JP3485247B2 - Ionized water generator and partition wall for ionized water generator - Google Patents
Ionized water generator and partition wall for ionized water generatorInfo
- Publication number
- JP3485247B2 JP3485247B2 JP32654998A JP32654998A JP3485247B2 JP 3485247 B2 JP3485247 B2 JP 3485247B2 JP 32654998 A JP32654998 A JP 32654998A JP 32654998 A JP32654998 A JP 32654998A JP 3485247 B2 JP3485247 B2 JP 3485247B2
- Authority
- JP
- Japan
- Prior art keywords
- electrolysis
- water
- exchange membrane
- ion
- chambers
- 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 - Fee Related
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- Separation Using Semi-Permeable Membranes (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は水を電気分解して健
康増進のためのアルカリ機能水(アルカリイオン水)
や、殺菌等の医療用水(酸性イオン水)を生成するイオ
ン水造水装置およびイオン水造水装置用仕切壁に関す
る。TECHNICAL FIELD The present invention relates to alkaline functional water (alkali ionized water) for promoting health by electrolyzing water.
The present invention relates to an ion water desalination apparatus and a partition wall for an ion water desalination apparatus that generate medical water (acidic ion water) for sterilization.
【0002】[0002]
【従来の技術】従来、水の電気分解は中央部にイオン交
換膜を配置した電解槽と、この電解槽の一方の電解室に
陽電極を配置するとともに、他方の電解室に陰電極を配
置して行なっている。2. Description of the Related Art Conventionally, in the electrolysis of water, an electrolytic cell having an ion exchange membrane in the central part and a positive electrode in one electrolytic chamber of the electrolytic cell and a negative electrode in the other electrolytic chamber are disposed. I am doing it.
【0003】[0003]
【発明が解決しようとする課題】従来のイオン交換膜を
用いた水の電気分解では、電荷移動は殆どすべて陽電極
から陰電極へのカチオンの移動で行なわれるとともに、
水酸イオンの逆移動が生じないため、陽電極槽で成形さ
れる酸性イオン水のペーハーの低下は著しく促進される
という欠点があった。また、等量の水量で電気分解する
と、陰電極槽側の反応はアルカリイオン水のペーハーが
高くなるという欠点があった。In the electrolysis of water using a conventional ion exchange membrane, almost all the charge transfer is carried out by the transfer of cations from the positive electrode to the negative electrode.
Since there is no reverse migration of hydroxide ions, there is a drawback in that the decrease in pH of the acidic ionized water formed in the positive electrode tank is significantly promoted. Further, when electrolyzing with an equal amount of water, the reaction on the negative electrode tank side has a drawback that the pH of the alkaline ionized water becomes high.
【0004】本発明は以上のような従来の欠点に鑑み、
通電電気量のコントロールによって水素イオン生成量の
バランスを取るために、陰電極の通電量を半減させるこ
とにより、目標とするイオン水のペーハーをコントロー
ルすることができるイオン水造水装置を提供することを
目的としている。In view of the above-mentioned conventional drawbacks, the present invention has been made.
(EN) An ion water desalination apparatus capable of controlling the target pH of ion water by halving the amount of electricity applied to the negative electrode in order to balance the amount of hydrogen ion production by controlling the amount of electricity applied. It is an object.
【0005】また、本発明は電解槽に導入された水を純
性なイオン水に電気分解することができるとともに、イ
オン濃度を高めたイオン水も作ることができるイオン水
造水装置を提供することを目的としている。Further, the present invention provides an ion water desalination apparatus capable of electrolyzing water introduced into an electrolytic cell into pure ion water and also producing ion water having an increased ion concentration. Is intended.
【0006】本発明の前記ならびにそのほかの目的と新
規な特徴は次の説明を添付図面と照らし合わせて読む
と、より完全に明らかになるであろう。ただし、図面は
もっぱら解説のためのものであって、本発明の技術的範
囲を限定するものではない。The above and other objects and novel features of the present invention will become more fully apparent when the following description is read in view of the accompanying drawings. However, the drawings are only for explanation and do not limit the technical scope of the present invention.
