JP3497357B2 - Electrolytic cell - Google Patents

Electrolytic cell

Info

Publication number
JP3497357B2
JP3497357B2 JP28258797A JP28258797A JP3497357B2 JP 3497357 B2 JP3497357 B2 JP 3497357B2 JP 28258797 A JP28258797 A JP 28258797A JP 28258797 A JP28258797 A JP 28258797A JP 3497357 B2 JP3497357 B2 JP 3497357B2
Authority
JP
Japan
Prior art keywords
plate
cathode
electrolytic cell
anode
electrode
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
Application number
JP28258797A
Other languages
Japanese (ja)
Other versions
JPH11104641A (en
Inventor
正人 福島
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.)
Amano Corp
Original Assignee
Amano Corp
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 Amano Corp filed Critical Amano Corp
Priority to JP28258797A priority Critical patent/JP3497357B2/en
Publication of JPH11104641A publication Critical patent/JPH11104641A/en
Application granted granted Critical
Publication of JP3497357B2 publication Critical patent/JP3497357B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

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】本発明は、例えば食塩水等の
電解水を電気分解することにより、酸性水とアルカリ水
を生成することができる電解槽に関するものであり、具
体的には、構成部品を汎用化することによって必要に応
じた電解能力及び大きさ等の諸条件を達成できるように
工夫した電解槽に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolytic cell capable of producing acidic water and alkaline water by electrolyzing electrolyzed water such as saline solution, and more specifically, to a constituent part. The present invention relates to an electrolytic cell devised so that various conditions such as electrolysis capacity and size can be achieved by generalizing the above.

【0002】[0002]

【従来の技術】従来の電解槽は、例えば図8に示すよう
に食塩水等の電解水を供給自在に構成した電解槽20の
内部を、イオン交換樹脂を用いて構成した隔膜21によ
って陰極室20Aと陽極室20Bの左右2室に区画し、
陰極室20Aには陰極となる電極23を設け、陽極室2
0Bには陽極となる電極24を設けて、これ等両電極間
に直流電流22を供給するように構成している。
2. Description of the Related Art In a conventional electrolytic cell, for example, as shown in FIG. 8, the inside of an electrolytic cell 20 configured to be able to supply electrolyzed water such as salt water is provided with a diaphragm 21 made of an ion exchange resin to form a cathode chamber. 20A and anode chamber 20B are divided into two chambers on the left and right,
The cathode chamber 20A is provided with an electrode 23 serving as a cathode, and the anode chamber 2
An electrode 24 serving as an anode is provided at 0B, and a direct current 22 is supplied between these electrodes.

【0003】そして電解槽20内で水の電気分解を行う
ことにより、電解水中に含まれている各種の陽イオンを
陰極室20Aに集約し、また、各種の陰イオンを陽極室
20Bに集約することによって、陽極室20Bに設けた
取水口26から酸性水を取出し、陰極室20Aに設けた
取水口25からはアルカリ水を取出すように構成されて
いる。
By electrolyzing water in the electrolytic cell 20, various cations contained in the electrolyzed water are collected in the cathode chamber 20A and various anions are collected in the anode chamber 20B. Thus, the acidic water is taken out from the water intake port 26 provided in the anode chamber 20B, and the alkaline water is taken out from the water intake port 25 provided in the cathode chamber 20A.

【0004】ところが、電解水を例えば家庭用に供する
場合と、業務用或は工業用に供する場合とでは、電解槽
の用途によって求められるpH値、単位時間当りの取水
量等の諸条件が種々様々であるため、上記図8に示した
ような従来の電解槽では、その都度要求に応じた仕様で
電解槽自体、電極、電源等の各種構成部品を製造しなく
てはならないため、必要な金型や製造設備と云った諸設
備に多額の費用が掛って、製造コストを高くする問題が
あった。
However, when electrolyzed water is used for household use and for commercial or industrial use, various conditions such as pH value and water withdrawal amount per unit time are required depending on the use of the electrolytic cell. Since there are various types, in the conventional electrolytic cell as shown in FIG. 8, it is necessary to manufacture various components such as the electrolytic cell itself, the electrodes and the power source according to the requirements each time. There has been a problem that a large amount of cost is required for various equipment such as molds and manufacturing equipment, which raises the manufacturing cost.

