JPH0244909B2 - - Google Patents

Info

Publication number
JPH0244909B2
JPH0244909B2 JP62117770A JP11777087A JPH0244909B2 JP H0244909 B2 JPH0244909 B2 JP H0244909B2 JP 62117770 A JP62117770 A JP 62117770A JP 11777087 A JP11777087 A JP 11777087A JP H0244909 B2 JPH0244909 B2 JP H0244909B2
Authority
JP
Japan
Prior art keywords
water
electrode body
gap
electrode
titanium
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.)
Expired - Lifetime
Application number
JP62117770A
Other languages
Japanese (ja)
Other versions
JPS63282286A (en
Inventor
Minoru Tamura
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.)
SHIBA KENZABURO
Original Assignee
SHIBA KENZABURO
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 SHIBA KENZABURO filed Critical SHIBA KENZABURO
Priority to JP62117770A priority Critical patent/JPS63282286A/en
Publication of JPS63282286A publication Critical patent/JPS63282286A/en
Publication of JPH0244909B2 publication Critical patent/JPH0244909B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Landscapes

  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、チタンからなる筒状基体の内面に二
酸化イリジウム又は白金をコーテイングした第1
の電極体を用いることを基本として、酸性水の生
成率を向上しうる水電解槽に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention provides a first method in which the inner surface of a cylindrical substrate made of titanium is coated with iridium dioxide or platinum.
The present invention relates to a water electrolyzer that can improve the production rate of acidic water based on the use of an electrode body.

〔背景技術〕[Background technology]

従来、水の電気分解により得られるアルカリ性
水が、胃腸の強化、健康維持に効果的であるとと
もに酸化防止作用を有することが知られており、
例えば飲料用、豆腐等の食料品の長期保存用とし
て用いられる他、酸性水も、その酸化作用による
漂白、殺菌効果によつて化粧用、洗顔用の他、食
器類等の洗浄に用いられてきた。さらに製麺等に
用いるときには、麺体の溶出を防いで歩止まりを
向上しうる他、防腐効果によつて薬剤の使用を減
じうることも知られている。
It has been known that alkaline water obtained through water electrolysis is effective for strengthening the gastrointestinal tract and maintaining health, as well as having antioxidant effects.
For example, in addition to being used for beverages and for long-term preservation of foodstuffs such as tofu, acidic water is also used for cosmetics, face washing, and washing tableware due to its bleaching and sterilizing effects due to its oxidizing action. Ta. Furthermore, when used in noodle making, etc., it is known that not only can the elution of noodle bodies be prevented to improve the yield, but also that the use of chemicals can be reduced due to the preservative effect.

しかし、近年、この酸性水は、例えば、皮膚病
の治癒、防止効果及び水のにごりを低減しうる効
果等とあいまつてプール、風呂等の水としての使
用が望まれる他、ビール、清涼飲料水等の容器、
食器類の殺菌等、工業用洗浄水としての需要も高
まつている。
However, in recent years, this acidic water has been desired to be used as water for pools, baths, etc. due to its effects on curing and preventing skin diseases, as well as its ability to reduce water turbidity. containers such as
Demand for industrial cleaning water, such as for sterilizing tableware, is also increasing.

一方、このようなアルカリ性水、酸性水の生成
には、例えばカーボン、ニツケルフエライトなど
の棒状陽電極と、ステンレス等の不錆金属からな
りかつ陽電極に外挿される円筒状陰電極との間
に、イオン交換膜を介在させた水電解槽が従来か
ら用いられており、該電極間に清水を流過させつ
つ電気分解することによりイオン交換膜である隔
膜内側即ち陽極側に酸性水を、又外側即ち陰極側
にアルカリ性水を生成していた。
On the other hand, in order to generate such alkaline water and acidic water, it is necessary to use a method between a rod-shaped positive electrode made of carbon, nickel ferrite, etc., and a cylindrical negative electrode made of rust-free metal such as stainless steel and inserted into the positive electrode. A water electrolyzer with an ion-exchange membrane interposed therein has been conventionally used, and by electrolyzing fresh water while flowing between the electrodes, acidic water is supplied to the inside of the diaphragm, which is the ion-exchange membrane, that is, on the anode side. Alkaline water was generated on the outside, that is, on the cathode side.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしこのような水電解槽においては、酸性水
のアルカリ性水に対する生成率を増加することが
できないという欠点があつた。
However, such water electrolyzers have a drawback in that the production rate of acidic water relative to alkaline water cannot be increased.