【0007】[0007]
【課題を解決するための手段】上記目的を達成するため
に、本発明は電気分解を行なうことができる電解槽と、
この電解槽内が3個の電解室に仕切られるように配置さ
れた陽イオン交換膜と陰イオン交換膜とをそれぞれ備え
る2個の仕切壁と、前記電解槽の中央部の電解室に設け
られた陽電極と、前記電解槽の両側部の電解室にそれぞ
れ設けられた前記陽電極へ流す電流の半分の電流がそれ
ぞれ流される陰電極とでイオン水造水装置を構成してい
る。In order to achieve the above object, the present invention provides an electrolytic cell capable of electrolysis,
Two partition walls each provided with a cation exchange membrane and an anion exchange membrane arranged so that the inside of the electrolytic cell is partitioned into three electrolytic chambers, and provided in the electrolytic chamber at the center of the electrolytic cell. The positive electrode and the negative electrodes, which are respectively provided in the electrolysis chambers on both sides of the electrolytic cell and are supplied with half of the current flowing to the positive electrodes, constitute an ion water desalination apparatus.
【0008】[0008]
【発明の実施の形態】以下、図面に示す実施の形態によ
り、本発明を詳細に説明する。BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in detail below with reference to the embodiments shown in the drawings.
【0009】図1ないし図6に示す本発明の第1の実施
の形態において、1は機枠2の上部に設置された水の電
気分解を行なうことができる電解槽で、この電解槽1は
3個の電解室3、3A、3に仕切られるように該電解槽
1の内壁面に支持片4、4が形成されている。In the first embodiment of the present invention shown in FIGS. 1 to 6, reference numeral 1 denotes an electrolytic cell installed on the upper part of a machine casing 2 for electrolyzing water. Supporting pieces 4, 4 are formed on the inner wall surface of the electrolytic cell 1 so as to be partitioned into three electrolytic chambers 3, 3A, 3.
【0010】5、5は前記電解槽1を3個の電解室3、
3A、3に仕切る前記支持片4、4にシール材6、6を
介して4個のターンバックル機構を用いた押し圧具7、
7、7、7によって押し圧固定された2個のイオン交換
ユニットで、この2個のイオン交換ユニット5、5は、
図4および図5に示すように前記支持片4に外周部が支
持される複数個の陽イオン交換膜8および複数個の陰イ
オン交換膜9が取付けられた一対の仕切り壁10、10
Aと、この一対の仕切り壁10、10A間に水室11を
形成するための枠体12と、この枠体12内の水室11
に水道水や飲料水を供給しながら排出する水供給装置1
3とで構成されている。Reference numerals 5 and 5 denote the electrolytic cell 1 and three electrolytic chambers 3,
3A, a pressing member 7 using four turnbuckle mechanisms on the supporting pieces 4, 4 with sealing materials 6, 6 between them.
Two ion exchange units, which are pressed and fixed by 7, 7, and 7, the two ion exchange units 5 and 5 are
As shown in FIGS. 4 and 5, a pair of partition walls 10 and 10 to which a plurality of cation exchange membranes 8 and a plurality of anion exchange membranes 9 whose outer peripheral portions are supported by the support pieces 4 are attached.
A, a frame body 12 for forming a water chamber 11 between the pair of partition walls 10 and 10A, and a water chamber 11 in the frame body 12.
Water supply device that discharges tap water and drinking water while supplying water 1
3 and 3.
【0011】14は前記電解室1の中央部の電解室3A
内に設置された、チタニウムに白金メッキで被覆した陽
電極である。Reference numeral 14 is an electrolysis chamber 3A in the center of the electrolysis chamber 1.
It is a positive electrode which is installed inside and coated with platinum on titanium.
【0012】15、15は前記電解槽1の両側部の電解
室3、3内にそれぞれ設置された、前記陽電極14へ流
す電流の半分の電流がそれぞれ流される、チタニウムに
白金メッキで被覆した陰電極である。Numerals 15 and 15 are provided in the electrolysis chambers 3 and 3 on both sides of the electrolytic cell 1, respectively. Half of the current flowing to the positive electrode 14 is applied to each of them, and titanium is coated with platinum plating. It is a negative electrode.
【0013】16は前記電解槽1の各電解室3、3A、
3へ電気分解する水道水等の飲料水を分岐管17、1
7、17を用いて供給する分解水供給装置で、この分解
水供給装置16の分岐管17、17、17にはそれぞれ
開閉弁18、18、18が介装されている。Reference numeral 16 denotes each of the electrolysis chambers 3 and 3A of the electrolysis tank 1.