【0005】そこで、例えば特開平6−339683号
公報に開示されているように、構成部品を汎用化するこ
とによって、必要最小限の部品の組合せにより、必要に
応じて電解能力(取水量)及び電解槽の大きさ等の諸条
件を変更可能に構成した電解水生成装置が考えられた。
Therefore, as disclosed in, for example, Japanese Unexamined Patent Publication No. 6-339683, the generalization of the components makes it possible to combine the minimum necessary number of components, and if necessary, the electrolysis capacity (water intake amount) and An electrolyzed water generation device was conceived in which various conditions such as the size of the electrolytic cell can be changed.

【0006】[0006]

【発明が解決しようとする課題】しかし、上述した従来
の電解水生成装置は、汎用化した同じ形状の電極板を重
ねて陽極室と陰極室を構成する場合に、各電極板に設け
た通孔同士を連通接続して水の流路を構成するには、上
記公報の図7に示すようなスルーパッキンやターンパッ
キン等の各種接続部材を、接続部の用途に応じて適宜選
択して組付ける必要があるため、その接続作業が煩雑で
あると共に、パッキンの選択を間違えると陽極室と陰極
室の流路を適正に構築できなくなるので、電解槽の組立
てには時間と費用が掛る問題があった。
However, in the above-mentioned conventional electrolyzed water generator, when the general-purposed electrode plates having the same shape are stacked to form the anode chamber and the cathode chamber, the conventional electrolytic water generators are installed in the electrode plates. In order to connect the holes to each other to form a water flow path, various connecting members such as through packing and turn packing as shown in FIG. 7 of the above publication are appropriately selected and assembled according to the application of the connecting portion. Since it is necessary to attach it, the connecting work is complicated, and if the packing is selected incorrectly, the flow path of the anode chamber and the cathode chamber cannot be constructed properly, so it takes time and cost to assemble the electrolytic cell. there were.

【0007】更に、上記従来の電解水生成装置は、電極
をチタンの母材を用いて形状を造り、その表面に白金若
しくはイリジウムの合金を薄膜状にコーテイングすると
共に、これ等構成部品に上述したような各種のパツキン
グを取付けて水の流路を構成するものであるから、電気
分解によって電極が水に溶出してしまう場合があり、特
に、チタンに白金等のコーテイングを施したものは、コ
ーテイングにピンホール等の疵があるとチタンが溶液に
さらされて、電解作用でその部品の消耗が加速されるた
め、結果的にその部分が大きく損傷して孔があいてしま
う問題もあった。
Further, in the above-mentioned conventional electrolyzed water generator, the electrode is formed by using a titanium base material, and a platinum or iridium alloy is coated on the surface of the electrode in a thin film shape. Since various types of packing are attached to form a water flow path, the electrodes may be dissolved in water by electrolysis, and in particular, titanium coated with platinum, etc. If there is a flaw such as a pinhole on the surface of titanium, the titanium is exposed to the solution and the wear of the component is accelerated by the electrolytic action. As a result, there is a problem that the portion is greatly damaged and a hole is formed.

【0008】従って本発明の技術的課題は、汎用化した
同じ形状の電極板を重ねて電気分解のための陽極室と陰
極室を造るに当って、各種のパッキン類や接続具等を用
いなくても少い構成部品で陽極室と陰極室の各流路を容
易に造ることができ、また、チタンの溶解を防止し、且
つ、電解槽の水漏れも防止できるようにすることであ
る。
Therefore, the technical problem of the present invention is to use various packings, connecting tools, etc. in stacking general-purpose electrode plates of the same shape to form an anode chamber and a cathode chamber for electrolysis. Even if the flow paths of the anode chamber and the cathode chamber can be easily made with a small number of components, the dissolution of titanium and the leakage of water from the electrolytic cell can be prevented.