その原因としては、 例えば隔膜内側を流過する酸性水の流量を、
外側を流過するアルカリ性水の流量に比して増
加させた場合、前記流量の増加即ち流速の増加
とともに隔膜内側の内圧が減少し、従つてこの
内外の圧力差によつて隔膜は内方へ押圧される
こととなる。さらに酸性水取出口は、アルカリ
性水取出口との位置関係により水電解槽中央付
近に設けられるため、酸性水は、取出口近傍で
中央側に向かう流線を描き、従つて隔膜を内方
に引つ張ることとなる。
The cause of this is, for example, the flow rate of acidic water flowing inside the diaphragm.
When the flow rate of alkaline water is increased compared to the flow rate of alkaline water flowing outside, the internal pressure inside the diaphragm decreases as the flow rate increases, that is, the flow velocity increases, and this pressure difference between the inside and outside causes the diaphragm to move inward. You will be under pressure. Furthermore, because the acidic water outlet is provided near the center of the water electrolyzer due to its positional relationship with the alkaline water outlet, the acidic water draws a streamline toward the center near the outlet, thus pushing the diaphragm inward. It will be a drag.

又各電極間距離の限界値、即ち放電可能距離
は、一般に7mm程度と比較的小寸であり、従つ
てその内部に介在する隔膜は、各電極と近接し
て配されることとなる。さらに隔膜は、円筒状
のシート体であり、剛性が弱く、従つて前記し
た圧力差、水流等による外力によつて内方へ変
形しやすく、例えば陽電極と接触、シヨートし
た際には、電極の劣化を招来しその寿命を短命
化する。
Further, the limit value of the distance between each electrode, that is, the dischargeable distance is generally relatively small, about 7 mm, and therefore the diaphragm interposed inside the diaphragm is disposed close to each electrode. Furthermore, the diaphragm is a cylindrical sheet body and has low rigidity, so it is easily deformed inward by external forces such as the above-mentioned pressure difference and water flow. lead to deterioration and shorten its lifespan.

一方、逆に、隔膜外側圧力を減少させること
は隔膜を張設でき、前記シヨート防止に効果的
であるため、隔膜外側の流量を増加しかつ前記
陽電極側に負電圧を又陰電極側に正電圧を印加
することが考えられうる。
On the other hand, on the other hand, reducing the pressure outside the diaphragm allows the diaphragm to be stretched and is effective in preventing the shoot, so it increases the flow rate outside the diaphragm and applies a negative voltage to the positive electrode side and to the negative electrode side. It is conceivable to apply a positive voltage.

しかし、 従来の陰電極即ちステンレス側に正電圧を印
加した場合、ステンレスはその表面が酸化さ
れ、耐久性を減じることとなるばかりか、含有
するクロムを溶出する傾向があり、健康上問題
となる場合もある。
However, when a positive voltage is applied to the conventional negative electrode, i.e., the stainless steel side, the surface of the stainless steel becomes oxidized, reducing its durability and also tends to elute the chromium it contains, which poses a health problem. In some cases.

又、ステンレスによつて棒状陰電極を又カー
ボン、ニツケルフエライトによつて円筒状陽電
極を形成することも考えられるが、カーボン、
ニツケルフエライトは、陶器状であり、割れや
すく、加工が困難であり、又焼付収縮等により
精度も一定せず、従つてこのような電極は形成
し難い。
It is also possible to form a rod-shaped negative electrode with stainless steel and a cylindrical positive electrode with carbon or nickel ferrite;
Nickel ferrite is ceramic-like, easily cracked, difficult to process, and has inconsistent precision due to shrinkage due to baking, etc., and therefore it is difficult to form such an electrode.