Drinking water such as tap water that is electrolyzed into 3 branch pipes 17, 1
An on-off valve 18, 18, 18 is provided in each of the branch pipes 17, 17, 17 of the decomposed water supply device 16 for supplying the decomposed water using 7, 7.
【0014】19は前記電解槽1の中央部の電解室3A
で生成された純性な酸性イオン水を酸性イオン水収納タ
ンク20へ排水する開閉弁21が設けられた酸性イオン
水排水管である。Reference numeral 19 denotes an electrolysis chamber 3A at the center of the electrolysis cell 1.
It is an acidic ionized water drainage pipe provided with an opening / closing valve 21 for draining the pure acidic ionized water generated in 1 above to the acidic ionized water storage tank 20.
【0015】22は前記電解槽1の両側部の電解室3、
3で生成された純性なアルカリイオン水を開閉弁23、
23が備えられた分岐パイプ24、24を介してアルカ
リイオン水収納タンク25へ排水するアルカリイオン水
排水管である。Reference numeral 22 denotes the electrolysis chambers 3 on both sides of the electrolysis cell 1.
Open / close valve 23 for pure alkaline ionized water generated in 3.
It is an alkaline ionized water drainage pipe for draining to an alkaline ionized water storage tank 25 through branch pipes 24 provided with 23.
【0016】26は前記陽電極14と前記陰電極15、
15に目的とする電流を供給するための電圧を制御する
電圧制御装置である。26 is the positive electrode 14 and the negative electrode 15,
15 is a voltage control device for controlling a voltage for supplying a target current to 15.
【0017】上記構成のイオン水造水装置27は電解槽
1の各電解室3、3A、3内に分解水供給装置16の開
閉弁18、18、18を開放して、飲料水をそれぞれ所
定量供給して開閉弁18、18、18を閉じるととも
に、2個のイオン交換ユニット5、5の水供給装置1
3、13によって水室11、11内に水を供給する。In the ion water desalination apparatus 27 having the above-mentioned structure, the opening / closing valves 18, 18, 18 of the decomposition water supply apparatus 16 are opened in the electrolysis chambers 3, 3A, 3 of the electrolysis tank 1 to supply drinking water respectively. A fixed amount of water is supplied to close the on-off valves 18, 18, 18 and the water supply device 1 of the two ion exchange units 5 and 5
Water is supplied into the water chambers 11 and 11 by 3, 13.
【0018】しかる後、陽電極14と陰電極15、15
に電流を一定時間流し、電気分解を行なう。この時、電
解反応によって電荷移動したアニオン、カチオンを陽イ
オン交換膜や陰イオン交換膜で分離採取されるととも
に、図6に示すように電解槽1の中央部の陽電極14が
設けられた電解室3Aの分解水の陽イオンは2個のイオ
ン交換ユニット5、5の一対の仕切壁10、10Aの複
数個の陽イオン交換膜8、8を通過して、両側部の陰電
極15、15が設けられた電解室3、3へ導かれる。After that, the positive electrode 14 and the negative electrodes 15, 15
An electric current is applied for a certain period of time to perform electrolysis. At this time, the anions and cations that have undergone the charge transfer due to the electrolytic reaction are separated and collected by the cation exchange membrane or the anion exchange membrane, and as shown in FIG. The cations of the decomposed water in the chamber 3A pass through the plurality of cation exchange membranes 8, 8 of the pair of partition walls 10, 10A of the two ion exchange units 5, 5, and the negative electrodes 15, 15 on both sides. Is introduced into the electrolysis chambers 3 and 3.
【0019】また、両側部の陰電極15、15が設けら
れた電解室3、3の分解水の陰イオンは2個のイオン交
換ユニット5、5の一対の仕切壁10、10Aの複数個
の陰イオン交換膜9、9を通過して中央部の陽電極14
が設けられた電解室3Aへ導かれる。Further, the anions of the decomposed water in the electrolysis chambers 3 and 3 provided with the negative electrodes 15 and 15 on both sides are formed by a plurality of partition walls 10 and 10A of the two ion exchange units 5 and 5, respectively. The positive electrode 14 in the central portion passes through the anion exchange membranes 9 and 9.
Is introduced to the electrolysis chamber 3A in which is provided.