【0009】[0009]

【課題を解決するための手段】上記の技術的課題を解決
するために本発明で講じた手段は以下の如くである。
[Means for Solving the Problems] Means taken in the present invention for solving the above technical problems are as follows.

【0010】同じ形状に形成した陽極板と陰極板を中間
に隔膜プレートを介在させて重ねて取付け、陽極板と隔
膜プレートの間を陽極室とし、陰極板と隔膜プレートの
間を陰極室として、これ等陽極室と陰極室に電解水を送
り込んで電気分解することにより、陽極室から酸性水を
取出し、陰極室からはアルカリ水を取出すように構成し
た電解槽であって、
An anode plate and a cathode plate, which are formed in the same shape, are mounted so as to overlap with each other with a diaphragm plate interposed therebetween, and an anode chamber is defined between the anode plate and the diaphragm plate, and a cathode chamber is defined between the cathode plate and the diaphragm plate. An electrolytic cell configured such that electrolytic water is sent to the anode chamber and the cathode chamber and electrolyzed to extract acidic water from the anode chamber and alkaline water from the cathode chamber.

【0011】(1) 上記陽極板と陰極板の双方を構成
する電極板の四隅対称位置に電解水用の4個の通孔を穿
設し、これ等の通孔のうち一方の対角線上に位置する上
下2つの通孔を、電極板に対して直角方向への直角流路
を備えた筒状の通孔と成し、他方の対角線上に位置する
上下2つの通孔を、電極板に沿った方向に流れる迂回通
路を備えたボス状の通孔と成すと共に、上記の電極板を
上下を逆さにして交互に重ねて取付けることにより、上
記筒状とボス状に形成した各通孔口同士を連通接続自在
に構成すること。(請求項1)
(1) Four through holes for electrolyzed water are formed at four corner symmetrical positions of the electrode plates constituting both the above-mentioned anode plate and cathode plate, and one of these through holes is formed on one diagonal line. The upper and lower two through holes which are positioned are cylindrical through holes having a right-angled flow path in a direction perpendicular to the electrode plate, and the upper and lower two through holes located on the other diagonal line are formed in the electrode plate. A through hole formed in a cylindrical shape and a boss shape by forming a boss-shaped through hole having a bypass passage that flows in the direction along with the above-mentioned electrode plates by alternately stacking them upside down. Configure so that they can communicate with each other. (Claim 1)

【0012】(2) 電極板に沿った方向に流れる迂回
通路を備えたボス状の通孔が、ボスの周囲にスプライン
状の切り欠き溝を形成すること。(請求項2)
(2) A boss-shaped through hole having a bypass passage that flows in a direction along the electrode plate forms a spline-shaped cutout groove around the boss. (Claim 2)

【0013】(3) 陽極板と陰極板の双方を構成する
電極板の全体をプラスチック材を用いて構成すると共
に、このプラスチック製電極板の少くとも電極を形成す
る部分に白金層を形成すること。(請求項3)
(3) The whole of the electrode plates constituting both the anode plate and the cathode plate is made of a plastic material, and a platinum layer is formed at least on the electrodes of the plastic electrode plate. . (Claim 3)

【0014】上記(1)で述べた請求項1に係る手段に
よれば、例えば4枚の電極板を間に隔膜プレートを介在
させた状態で上下を逆さにして交互に重ねて組付けた場
合には、上下4ケ所の対称位置に設けた筒状とボス状の
各通孔は、筒状のものとボス状のものが各々その通孔口
を連通状態に接続され、ボス状の通孔部分では電解水を
電極板に沿って流し、筒状の通孔部分では電解水を直角
に流すように構成するため、陽極板と陰極板との間に隔
膜プレートによって仕切り形成された各陽極室同士及び
各陰極室同士を夫々筒状の通孔で連通し、また、各ボス
状の通孔部分では電解水を電極板に沿って各陽極室及び
陰極室の内部に流し込んで電気分解することができるも
のであって、汎用性のある電極板を交互に重ねて各通孔
同士を連通接続するだけで、パッキン等の接続部材を用
いなくても陽極室同士と陰極室同士が連通接続された高
性能な電解槽を提供することを可能にする。
According to the means according to claim 1 described in the above (1), in the case where, for example, four electrode plates are assembled by alternately stacking them upside down with a diaphragm plate interposed therebetween. In the cylindrical and boss-shaped through holes provided at four symmetrical positions at the top and bottom, the cylindrical and boss-shaped through holes are connected so that their through holes are connected to each other. Electrolyzed water is made to flow along the electrode plate in the part, and electrolytic water is made to flow in the cylindrical through-hole at a right angle.Therefore, each anode chamber is formed by a diaphragm plate between the anode plate and the cathode plate. Each of them and each cathode chamber are communicated with each other through a cylindrical through hole, and at each boss through hole, electrolyzed water is poured along the electrode plate into each of the anode chamber and the cathode chamber for electrolysis. The general-purpose electrode plates are alternately stacked to connect the through holes to each other. Alone, an anode chamber between the cathode chamber together without using a connecting member such as a packing is it possible to provide a high-performance electrolytic cell is connected in communication.