このように、従来の水電解槽においては、その
電極の劣化防止のため、隔膜内側の流量を増加で
きず又、加工性に富みさらに放電効果が良くかつ
人体に無害な陽電極体を形成しえなかつたため、
酸性水の生成率を増加できず、時にアルカリ性水
の余剰生成を招きコストの上昇を招来していた。
As described above, in conventional water electrolyzers, it is not possible to increase the flow rate inside the diaphragm in order to prevent deterioration of the electrode, and it is difficult to form a positive electrode body that is easy to process, has a good discharge effect, and is harmless to the human body. Because it was not possible,
It was not possible to increase the production rate of acidic water, which sometimes led to excessive production of alkaline water, leading to an increase in costs.

〔発明の目的〕[Purpose of the invention]

本発明は、チタンからなる筒状基体の内面に二
酸化イリジウム又は白金をコーテイングした第1
の電極体に正電圧を印加することを基本として、
構成簡易にかつ安定して酸性水の生成率を向上で
き、アルカリ性水の余剰生成を防止でき、生産コ
ストの低減、省資源化にも寄与しうる水電解槽の
提供を目的としている。
The present invention provides a first method in which the inner surface of a cylindrical substrate made of titanium is coated with iridium dioxide or platinum.
Basically, applying a positive voltage to the electrode body of
The object of the present invention is to provide a water electrolyzer that can easily and stably improve the production rate of acidic water, prevent excessive production of alkaline water, and contribute to reducing production costs and saving resources.

〔問題点を解決するための手段〕[Means for solving problems]

以下本発明の一実施例を図面に基づき説明す
る。
An embodiment of the present invention will be described below based on the drawings.

図において、水電解槽1は、チタンからなる筒
状の基体2内面に二酸化イリジウム又は白金をコ
ーテイングした第1の電極体3の内部に、該第1
の電極体3の内面から水流過用間隙5を隔てて前
記第1の電極体3と平行に第2の電極体6を挿入
するとともに、前記第1の電極体3に正電圧を印
加している。
In the figure, a water electrolyzer 1 has a first electrode body 3 in which the inner surface of a cylindrical base body 2 made of titanium is coated with iridium dioxide or platinum.
A second electrode body 6 is inserted from the inner surface of the electrode body 3 in parallel with the first electrode body 3 across a water flow gap 5, and a positive voltage is applied to the first electrode body 3. There is.

第1の電極体3は、チタンからなる円筒状の基
体2を具え、その外周面には導電性のネジ部材か
らなる接続端子12が溶着されるとともに、その
内面には本例では二酸化イリジウムがコーテイン
グされる。なお二酸化イリジウムは、吹付、刷毛
ぬり等により基体2内面に塗布された後焼付処理
が施される。
The first electrode body 3 includes a cylindrical base body 2 made of titanium, and a connecting terminal 12 made of a conductive screw member is welded to the outer peripheral surface of the base body 2, and in this example, iridium dioxide is attached to the inner surface of the base body 2. coated. Note that iridium dioxide is applied to the inner surface of the base 2 by spraying, brushing, etc., and then subjected to a baking treatment.

第2の電極体6は、本例では、両端の開口部を
円板体13,13で封止された中空状基筒15を
具え、各円板体13にはその中心に、先端に外ネ
ジを螺刻する芯軸16が突設される。
In this example, the second electrode body 6 includes a hollow base tube 15 whose openings at both ends are sealed with disk bodies 13, 13, and each disk body 13 has a central part and an outer part at the tip. A core shaft 16 for threading a screw is provided protrudingly.

なお、前記円板体13,13、基筒15、芯軸
16,16は、夫々チタン材からなり、アルゴン
ガス溶接によつて一体かつ密封状に固着されると
ともに、その周囲には、二酸化イリジウムがコー
テイングされる。
The disk bodies 13, 13, the base tube 15, and the core shafts 16, 16 are each made of titanium material, and are fixed integrally and hermetically by argon gas welding, and around them are covered with iridium dioxide. is coated.