【0020】さらに、2個のイオン交換ユニット5、5
の一対の仕切壁10、10Aおよび10、10A間の水
室11、11内に供給された水道水や飲料水の陽イオン
は両側部の電解室3、3へ導かれるとともに、陰イオン
は中央部の電解室3Aへ導かれ、イオン濃度が高めら
れ、中央部の電解室3Aにはペーハーが3〜3.2の純
性の酸性イオン水が生成されるとともに、両側部の電解
室3、3にはペーハーが9.2〜9.7の純性のアルカ
リイオン水が生成される。Furthermore, two ion exchange units 5, 5
The cations of tap water or drinking water supplied into the water chambers 11, 11 between the pair of partition walls 10, 10A and 10, 10A are guided to the electrolysis chambers 3, 3 on both sides, and the anions are in the center. Is introduced into the electrolysis chamber 3A in the central part, the ion concentration is increased, pure acidic ionized water having a pH of 3 to 3.2 is generated in the electrolysis chamber 3A in the central part, and the electrolysis chambers 3 in both sides are In 3, pure alkaline ionized water having a pH of 9.2 to 9.7 is generated.
【0021】このように酸性イオン水やアルカリイオン
水が生成されると、酸性イオン水排水管19の開閉弁2
1を開放して酸性イオン水収納タンク20に収納すると
ともに、アルカリイオン水排水管22の開閉弁23を開
放してアルカリイオン水収納タンク25に収納する。When acidic ionized water or alkaline ionized water is generated in this manner, the opening / closing valve 2 of the acidic ionized water drain pipe 19
1 is opened and stored in the acidic ion water storage tank 20, and the opening / closing valve 23 of the alkaline ion water drain pipe 22 is opened and stored in the alkaline ion water storage tank 25.
【0022】また、2個のイオン交換ユニット5、5を
通過した水は、純水を作るための予備水として使用する
ことができる。The water that has passed through the two ion exchange units 5 and 5 can be used as preliminary water for producing pure water.
【0023】[0023]
【発明の異なる実施の形態】次に、図7ないし図18に
示す本発明の異なる実施の形態および本願発明者が考え
たイオン水造水装置につき説明する。なおこれらの本発
明の異なる実施の形態および本願発明者が考えたイオン
水造水装置の説明に当って、前記本発明の第1の実施の
形態と同一構成部分には同一符号を付して重複する説明
を省略する。Different Embodiments of the Invention Next, different embodiments of the present invention shown in FIGS. 7 to 18 and an ion water desalination apparatus considered by the inventor of the present invention will be described. In the explanation of these different embodiments of the present invention and the ionized water desalination apparatus considered by the inventor of the present application, the same components as those of the first embodiment of the present invention are designated by the same reference numerals. A duplicate description will be omitted.
【0024】図7ないし図9に示す本発明の第2の実施
の形態において、前記本発明の第1の実施の形態と主に
異なる点は、電解槽1を3個の電解室3、3A、3に仕
切るため、2個の仕切壁10、10を用いた点で、この
ように構成したイオン水造水装置27Aにしても、イオ
ン濃度を高めることはできないが、その他は前記本発明
の第1の実施の形態と同様な作用効果が得られる。The second embodiment of the present invention shown in FIGS. 7 to 9 is mainly different from the first embodiment of the present invention in that the electrolytic cell 1 has three electrolytic chambers 3 and 3A. In order to divide into 3 parts, two partition walls 10 and 10 are used, and thus even if the ion water desalination apparatus 27A configured as described above cannot increase the ion concentration, the other parts are the same as those of the present invention. The same effect as that of the first embodiment can be obtained.
【0025】図10ないし図12に示す本願発明者が考
えたイオン水造水装置において、前記本発明の第2の実
施の形態と主に異なる点は、陽イオン交換膜あるいは陰
イオン交換膜だけを設けた仕切壁10B、10Bを用い
た点で、このように構成したイオン水造水装置27Bに
してもよい。The ion water desalination apparatus proposed by the inventor of the present invention shown in FIGS. 10 to 12 is mainly different from the second embodiment of the present invention only in the cation exchange membrane or the anion exchange membrane. The ion water demineralizer 27B thus configured may be used in that the partition walls 10B and 10B provided with are used.