【0015】上記(2)で述べた請求項2に係る手段に
よれば、ボス状の通孔に形成したスプライン状の切欠き
溝から、送られて来る電解水を隔膜プレートによって仕
切られた陽極室又は陰極室の内部に対して各電極板に沿
って流し込んで、電気分解することを可能にする。
According to the second aspect of the invention described in (2) above, the electrolyzed water sent from the spline-shaped notch groove formed in the boss-shaped through hole is partitioned by the diaphragm plate. It can be poured along the electrode plates into the interior of the chamber or cathode chamber for electrolysis.

【0016】上記(3)で述べた請求項3に係る手段に
よれば、電解作用に於いて母材、即ち、電極板自身が浸
食されることがなく、水漏れ防止と母材材料の溶出を防
止することを可能にする。
According to the third aspect of the invention described in (3) above, the base material, that is, the electrode plate itself is not corroded during the electrolytic action, preventing water leakage and eluting the base material. It is possible to prevent.

【0017】以上の如くであるから、上記(1)〜
(3)の手段によって上述した技術的課題を解決して、
前記従来の技術の問題点を解消することができる。
As described above, the above (1)-
By solving the above-mentioned technical problem by the means of (3),
It is possible to solve the problems of the conventional technology.

【0018】[0018]

【発明の実施の形態】以下に、本発明に係る電解槽の実
施の形態を図面と共に説明すると、図1の(イ)は本発
明の電解槽を構成する電極板1の構成を示した正面図、
(ロ)はその側面図を示し、図2の(イ)は図1(イ)
のY−Y線に沿った断面図、(ロ)、(ハ)、(ニ)は
夫々X−X線とW−W線並びにZ−Z線に沿った断面図
を示したものであって、全体をポリプロピレン等のプラ
スチック材を用いて一体成形して成るこの電極板1は、
上記の各図に示すように電極を形成する本体1Rの部分
を比較的肉薄に形成し、周縁の表裏には厚肉のリブ1K
を一体形成すると共に、上辺に電源からの端子を接続す
るフランジ1Tを突設した全体が略矩形状を成し、少く
とも上記の電極を形成する本体1Rの表裏両面1Ra,
1Raの部分には、白金層を形成するように構成されて
いる。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, an embodiment of an electrolytic cell according to the present invention will be described with reference to the drawings. FIG. 1 (a) is a front view showing the structure of an electrode plate 1 constituting the electrolytic cell of the present invention. Figure,
2B shows a side view thereof, and FIG. 2A shows FIG. 1A.
Of (b), (c), and (d) are cross-sectional views taken along line X-X, line W-W, and line Z-Z, respectively. The electrode plate 1 integrally formed by integrally molding a plastic material such as polypropylene,
As shown in each of the above figures, the portion of the main body 1R forming the electrode is formed to be relatively thin, and thick ribs 1K are formed on the front and back sides of the periphery.
And a flange 1T for connecting a terminal from a power supply to the upper side of the main body 1R, which has at least the above-mentioned electrodes and which has at least the above-mentioned electrodes.
The 1Ra portion is configured to form a platinum layer.