又第2の電極体6は、その外径を前記第1の電
極体3内径に比して小寸に形成され、前記第1の
電極体3内部に第1の電極体3と同芯かつ平行に
挿入することにより、基体2、基筒15間に間隙
5を形成するとともに、その両端は、蓋部材1
9,20により閉止される。
Further, the second electrode body 6 is formed with an outer diameter smaller than the inner diameter of the first electrode body 3, and has an inner diameter that is concentric with the first electrode body 3 and inside the first electrode body 3. By inserting them in parallel, a gap 5 is formed between the base body 2 and the base cylinder 15, and both ends thereof are connected to the lid member 1.
It is closed by 9 and 20.

蓋部材19,20は、カバー体21,22とそ
の内端に夫々取付く保持板23,24とからな
る。
The lid members 19, 20 consist of cover bodies 21, 22 and retaining plates 23, 24 attached to the inner ends thereof, respectively.

保持板23,24は、前記芯軸16を貫通する
中心孔を設ける円筒状をなしかつ該中心孔の周囲
には、通水孔25が透設するとともに、外周面に
は凹溝26が周設される。又保持板23,24の
外径は、前記第2の電極体6の外径よりも大かつ
第1の電極体3の内径よりも小に設定され、又一
方の保持板23は、その下面に凸設するボス部2
7を第2の電極体6上端と当接して又他方の保持
板24は、第2の電極体6下端間にシリコンゴム
などの弾性リング29を介在させて配置される。
The holding plates 23 and 24 have a cylindrical shape with a center hole passing through the core shaft 16, and a water passage hole 25 is provided around the center hole, and a groove 26 is formed on the outer peripheral surface. will be established. Further, the outer diameters of the holding plates 23 and 24 are set to be larger than the outer diameter of the second electrode body 6 and smaller than the inner diameter of the first electrode body 3, and one of the holding plates 23 has a lower surface. Boss part 2 protruding from
7 is placed in contact with the upper end of the second electrode body 6, and the other holding plate 24 is disposed with an elastic ring 29 made of silicone rubber or the like interposed between the lower end of the second electrode body 6.

又保持板23,24間には、本例では、その外
周面に取付き、前記基筒15を囲む隔筒31が設
けられ、前記間隙5を内間隙部5A、外間隙部5
Bに区分しかつ外間隙部5Bには内間隙部5Aに
比して多量の水を流過させる。なお隔筒31は、
弾性リング29を圧縮した状態にて前記凹溝26
に巻装する紐体等を用いて緊縛され、従つて弾性
リング29の反発とともに、該隔筒31は張設さ
れる。なお隔筒31は、水の電解によつて生じる
イオンを通過させる反面、水分子の透過を妨げる
不織布等のいわゆるイオン交換用の膜が用いられ
る。
Further, in this example, a partition 31 is provided between the holding plates 23 and 24, and is attached to the outer peripheral surface thereof and surrounds the base cylinder 15.
A larger amount of water is allowed to flow through the outer gap 5B than the inner gap 5A. Note that the partition cylinder 31 is
When the elastic ring 29 is compressed, the groove 26
The partition tube 31 is tightened using a string or the like wrapped around the tube, and the partition tube 31 is stretched as a result of the repulsion of the elastic ring 29. Note that the partition tube 31 is made of a so-called ion exchange membrane such as a nonwoven fabric that allows ions generated by electrolysis of water to pass through but prevents water molecules from passing through.

前記カバー体21,22は、円形の基板33の
周囲に、前記第1の電極体3を嵌入する段差35
を有する周壁36を設けたキヤツプ状をなし、基
板33の中心には、前記芯軸16の先端部を挿通
する孔部を有するボス37を突設している。
The cover bodies 21 and 22 have a step 35 around a circular substrate 33 into which the first electrode body 3 is fitted.
The base plate 33 has a cap shape with a peripheral wall 36 having a circumferential wall 36, and a boss 37 protruding from the center of the base plate 33. The boss 37 has a hole through which the tip of the core shaft 16 is inserted.