【0026】図13および図14に示す本発明の第3の
実施の形態において、前記本発明の第1の実施の形態と
主に異なる点は、電解室1の中央部の電解室3A内に多
数の孔28が形成されたチタニウムに白金メッキで被覆
した少なくとも2枚以上、本発明の実施の形態では3枚
の陽電極14A、14A、14Aを所定間隔で並列させ
た点で、このように形成した陽電極14A、14A、1
4Aを3枚所定間隔で並列させることにより、通電率が
よくなり、重金属を含む水の電気分解に使用することが
できるとともに、陽電極14A、14A、14Aの多数
の孔28によってイオンの移動が可能になり、強酸イオ
ン水と、強アルカリイオン水を容易に作り出すことがで
きるイオン水造水装置27Cにすることができる。The third embodiment of the present invention shown in FIGS. 13 and 14 is mainly different from the first embodiment of the present invention in that the inside of the electrolytic chamber 3A in the central portion of the electrolytic chamber 1 is different. As described above, at least two positive electrodes 14A, 14A, 14A, which are formed by coating titanium with a large number of holes 28 with platinum plating, and in the embodiment of the present invention, three positive electrodes 14A, 14A, 14A, are arranged in parallel at a predetermined interval. Formed positive electrodes 14A, 14A, 1
By arranging 3 pieces of 4A in parallel at a predetermined interval, the conductivity can be improved and can be used for the electrolysis of water containing heavy metals, and the migration of ions can be prevented by the numerous holes 28 of the positive electrodes 14A, 14A, 14A. This makes it possible to provide an ion water desalination apparatus 27C capable of easily producing strong acid ion water and strong alkali ion water.
【0027】図15および図16に示す本発明の第4の
実施の形態において、前記本発明の第4の実施の形態と
主に異なる点は、電解室1の中央部の電解室3A内にチ
タニウムに白金メッキで被覆した線材29を織つたり編
んだりしてメッシュ状に形成した少なくとも2枚以上、
本発明の実施の形態では3枚の陽電極14B、14B、
14Bを所定間隔で並列させた点で、このように構成し
たイオン水造水装置27Dにしても前記本発明の第4の
実施の形態と同様な作用効果が得られる。The fourth embodiment of the present invention shown in FIGS. 15 and 16 is mainly different from the fourth embodiment of the present invention in that the inside of the electrolytic chamber 3A in the central portion of the electrolytic chamber 1 is different. At least two or more pieces formed by weaving or knitting a titanium-plated wire rod 29 coated with platinum to form a mesh,
In the embodiment of the present invention, three positive electrodes 14B, 14B,
Even if the ion water desalination apparatus 27D having such a configuration is used, the same effects as those of the fourth embodiment of the present invention can be obtained in that the 14B are arranged in parallel at a predetermined interval.
【0028】図17および図18に示す本発明の第5の
実施の形態において、前記本発明の第4の実施の形態と
主に異なる点は、電解室1の中央部の電解室3A内にチ
タニウムに白金メッキで被覆した線材29を織つたり編
んだりして円筒形状のメッシュ状に形成した陽電極14
Cを設けた点で、このように構成したイオン水造水装置
27Eにしても前記本発明の第4の実施の形態と同様な
作用効果が得られる。The fifth embodiment of the present invention shown in FIGS. 17 and 18 is mainly different from the fourth embodiment of the present invention in that the inside of the electrolytic chamber 3A in the central portion of the electrolytic chamber 1 is different. Positive electrode 14 formed by weaving or knitting titanium-plated wire rod 29 coated with platinum to form a cylindrical mesh
In view of the provision of C, the ion water desalination apparatus 27E having the above-described structure can also obtain the same operational effect as that of the fourth embodiment of the present invention.
【0029】[0029]
【発明の効果】以上の説明から明らかなように、本発明
にあっては次に列挙する効果が得られる。As is apparent from the above description, the following effects can be obtained in the present invention.
【0030】(1)電気分解を行なうことができる電解
槽と、この電解槽内が3個の電解室に仕切られるように
配置された陽イオン交換膜と陰イオン交換膜とをそれぞ
れ備える2個の仕切壁と、前記電解槽の中央部の電解室
に設けられた陽電極と、前記電解槽の両側部の電解室に
それぞれ設けられた前記陽電極へ流す電流の半分の電流
がそれぞれ流される陰電極とで構成されているので、通
電電気量のコントロールによって、水素イオン生成量の
バランスをとることができる。したがって、目標とする
イオン水のペーハーコントロールを行なうことができ
る。(1) Two electrolysis cells each capable of performing electrolysis and two cation exchange membranes and anion exchange membranes arranged so that the interior of the electrolysis cell is divided into three electrolysis chambers. The partition wall, the positive electrode provided in the electrolytic chamber at the center of the electrolytic cell, and half the current flowing to the positive electrodes provided in the electrolytic chambers at both sides of the electrolytic cell, respectively. Since it is composed of a negative electrode, the amount of hydrogen ions produced can be balanced by controlling the amount of electricity supplied. Therefore, the target pH control of the ionized water can be performed.
