっている。
(Hypochlorous acid water mode) When hypochlorous acid water is selected by the operation switch of the main body and water flows in from the branch plug, the control unit 12 closes the solenoid valve B and opens the solenoid valve A. . When the solenoid valve A is opened, water flows from the water purification cartridge 2 to the flow rate sensor 3 and the medicine addition cylinder 4.
Through the electromagnetic valve A to the salt addition cylinder 8 and then into the flow path that joins before entering the electrolytic cell 5. As shown in FIG. 2, the salt addition cylinder 8 is introduced from below and reaches the salt reservoir below through the plate 13 from the upper part. Since the salt is filled in a sufficient amount, the water that has passed through the salt reservoir has reached a saturated concentration, and therefore an accurate concentration can be set by setting the flow rate ratio at the time of merging.
In this embodiment, the flow rate is controlled by providing the orifice 15 immediately before the merging.

【0014】このように正確に濃度が調整された食塩水
が電解槽5へ流入され、食塩水が電解され、次亜塩素酸
水が生成される。本実施例では電解槽5を上述のような
構成の無隔膜方式としているため、電磁弁Bを閉じるの
みで電解槽5に負荷をかけることなく、全ての水が次亜
塩素酸水として電極間の偏りのない端部から排出され
る。この次亜塩素酸排出流路はアルカリ水流路6と同じ
流路になる。なお、次亜塩素酸モードは上記飲用アルカ
リ水モードの状態からに入ることが望ましく、特に強ア
ルカリ濃度選択の状態で数秒間通水した後、次亜塩素酸
モードとすれば次亜塩素酸の塩素濃度がアップすること
を知見した。したがって次亜塩素酸モードの選択時に自
動的に所定時間、飲用アルカリ水モードの強アルカリ選
択状態を実行されるように制御することが望ましい。具
体的には使用者が次亜塩素酸モードを選択すれば、制御
部12がまず電解槽5に強アルカリ濃度となるように電
圧を印加し、電磁弁Aが閉じられるとともに電磁弁Bが
開く。この状態を所定時間、例えば5秒間継続させ強ア
ルカリ水を生成する。その後電磁弁Aを開き電磁弁Bを
閉じ、食塩水が電解槽5へ流れ所定の電圧印加により次
亜塩素酸が生成され単一の出口から全て排出されるよう
にしている。
The salt solution whose concentration has been accurately adjusted as described above flows into the electrolytic cell 5 to electrolyze the salt solution to generate hypochlorous acid water. In this embodiment, since the electrolytic cell 5 is of the diaphragm-free type having the above-described structure, all the water is hypochlorous acid water between the electrodes without loading the electrolytic cell 5 only by closing the solenoid valve B. Is discharged from the flat end of the. This hypochlorous acid discharge channel is the same channel as the alkaline water channel 6. Incidentally, it is desirable that the hypochlorous acid mode be entered from the state of the drinking alkaline water mode, especially after passing water for several seconds in the state of selecting strong alkaline concentration, and if the hypochlorous acid mode is set, We found that the chlorine concentration increased. Therefore, it is desirable to control so that when the hypochlorous acid mode is selected, the strongly alkaline selected state of the drinking alkaline water mode is automatically executed for a predetermined time. Specifically, if the user selects the hypochlorous acid mode, the control unit 12 first applies a voltage to the electrolytic cell 5 so that the alkaline concentration becomes strong, and the solenoid valve A is closed and the solenoid valve B is opened. . This state is continued for a predetermined time, for example, 5 seconds to generate strong alkaline water. After that, the electromagnetic valve A is opened and the electromagnetic valve B is closed so that saline solution flows into the electrolytic cell 5 to generate hypochlorous acid by applying a predetermined voltage, and all the hypochlorous acid is discharged from a single outlet.

【0015】(浄水モード)本体の操作スイッチにより
浄水が選択され分岐栓から水が流入されると、制御部1
2により電磁弁A、Bのいずれもが閉じられる。電磁弁
A、Bが閉じられることにより水は浄水カートリッジか
ら流量センサー3、薬剤添加筒4を経て電解槽5へ流入
され上述のアルカリ水流路6からのみ排出される。この
時電解制御を行なわないように制御しているので浄水と
して飲用に適した水が排出される。本実施例では上述の
ように無隔膜の電解槽を採用しているので、隔膜付きの
電解槽のように一方の排出口が閉じられることによる圧
力差での隔膜の損傷がなくなる利点がある。この利点
は、次亜塩素酸水モードの場合にもいえる。
(Water purification mode) When water purification is selected by the operation switch of the main body and water flows in from the branch tap, the control unit 1
Both solenoid valves A and B are closed by 2. When the electromagnetic valves A and B are closed, water flows from the water purification cartridge into the electrolytic cell 5 through the flow rate sensor 3 and the chemical addition cylinder 4, and is discharged only from the alkaline water flow path 6 described above. At this time, electrolysis is controlled so that drinking water suitable for drinking is discharged as purified water. In this embodiment, since the electrolytic cell having no diaphragm is adopted as described above, there is an advantage that the diaphragm is not damaged by the pressure difference due to the closing of one of the outlets like the electrolytic cell with the diaphragm. This advantage is also applicable to the hypochlorous acid water mode.