又カバー体21,22は、前記段差35外方に
設ける内周溝に嵌合するOリングにより、前記第
1の電極体3を水蜜しつつ該第1の電極体3を嵌
着するとともに、前記ボス37をへて基板33か
ら突出する芯軸16の外ネジに、例えばナツトで
あるナツト金具39を螺締することによりカバー
体21,22は前記段差35を第1の電極体3端
面に押付けられて取付けられる。
Further, the cover bodies 21 and 22 fit the first electrode body 3 while keeping the first electrode body 3 moist by an O-ring that fits into an inner circumferential groove provided on the outside of the step 35, and By screwing a nut fitting 39, for example, a nut, onto the outer thread of the core shaft 16 that protrudes from the substrate 33 through the boss 37, the cover bodies 21, 22 can attach the step 35 to the end surface of the first electrode body 3. It is pressed and installed.

又下方のカバー体22は、前記周壁36とボス
37との間で前記通水孔25をへて内間隙部5A
に通じるとともに又隔筒31と第1の電極体3と
の間をへて外間隙部5Bにも導通する流入路40
が形成され、又流入路40は、周壁36に螺着す
るエルボ41に連通する。
Further, the lower cover body 22 passes through the water passage hole 25 between the peripheral wall 36 and the boss 37 to form an inner gap 5A.
An inflow path 40 that communicates with the outer gap 5B through the space between the partition tube 31 and the first electrode body 3.
is formed, and the inlet passage 40 communicates with an elbow 41 screwed into the peripheral wall 36.

他方のカバー体21は、第3図に示すごとく、
前記周壁36とボス37との間に中壁42を設け
ており、又中壁42は、カバー体22の取付けと
ともに前記保持板23の外周縁でその端面が当接
する。従つて、ボス37と中壁42との間は、通
水孔25をへて前記内間隙部5Aに通じる内流路
45を形成でき、又中壁42と周壁36との間
は、隔筒31と第1の電極体3との間で外間隙部
5Bに通じる外流路46を夫々独立して構成す
る。なお外流路46は周壁36に螺着するエルボ
47に導通し、又内流路45は、中壁42と周壁
36とを継ぐ橋絡片49を通りかつ中壁42で開
口する導孔に螺着するエルボ48に通じている。
The other cover body 21 is, as shown in FIG.
An intermediate wall 42 is provided between the peripheral wall 36 and the boss 37, and the end surface of the intermediate wall 42 comes into contact with the outer peripheral edge of the retaining plate 23 when the cover body 22 is attached. Therefore, between the boss 37 and the inner wall 42, an inner flow path 45 can be formed which passes through the water passage hole 25 and communicates with the inner gap 5A, and between the inner wall 42 and the peripheral wall 36, a partition can be formed. 31 and the first electrode body 3, an outer flow path 46 communicating with the outer gap 5B is independently configured. The outer flow path 46 is connected to an elbow 47 screwed into the peripheral wall 36, and the inner flow path 45 passes through a bridge piece 49 connecting the inner wall 42 and the peripheral wall 36 and is screwed into a guide hole opened in the inner wall 42. It leads to elbow 48 where it will be worn.

なお、水電解槽1には、第1の電極体3に溶着
する接続端子12に電源ボツクスからのびる正電
極側の電気コード51が端金具を用いてネジ止め
され、又前記芯軸16上端には、芯軸16に外挿
されかつナツト52により挟圧される端金具を用
いて電源ボツクスからのびる負電極側の電気コー
ド53が導通される。なお第1の電極体3、第2
の電極体6間には例えば30V〜100Vの直流電圧
が印加される。又本例では、芯軸16上端側に一
方の電気コード53を接続することにより、基体
2表面に付着する露が該接続部へ滴下するのを防
止している。
In addition, in the water electrolyzer 1, an electric cord 51 on the positive electrode side extending from the power supply box is screwed to the connection terminal 12 welded to the first electrode body 3 using an end fitting. An electrical cord 53 on the negative electrode side extending from the power supply box is electrically connected using an end fitting that is inserted over the core shaft 16 and compressed by a nut 52. Note that the first electrode body 3, the second
For example, a DC voltage of 30V to 100V is applied between the electrode bodies 6. Further, in this example, by connecting one of the electric cords 53 to the upper end side of the core shaft 16, dew attached to the surface of the base body 2 is prevented from dripping to the connecting portion.

又水電解槽1には、例えば浄水器を介して、本
例では、水道管である水供給源に連通する。
The water electrolyzer 1 is also connected to a water supply source, which is a water pipe in this example, via a water purifier, for example.