【0031】(2)前記(1)によって、電解反応によ
って電荷移動したアニオン、カチオンをイオン交換膜に
よって分離、採取することができる。(2) According to the above (1), the anions and cations that have undergone charge transfer by the electrolytic reaction can be separated and collected by the ion exchange membrane.
【0032】(3)前記(1)によって、構造が簡単で
あるので、容易に実施することができる。(3) According to the above (1), since the structure is simple, it can be easily implemented.
【0033】(4)前記(1)によって、2個の仕切壁
にそれぞれ陽イオン交換膜と陰イオン交換膜を備えてい
るので、純性の酸性イオン水とアルカリイオン水に生成
することができる。(4) According to the above (1), since two partition walls are provided with a cation exchange membrane and an anion exchange membrane, respectively, pure acidic ion water and alkaline ion water can be produced. .
【0034】(5)請求項2は前記(1)〜(4)と同
様な効果が得られるとともに、2個のイオン交換ユニッ
トに供給される水によって通電量を増加させ、水素イオ
ン生成量の促進、低下のバランス調整が可能で、イオン
濃度を高めることができる。(5) According to the second aspect, the same effects as the above (1) to (4) can be obtained, and the amount of electricity supplied is increased by the water supplied to the two ion exchange units so that the hydrogen ion production amount can be increased. It is possible to adjust the balance of acceleration and decrease, and to increase the ion concentration.
【0035】(6)請求項3、4、5は前記(1)〜
(4)と同様な効果が得られるとともに、多数の孔を形
成したり、メッシュ状に形成した少なくとも2枚以上の
陽電極あるいは円筒形状のメッシュ状に形成した陽電極
を用いているので、通電率がよくなり、重金属を含む水
の電気分解に使用することができるとともに、陽電極で
のイオンの移動が可能になり、強酸イオン水と、強アル
カリイオン水を容易に作り出すことができる。(6) Claims 3, 4, and 5 are the above (1) to
In addition to obtaining the same effect as (4), since a large number of holes are formed or at least two positive electrodes formed in a mesh shape or a positive electrode formed in a cylindrical mesh shape are used, it is possible to energize The efficiency is improved, and it can be used for electrolysis of water containing heavy metals, and ions can be moved at the positive electrode, and strong acid ion water and strong alkali ion water can be easily produced.
【図1】本発明の第1の実施の形態の平面図。FIG. 1 is a plan view of a first embodiment of the present invention.
【図2】本発明の第1の実施の形態の正面図。FIG. 2 is a front view of the first embodiment of the present invention.
【図3】図1の3−3線に沿う拡大断面図。FIG. 3 is an enlarged sectional view taken along line 3-3 of FIG.
【図4】本発明の第1の実施の形態のイオン交換ユニッ
トの分解斜視図。FIG. 4 is an exploded perspective view of the ion exchange unit according to the first embodiment of this invention.
【図5】本発明の第1の実施の形態のイオン交換ユニッ
トの一部破断説明図。FIG. 5 is a partially cutaway explanatory view of the ion exchange unit according to the first embodiment of the present invention.
【図6】本発明の第1の実施の形態の電気分解時の説明
図。FIG. 6 is an explanatory diagram during electrolysis according to the first embodiment of this invention.
【図7】本発明の第2の実施の形態の平面図。FIG. 7 is a plan view of the second embodiment of the present invention.
【図8】本発明の第2の実施の形態の正面図。FIG. 8 is a front view of the second embodiment of the present invention.
【図9】図7の9−9線に沿う拡大断面図。9 is an enlarged cross-sectional view taken along line 9-9 of FIG.
【図10】本願発明者が考えたイオン水造水装置の平面
図。FIG. 10 is a plan view of an ionized water desalination apparatus considered by the present inventors.
【図11】本願発明者が考えたイオン水造水装置の正面
図。FIG. 11 is a front view of an ionized water desalination apparatus considered by the present inventor.
【図12】図10の12−12線に沿う拡大断面図。12 is an enlarged cross-sectional view taken along line 12-12 of FIG.