【0016】以上説明したように本発明における電解水
生成装置は、陽極板52と陰極板51を備えた電解槽5
の上流側に浄水手段2と塩素イオン供給手段8を有し、
上記電解槽5の下流側に陽極板側52の水を排出する酸
性水流路7と陰極板側51の水を排出するアルカリ水流
路6を設けた電解水生成装置において、上記塩素イオン
供給手段8は電解槽5内に塩素イオンが供給される状態
と電解槽5内に塩素イオンが供給されない状態に切替え
自在であり、塩素イオンを電解槽5内に切り替えるのと
連動して電解槽5の下流側に設けられた酸性水流路7も
しくはアルカリ水流路6の少なくとも一方の流路が閉塞
され、電解槽5からの排水が全て単一の排出口から排出
されるように構成したので、一つの電解槽5で、飲用の
電解水と殺菌用の電解水のいずれをも簡単に自在に生成
可能となり、全体としての製造コストが低減できる効果
がある。特に飲用の電解水と殺菌用の電解水では添加す
る薬剤が異なるにも関わらず、各モード毎に確実に最適
な添加が実施されることになる点において効果的であ
る。また、請求項2に記載の構成によれば、次亜塩素酸
を生成時において、電極のスリット53からの流出が停
止されることになり、隔膜がないことと相まって、次亜
塩素酸生成専用の電解槽とほとんど同一の構成を得ら
れ、電極間の偏りのない位置から排出され極めて効果的
に次亜塩素酸が生成可能となる効果がある。更には、請
求項3に記載の構成によれば、食塩水の供給のために添
加筒4と電磁弁Aの構成を追加するのみで良いため、従
来のようなポンプ手段を必要とせず、故障の虞を可及的
に減少させ、コスト的にも有利となる。
As described above, in the electrolyzed water producing apparatus of the present invention, the electrolytic cell 5 having the anode plate 52 and the cathode plate 51 is provided.
Has a water purification means 2 and a chlorine ion supply means 8 on the upstream side of
In the electrolyzed water generating apparatus, which is provided with an acidic water flow path 7 for discharging water on the anode plate side 52 and an alkaline water flow path 6 for discharging water on the cathode plate side 51 on the downstream side of the electrolytic cell 5, the chlorine ion supply means 8 is used. Can be switched between a state where chlorine ions are supplied to the electrolytic cell 5 and a state where chlorine ions are not supplied to the electrolytic cell 5. Downstream of the electrolytic cell 5 in conjunction with switching chlorine ions into the electrolytic cell 5. At least one of the acidic water flow path 7 and the alkaline water flow path 6 provided on the side is closed so that all the drainage water from the electrolysis tank 5 is discharged from a single discharge port. In the tank 5, both the electrolytic water for drinking and the electrolytic water for sterilization can be easily and freely generated, and the manufacturing cost as a whole can be reduced. In particular, it is effective in that the optimum addition is surely carried out for each mode, although the chemicals to be added are different between the electrolytic water for drinking and the electrolytic water for sterilization. Further, according to the configuration of claim 2, when hypochlorous acid is produced, the outflow from the slit 53 of the electrode is stopped, which is combined with the absence of the diaphragm, and therefore is exclusively for hypochlorous acid production. Almost the same structure as that of the electrolytic cell can be obtained, and there is an effect that hypochlorous acid can be generated very effectively by being discharged from a position where there is no bias between the electrodes. Further, according to the configuration of claim 3, since it is only necessary to add the configuration of the addition cylinder 4 and the solenoid valve A for supplying the saline solution, a pump means unlike the conventional one is not required, and a malfunction occurs. The risk of occurrence is reduced as much as possible, which is advantageous in terms of cost.

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

【図1】この発明の実施の形態を示す電解水供給装置の
システム構成図である。
FIG. 1 is a system configuration diagram of an electrolyzed water supply device showing an embodiment of the present invention.

【図2】この発明の実施例における食塩添加筒を説明し
た本体の一部断面図である。
FIG. 2 is a partial cross-sectional view of the main body explaining the salt addition cylinder in the embodiment of the present invention.

【図3】この発明の実施例における電解槽を説明した斜
視図である。
FIG. 3 is a perspective view illustrating an electrolytic cell according to an embodiment of the present invention.