【0019】1S…は上記厚肉のリブ1Kに間隔をあけ
て多数設けた突起部、1Sa…はこれ等各突起部1S…
に穿設した締付ボルト用の挿通穴、1Taは上記のフラ
ンジ1Tに設けた端子接続用の穴であって、当該電極板
1を陽極板として用いる場合はプラス極の端子が接続さ
れ、反対に陰極板として用いる場合にはマイナス極の端
子が接続される仕組に成っている。
1S ... Protrusions provided in large numbers on the thick rib 1K at intervals, 1Sa ... Protrusions 1S ...
Insertion holes for tightening bolts, which are drilled in 1 and 1Ta, are holes for connecting terminals provided in the flange 1T, and when the electrode plate 1 is used as an anode plate, a positive electrode terminal is connected and When it is used as a cathode plate, it has a structure in which a negative electrode terminal is connected.

【0020】同じく図1と図2に於いて、2,3,4,
5は上記電極板1の四隅の対称位置に設けた電解水を流
通させるための通孔であって、これ等4個の通孔2〜5
のうち、一方の対角線上に位置する上下2つの通孔3,
4を、電極板1に対して直角方向への直流通路3a,4
aを備えた筒状の通孔と成し、他方の対角線上に位置す
る上下2つの通孔2,5が、電極板1に沿った方向に電
解水を流すスプライン状の切り欠き溝2a,5a(迂回
通路)を設けたボス状の通孔に成っている。
Similarly, in FIGS. 1 and 2, 2, 3, 4,
Reference numeral 5 is a through-hole provided at symmetrical positions at the four corners of the electrode plate 1 for passing the electrolyzed water, and these four through-holes 2 to 5 are provided.
Of the two upper and lower through holes 3, which are located on one diagonal line
4 is a DC passage 3a, 4 in a direction perpendicular to the electrode plate 1.
a cylindrical through hole provided with a, and two upper and lower through holes 2 and 5 located on the other diagonal line are spline-shaped notch grooves 2a for flowing electrolyzed water in the direction along the electrode plate 1, It is formed as a boss-shaped through hole provided with 5a (a bypass passage).

【0021】図3の(イ)は、上記4枚の電極板1…を
上下を逆さにして交互に重ねて取付けることによって構
成した本発明に係る電解槽の一部断面側面図で、(ロ)
はその一部断面平面図を示したものであって、重ねた計
4枚の電極板1…は、各図に示すように各挿通穴1Sa
…に締付ボルト6…を挿通してナット7…で締付ること
により、一体的に組付けられるものであるが、これ等各
電極板1の組付けに当っては、各電極板1の間に図7に
示すように全体をイオン交換樹脂を用いて矩形状に形成
した隔膜プレート13が介在されて、各電極板1…の間
に形成される電解室を陽極室1Ha…と陰極室1Hb…
に区画するように構成されている。
FIG. 3A is a partial cross-sectional side view of the electrolytic cell according to the present invention constructed by mounting the above four electrode plates 1 ... )
Shows a partial cross-sectional plan view thereof, and a total of four stacked electrode plates 1 ... Show each insertion hole 1Sa as shown in each drawing.
It is integrally assembled by inserting the tightening bolts 6 into the nuts and tightening them with the nuts 7. In assembling the electrode plates 1, the electrode plates 1 As shown in FIG. 7, a diaphragm plate 13 having a rectangular shape entirely made of an ion exchange resin is interposed between the electrode plates 1 ... Chamber 1Hb ...
It is configured to partition into.

【0022】即ち、図3の(イ)に示す如く重ねて組付
けた計4枚の電極板1…のうち、フランジ1Tを上方に
突出した左から1番目と3番目の電極板にプラス極を接
続することによって、これ等を陽極板とし、同じくフラ
ンジ1Tを下方に突出した左から2番目と4番目の電極
板にマイナス極を接続することによって、これ等を陰極
板とした場合には、各陽極板1…と隔膜プレート13…
の間を夫々陽極室1Ha…とする一方、各陰極板1…と
隔膜プレート13…の間が夫々陰極室1Hb…と成るよ
うに構成されている。
That is, of the four electrode plates 1 ... Assembled in a stack as shown in FIG. 3A, the flanges 1T are projected upward and the first and third electrode plates from the left are positive electrodes. When these are used as a cathode plate by connecting these to the anode plate and by connecting the negative electrodes to the second and fourth electrode plates from the left, which also project the flange 1T downward, , Each anode plate 1 ... and diaphragm plate 13 ...
The spaces between the cathode plates 1 ... and the diaphragm plates 13 ... Are respectively defined as the cathode chambers 1Hb.