【図13】本発明の第3の実施の形態の平面図。FIG. 13 is a plan view of the third embodiment of the present invention.
【図14】本発明の第3の実施の形態の陽電極の説明
図。FIG. 14 is an explanatory diagram of a positive electrode according to a third embodiment of the present invention.
【図15】本発明の第4の実施の形態の平面図。FIG. 15 is a plan view of the fourth embodiment of the present invention.
【図16】本発明の第4の実施の形態の陽電極の説明
図。FIG. 16 is an explanatory diagram of a positive electrode according to a fourth embodiment of the present invention.
【図17】本発明の第5の実施の形態の平面図。FIG. 17 is a plan view of the fifth embodiment of the present invention.
【図18】本発明の第5の実施の形態の陽電極の説明
図。FIG. 18 is an explanatory diagram of a positive electrode according to a fifth embodiment of the present invention.
1:電解槽、 2:機枠、
3、3A:電解室、 4:支持片、
5:イオン交換ユニット、6:シール材、
7:押し圧具、 8:陽イオン交換膜、
9:陰イオン交換膜、 10、10A、10B:仕切
壁、
11:水室、 12:枠体、
13:水供給装置、
14、14A、14B、14C:陽電極、
15:陰電極、 16:分解水供給装置、
17:分岐管、 18:開閉弁、
19:酸性イオン水排水管、
20:酸性イオン水収納タンク、
21:開閉弁、 22:アルカリイオン水排水
管、
23:開閉弁、 24:分岐パイプ、
25:アルカリイオン水収納タンク、
26:電圧制御装置、
27、27A〜27E:イオン水造水装置、
28:多数の孔、 29:線材。1: Electrolysis tank, 2: Machine frame, 3, 3A: Electrolysis chamber, 4: Support piece, 5: Ion exchange unit, 6: Sealing material, 7: Pressing tool, 8: Cation exchange membrane, 9: Anion Exchange membrane, 10, 10A, 10B: Partition wall, 11: Water chamber, 12: Frame body, 13: Water supply device, 14, 14A, 14B, 14C: Positive electrode, 15: Cathode electrode, 16: Decomposition water supply device , 17: Branch pipe, 18: Open / close valve, 19: Acid ion water drain pipe, 20: Acid ion water storage tank, 21: Open / close valve, 22: Alkaline ion water drain pipe, 23: Open / close valve, 24: Branch pipe, 25: Alkaline ion water storage tank, 26: Voltage control device, 27, 27A to 27E: Ion water desalination device, 28: Many holes, 29: Wire rod.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平8−173963(JP,A) 特開 平7−164479(JP,A) 特開 平7−136659(JP,A) 特開 平7−108273(JP,A) 特開 平6−312185(JP,A) 特開 平8−187492(JP,A) 特開 平9−268395(JP,A) 特開 平9−239364(JP,A) 特開 平7−308672(JP,A) 特開 昭64−90088(JP,A) 特開 昭54−23078(JP,A) (58)調査した分野(Int.Cl.7,DB名) C02F 1/46 B01D 61/46 ─────────────────────────────────────────────────── --Continued from the front page (56) References JP-A-8-173963 (JP, A) JP-A-7-164479 (JP, A) JP-A-7-136659 (JP, A) JP-A-7- 108273 (JP, A) JP-A-6-312185 (JP, A) JP-A-8-187492 (JP, A) JP-A-9-268395 (JP, A) JP-A-9-239364 (JP, A) JP-A-7-308672 (JP, A) JP-A 64-90088 (JP, A) JP-A 54-23078 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) C02F 1/46 B01D 61/46
Claims (5)
と、この電解槽内が3個の電解室に仕切られるように配
置された陽イオン交換膜と陰イオン交換膜とをそれぞれ
備える2個の仕切壁と、前記電解槽の中央部の電解室に
設けられた陽電極と、前記電解槽の両側部の電解室にそ
れぞれ設けられた前記陽電極へ流す電流の半分の電流が
それぞれ流される陰電極とからなることを特徴とするイ
オン水造水装置。1. An electrolyzer capable of performing electrolysis, and two electrolyzers each including a cation exchange membrane and an anion exchange membrane arranged so that the interior of the electrolyzer is partitioned into three electrolysis chambers. A partition wall, a positive electrode provided in the electrolysis chamber at the center of the electrolytic cell, and a negative current to which half of the current flowing to the positive electrodes provided in the electrolysis chambers at both sides of the electrolytic cell are respectively passed. An ion water desalination apparatus comprising an electrode.