浄水器は例えば、内部に活性炭、亜硫酸カルシ
ウム等を収納した周知構成の濾過器であり、送給
される水道水などの清水を清浄化しつつ前記エル
ボ41を介して水電解槽1に清水を供給する。
The water purifier is, for example, a filter with a well-known configuration that stores activated carbon, calcium sulfite, etc. inside, and supplies clean water to the water electrolyzer 1 through the elbow 41 while purifying clean water such as tap water that is being fed. do.

なお、浄水器、水道管間には開閉弁が介在し、
前記清水の送給を入、切するとともに、前記エル
ボ47,48は、周知構成の調量弁を介して夫々
アルカリ性水取出口、酸性水取出口に連通する。
In addition, there is an on-off valve between the water purifier and the water pipes.
In addition to turning on and off the fresh water supply, the elbows 47 and 48 communicate with an alkaline water outlet and an acidic water outlet, respectively, via metering valves of well-known construction.

なお、例えば酸性水側のエルボ47と蛇口との
間にフロースイツチ(図示せず)を設けるととも
に、アルカリ性水側のエルボ48には、該フロー
スイツチにより開閉する電磁バルブを設けること
もできる。そのとき、酸性水の取出しと同時にア
ルカリ性水の排出が可能とする。又フロースイツ
チの作動によつて電解用の電源スイツチをON
し、第1、第2の電極3,6に電圧を印加する。
なお、そのとき清水取入れ用のエルボ41には、
清水供給管、例えば水道管を逆流防止弁を介して
直結させておく。
For example, a flow switch (not shown) may be provided between the elbow 47 on the acidic water side and the faucet, and an electromagnetic valve that is opened and closed by the flow switch may be provided on the elbow 48 on the alkaline water side. At this time, alkaline water can be discharged at the same time as acidic water is taken out. Also, turn on the power switch for electrolysis by operating the flow switch.
Then, a voltage is applied to the first and second electrodes 3 and 6.
In addition, at that time, in the elbow 41 for fresh water intake,
A fresh water supply pipe, such as a water pipe, is directly connected via a backflow prevention valve.

〔作用〕[Effect]

然して、水道水は、開閉弁の開放により浄水器
に流れ込み、濾過、清浄化されたのちエルボ41
をへて流入路40に流入する。又調量弁は、内間
隙部5A、外間隙部5Bを夫々流過する水の流量
比が、例えば1:5になるごとく調節され、従つ
て流入路40を通る水は、前記所望する流量比に
応じてその流速を変化しつつ夫々内間隙部5A,
外間隙部5Bを上昇する。
However, tap water flows into the water purifier by opening the on-off valve, is filtered and purified, and then passes through the elbow 41.
It flows into the inflow path 40 through the flow path. Further, the metering valve adjusts the flow rate ratio of the water flowing through the inner gap 5A and the outer gap 5B to, for example, 1:5, so that the water flowing through the inflow path 40 has the desired flow rate. While changing the flow velocity according to the ratio, the inner gap portion 5A,
The outer gap 5B is raised.

又、内、外間隙部5A,5B間を流れる水は第
1の電極体3、第2の電極体6間に印加される電
圧により電気分解され正電圧が印加される第1の
電極体3側即ち外間隙部5Bには酸性水が又内間
隙部5Aにはアルカリ性水が夫々生成される。
Further, the water flowing between the inner and outer gaps 5A and 5B is electrolyzed by the voltage applied between the first electrode body 3 and the second electrode body 6, and the first electrode body 3 to which a positive voltage is applied is Acidic water is generated in the side, ie, outer gap 5B, and alkaline water is generated in the inner gap 5A.

なお生成に際しては、外間隙部5B内が、前記
酸性水の流速の増加に伴い減圧されるため、隔筒
31は半径方向外側に向かつて張設され、従つて
水電解槽1は、隔筒31を夫々の電極体36に接
触させることなく、安定して水を電気分解でき
る。
Note that during generation, the pressure inside the outer gap 5B is reduced as the flow rate of the acidic water increases, so the partition 31 is stretched outward in the radial direction, and therefore the water electrolyzer 1 is Water can be stably electrolyzed without bringing 31 into contact with each electrode body 36.