【図4】この発明の実施例における食塩添加筒を説明し
た斜視図である。
FIG. 4 is a perspective view illustrating a salt addition cylinder according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

2・・・浄水カートリッジ 5・・・電解槽 8・・・食塩添加筒 A,B・・・電磁弁 2 ... Water purification cartridge 5 ... Electrolytic bath 8 ... Salt addition cylinder A, B ... Solenoid valve

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 陽極板と陰極板を備えた電解槽の上流側
に浄水手段と塩素イオン供給手段を有し、上記電解槽の
下流側に陽極板側の水を排出する酸性水流路と陰極板側
の水を排出するアルカリ水流路を設けた電解水生成装置
において、上記塩素イオン供給手段は電解槽内に塩素イ
オンが供給される状態と電解槽内に塩素イオンが供給さ
れない状態に切替え自在であり、塩素イオンを電解槽内
に供給する状態に切り替えるのと連動して電解槽の下流
側に設けられた酸性水流路もしくはアルカリ水流路の少
なくとも一方の流路が実質的に閉塞され、電解槽からの
排水が全て単一の排出口から排出されることを特徴とす
る電解水生成装置。
1. An acidic water flow path and a cathode for discharging water on the anode plate side to the downstream side of the electrolytic cell, which has a water purification means and a chlorine ion supply means on the upstream side of the electrolytic cell equipped with the anode plate and the cathode plate. In the electrolyzed water generator provided with an alkaline water flow path for discharging water on the plate side, the chlorine ion supply means can be switched between a state in which chlorine ions are supplied in the electrolytic cell and a state in which no chlorine ions are supplied in the electrolytic cell. That is, at least one of the acidic water channel and the alkaline water channel provided on the downstream side of the electrolytic cell is substantially closed in conjunction with switching to the state of supplying chlorine ions into the electrolytic cell, and electrolysis is performed. An electrolyzed water generator characterized in that all wastewater from the tank is discharged from a single outlet.
【請求項2】 上記電解槽は陽極板と陰極板を対向させ
その間に水を通す無隔膜式とし、酸性水流路は陽極板に
形成されたスリット状の開口と連通せしめ、アルカリ性
流路は対向電極間の端部からの排出口と連通させるとと
もに、上記酸性流路の途中に閉塞自在な電磁弁を設けた
ことを特徴とする請求項1に記載の電解水生成装置。
2. The electrolytic cell is of a non-diaphragm type in which an anode plate and a cathode plate are opposed to each other and water is allowed to pass between them, an acidic water flow path is communicated with a slit-shaped opening formed in the anode plate, and an alkaline flow path is opposed to each other. The electrolyzed water generating apparatus according to claim 1, wherein a solenoid valve that is in communication with an outlet from an end portion between the electrodes and that can be closed is provided in the middle of the acidic flow path.
【請求項3】 上記塩素イオン供給手段は食塩が収納さ
れた食塩添加筒であり、電解槽内に塩素イオンが供給さ
れる状態と電解槽内に塩素イオンが供給されない状態の
切替えは、食塩添加筒を含む流路の流れを開閉する電磁
弁により行なうことを特徴とする請求項1または2記載
の電解生成装置。
3. The chlorine ion supply means is a salt addition cylinder containing salt, and switching between a state in which chlorine ions are supplied in the electrolytic cell and a state in which no chlorine ions are supplied in the electrolytic cell is performed by adding salt. The electrolysis generating apparatus according to claim 1 or 2, wherein the flow is performed by a solenoid valve that opens and closes the flow path including the cylinder.
JP2002038227A 2002-02-15 2002-02-15 Electrolyzed water generator Expired - Fee Related JP4002594B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002038227A JP4002594B2 (en) 2002-02-15 2002-02-15 Electrolyzed water generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002038227A JP4002594B2 (en) 2002-02-15 2002-02-15 Electrolyzed water generator

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2004077312A Division JP2004202495A (en) 2004-03-18 2004-03-18 Electrolytic water generator

Publications (2)

Publication Number Publication Date
JP2003236548A true JP2003236548A (en) 2003-08-26
JP4002594B2 JP4002594B2 (en) 2007-11-07

Family

ID=27779595

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002038227A Expired - Fee Related JP4002594B2 (en) 2002-02-15 2002-02-15 Electrolyzed water generator

Country Status (1)

Country Link
JP (1) JP4002594B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100853347B1 (en) 2007-04-23 2008-08-21 (주)에이엠티기술 Sterilized water manufacturing apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100853347B1 (en) 2007-04-23 2008-08-21 (주)에이엠티기술 Sterilized water manufacturing apparatus

Also Published As

Publication number Publication date
JP4002594B2 (en) 2007-11-07

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