と、この電解槽内が3個の電解室に仕切られるように配
置された水室が形成できるように配置された陽イオン交
換膜と陰イオン交換膜をそれぞれ備える一対の仕切壁、
この一対の仕切壁間の水室内にイオン濃度を高めるため
の水を供給する水供給装置とからなる2個のイオン交換
ユニットと、前記電解槽の中央部の電解室に設けられた
陽電極と、前記電解槽の両側部の電解室にそれぞれ設け
られた前記陽電極へ流す電流の半分の電流がそれぞれ流
される陰電極とからなることを特徴とするイオン水造水
装置。2. An electrolyzer capable of performing electrolysis, a cation exchange membrane and an anion arranged so as to form a water chamber arranged so that the interior of the electrolyzer is partitioned into three electrolyzers. A pair of partition walls each equipped with an ion exchange membrane,
Two ion exchange units consisting of a water supply device for supplying water for increasing the ion concentration into the water chamber between the pair of partition walls, and a positive electrode provided in the electrolysis chamber at the center of the electrolytic cell. An ion water desalination apparatus comprising: a negative electrode that is provided with electrolysis chambers on both sides of the electrolyzer, to which half of the current that flows to the positive electrode is respectively passed.
と、この電解槽内が3個の電解室に仕切られるように配
置された陽イオン交換膜と陰イオン交換膜とをそれぞれ
備える2個の仕切壁と、前記電解槽の中央部の電解室に
所定間隔の並列状態で少なくとも2個以上設けられた多
数の孔が形成された陽電極と、前記電解槽の両側部の電
解室にそれぞれ設けられた前記陽電極へ流す電流の半分
の電流がそれぞれ流される陰電極とからなることを特徴
とするイオン水造水装置。3. An electrolyzer capable of performing electrolysis, and two electrolyzers each including a cation exchange membrane and an anion exchange membrane arranged so that the interior of the electrolyzer is partitioned into three electrolysis chambers. A partition wall, a positive electrode having a large number of holes provided at least two in parallel in a predetermined interval in the central electrolysis chamber of the electrolysis cell, and electrolysis chambers on both sides of the electrolysis cell. And a negative electrode to which half of the current flowing to the positive electrode is applied, respectively.
と、この電解槽内が3個の電解室に仕切られるように配
置された陽イオン交換膜と陰イオン交換膜とをそれぞれ
備える2個の仕切壁と、前記電解槽の中央部の電解室に
所定間隔の並列状態で少なくとも2個以上設けられたメ
ッシュ状の陽電極と、前記電解槽の両側部の電解室にそ
れぞれ設けられた前記陽電極へ流す電流の半分の電流が
それぞれ流される陰電極とからなることを特徴とするイ
オン水造水装置。4. An electrolyzer capable of performing electrolysis, and two electrolyzers each including a cation exchange membrane and an anion exchange membrane arranged so that the interior of the electrolyzer is divided into three electrolysis chambers. The partition wall, a mesh-shaped positive electrode provided in the electrolysis chamber at the center of the electrolysis cell in parallel at a predetermined interval, and at least two mesh positive electrodes, and the positive electrodes provided in the electrolysis cells on both sides of the electrolysis cell. An ion water desalination apparatus comprising a negative electrode to which half of the current flowing to the electrodes is respectively caused to flow.
と、この電解槽内が3個の電解室に仕切られるように配
置されたイオン交換膜を備える2個の仕切壁と、前記電
解槽の中央部の電解室に設けられた円筒形状に形成した
メッシュ状の陽電極と、前記電解槽の両側部の電解室に
それぞれ設けられた前記陽電極へ流す電流の半分の電流
がそれぞれ流される陰電極とからなることを特徴とする
イオン水造水装置。5. An electrolytic cell capable of performing electrolysis, two partition walls provided with an ion exchange membrane arranged so that the interior of the electrolytic cell is divided into three electrolytic chambers, and the electrolytic cell of the electrolytic cell. A cylindrical mesh-shaped positive electrode provided in the central electrolysis chamber and half of the current flowing to the positive electrodes respectively provided in the electrolysis chambers on both sides of the electrolytic cell An ion water desalination apparatus comprising an electrode.
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