なおチタンは、陽電極として単体で用いた場
合、通常その表面に酸化皮膜を形成し、絶縁され
うるが、本発明の水電解槽1は、二酸化イリジウ
ムでコーテイングしているため、陽電極として好
適に使用しうる。
Note that when titanium is used alone as a positive electrode, it usually forms an oxide film on its surface and can be insulated, but the water electrolyzer 1 of the present invention is coated with iridium dioxide, so it is suitable as a positive electrode. It can be used for

さらにチタンは、ステンレス等と異なり、電流
とともに表面に非導電性の酸化膜を形成し、チタ
ン自体の溶出を生じることがない。従つて、安全
性を高めうる。さらに二酸化イリジウム、白金等
の層部が剥離したときにも、剥離個所で前記した
チタンの酸化皮膜が形成されることにより、侵触
を防止できる。
Furthermore, unlike stainless steel and the like, titanium forms a non-conductive oxide film on its surface with electric current, and titanium itself does not elute. Therefore, safety can be improved. Furthermore, even when the layer portion of iridium dioxide, platinum, etc. is peeled off, the above-mentioned titanium oxide film is formed at the peeled portion, thereby preventing the layer from being attacked.

なお第1の電極体3は、二酸化イリジウムの他
白金を使用でき、かかる場合、メツキ、蒸着、メ
タリコン等により基体2内面にコーテイングしう
る。
In addition to iridium dioxide, platinum can be used for the first electrode body 3, and in such a case, the inner surface of the base body 2 can be coated by plating, vapor deposition, metallic coating, or the like.

又第2の電極体6としては、第1の電極体同様
白金によつてコーテイングするのもよく、又例え
ば、カーボン、ニツケルフエライトからなる従来
の電極体を用いることもできる他、さらにはステ
ンレスからなる軸体を用いるのもよい。
The second electrode body 6 may be coated with platinum like the first electrode body, or may be a conventional electrode body made of carbon, nickel ferrite, or even made of stainless steel. It is also good to use a shaft body of

〔発明の効果〕〔Effect of the invention〕

叙上のごとく、本発明の水電解槽は、チタンか
らなる筒状基体の内面に二酸化イリジウム又は白
金をコーテイングした第1の電極体に正電圧を印
加するため、隔筒外側を流過する水の流量を内側
に比して増加させることにより、隔筒を第1の電
極体及び第2の電極体に接触させることなく簡易
に酸性水の生成率を向上でき、酸性水とともに得
られるアルカリ性水の余剰生成を防止しうる。
As mentioned above, the water electrolyzer of the present invention applies a positive voltage to the first electrode body, which is made of a cylindrical base made of titanium and whose inner surface is coated with iridium dioxide or platinum. By increasing the flow rate compared to the inside, the production rate of acidic water can be easily improved without bringing the septum into contact with the first electrode body and the second electrode body, and the alkaline water obtained together with the acidic water can be can prevent surplus generation.

又隔筒を設けず、さらに第2の電極体をチタン
を母材としかつ表面に三酸化イリジウム又は白金
をコーテイングしたもので形成した場合、又はカ
ーボン、ニツケルフエライトで形成した場合に
は、第1の電極体、第2の電極体間に交流電圧を
印加することによつて、電解とともに活性水を連
続的に生成しうる。又交流電圧を印加するときに
は、スケールの発生を防止しうるなど本発明の水
電解槽は多くの効果を奏しうる。
In addition, if no partition is provided and the second electrode body is made of titanium as a base material and coated with iridium trioxide or platinum on the surface, or if it is made of carbon or nickel ferrite, the first electrode body By applying an alternating current voltage between the electrode body and the second electrode body, active water can be continuously generated along with electrolysis. Further, when applying an alternating current voltage, the water electrolyzer of the present invention can exhibit many effects such as being able to prevent the generation of scale.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例を示す断面図、第2
図はその分解斜視図、第3図は蓋部材を示す一部
を断面した平面図、第4図は本発明の他の実施例
を示す断面図である。 2……基体、3……第1の電極体、5……間
隙、6……第2の電極体。
FIG. 1 is a cross-sectional view showing one embodiment of the present invention, and FIG.
The figure is an exploded perspective view, FIG. 3 is a partially sectional plan view showing the lid member, and FIG. 4 is a sectional view showing another embodiment of the present invention. 2... Base body, 3... First electrode body, 5... Gap, 6... Second electrode body.

Claims (1)

【特許請求の範囲】[Claims] 1 チタンからなる筒状の基体の内面に二酸化イ
リジウム又は白金をコーテイングした第1の電極
体の内部に、該第1の電極体の内面から水流過用
の間隙を隔てて前記第1の電極体と平行に第2の
電極体を挿入しかつ前記間隙に、該間隙を第2の
電極側の内間隙部と、第1の電極側の外間隙部と
に区分するイオン交換用の膜からなる隔筒を設け
るとともに、前記第1の電極体に正電圧を印加し
しかも前記内間隙部に比して外間隙部を流れる水
量を大とすることにより酸性水の生成率を高める
ことを特徴とする水電解槽。
1. The first electrode body is placed inside a first electrode body whose inner surface is coated with iridium dioxide or platinum on the inner surface of a cylindrical base made of titanium, with a gap for water flow separated from the inner surface of the first electrode body. A second electrode body is inserted in parallel with the ion exchange membrane, and the gap is divided into an inner gap on the second electrode side and an outer gap on the first electrode side. The invention is characterized by providing a partition, applying a positive voltage to the first electrode body, and increasing the amount of water flowing through the outer gap compared to the inner gap to increase the production rate of acidic water. water electrolyzer.
JP62117770A 1987-05-13 1987-05-13 Electrolytic cell for water Granted JPS63282286A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62117770A JPS63282286A (en) 1987-05-13 1987-05-13 Electrolytic cell for water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62117770A JPS63282286A (en) 1987-05-13 1987-05-13 Electrolytic cell for water

Publications (2)

Publication Number Publication Date
JPS63282286A JPS63282286A (en) 1988-11-18
JPH0244909B2 true JPH0244909B2 (en) 1990-10-05

Family

ID=14719892

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62117770A Granted JPS63282286A (en) 1987-05-13 1987-05-13 Electrolytic cell for water

Country Status (1)

Country Link
JP (1) JPS63282286A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6344748B1 (en) * 2017-02-08 2018-06-20 アメミヤ機器株式会社 Ozone water generator / discharger

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2359217B1 (en) * 2008-08-06 2012-04-10 Jose Antonio Martinez Cao FUEL GAS PRODUCTION DEVICE FOR ELECTROLYSIS.
CN103693717B (en) * 2013-12-02 2016-04-13 王来珠 A kind of integrated form multiple spot face electrolytic module device and electrolysis cup
US10465302B2 (en) * 2014-08-07 2019-11-05 Marathon Systems, Inc. Modular gaseous electrolysis apparatus with actively-cooled header module, co-disposed heat exchanger module and gas manifold modules therefor

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5763683A (en) * 1980-10-03 1982-04-17 Asahi Glass Co Ltd Production of hydrogen
JPS5767182A (en) * 1980-10-14 1982-04-23 Showa Denko Kk Construction of electrolytic cell for water of aqueous solution
JPS57131376A (en) * 1981-02-06 1982-08-14 Japan Atom Energy Res Inst Electrolyzing method for water

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5763683A (en) * 1980-10-03 1982-04-17 Asahi Glass Co Ltd Production of hydrogen
JPS5767182A (en) * 1980-10-14 1982-04-23 Showa Denko Kk Construction of electrolytic cell for water of aqueous solution
JPS57131376A (en) * 1981-02-06 1982-08-14 Japan Atom Energy Res Inst Electrolyzing method for water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6344748B1 (en) * 2017-02-08 2018-06-20 アメミヤ機器株式会社 Ozone water generator / discharger
JP2018127713A (en) * 2017-02-08 2018-08-16 アメミヤ機器株式会社 Apparatus for generating and discharging ozone water

Also Published As

Publication number Publication date
JPS63282286A (en) 1988-11-18

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