【0023】また、以上の如く各電極板1…(陽極板と
陰極板)を上下逆さにして交互に重ねて取付けた場合に
は、上述した筒状の通孔3,4とボス状の通孔2,5
が、図5並びに図6の各(ロ)に示した断面図の如く、
その各通孔口3′,4′と2′,5′同士が連通状態に
接続されるように、各通孔口3′,4′と2′,5′が
接合自在な嵌込み形状に造られている。
Further, when the electrode plates 1 (anode plate and cathode plate) are mounted upside down alternately and alternately, as described above, the above-mentioned cylindrical through holes 3 and 4 and the boss-like through holes 3 and 4 are attached. Holes 2, 5
However, as shown in the sectional views shown in (b) of FIGS. 5 and 6,
Each of the through holes 3 ', 4'and 2', 5'has a fitting shape that can be joined so that the through holes 3 ', 4'and 2', 5'are connected to each other in a communicating state. It is built.

【0024】図3に於いて8と9は、ケーシングを兼ね
る第1番目の電極板1の下側の筒状通孔4とボス状通孔
5に嵌込み接続した電解水給水用のジョイントパイプ、
10と11は同じくケーシングを兼ねる第4番目の電極
板1の上側の筒状通孔4に嵌込み接続した酸性水取出し
用のジョイントパイプと、同じく上側のボス状通孔5に
嵌込み接続したアルカリ水取出し用のジヨイントパイプ
を示し、更に、図3乃至図6に於いて12B,12Dと
12A,12Cは、第1番目の電極板1の上側のボス状
通孔2と筒状通孔3、並びに、第4番目の電極板1の下
側の筒状通孔3とボス状通孔2を夫々塞ぐ栓を示す。
In FIG. 3, reference numerals 8 and 9 denote joint pipes for fitting and supplying electrolyzed water, which are fitted and connected to the lower cylindrical through hole 4 and the boss through hole 5 of the first electrode plate 1 which also serves as a casing. ,
10 and 11 are joint pipes for taking out acidic water, which are fitted and connected to the upper cylindrical through hole 4 of the fourth electrode plate 1 which also serves as a casing, and are also fitted and connected to the upper boss-like through hole 5 similarly. A joint pipe for taking out alkaline water is shown, and 12B, 12D and 12A, 12C in FIGS. 3 to 6 are boss-shaped through holes 2 and cylindrical through holes on the upper side of the first electrode plate 1. 3 and plugs that close the cylindrical through hole 3 and the boss-like through hole 2 on the lower side of the fourth electrode plate 1, respectively.

【0025】図4は図3の如く組立てた本発明に係る電
解槽の正面図、図5(イ)は図4に於けるA−B−C−
D−E−F−G−H線に沿った断面図で、(ロ)はその
M矢視部を取出して示した分解断面図、図6(イ)は同
じく図4に於けるA−B−J−E−D−K−G−H線に
沿った断面図で、(ロ)はそのN矢視部を取出して示し
た分解断面図であって、図5の(イ)は酸性水を得るた
めの電解室の構造とその流通経路を示し、図6の(イ)
はアルカリ水を得るための電解室の構造とその流通経路
を示したものである。
FIG. 4 is a front view of the electrolytic cell according to the present invention assembled as shown in FIG. 3, and FIG. 5 (A) is an ABC line in FIG.
6 is a cross-sectional view taken along the line D-E-F-G-H, in which (B) is an exploded cross-sectional view showing the M arrow section, and FIG. 6A is also an A-B line in FIG. 5B is a cross-sectional view taken along the line J-E-D-K-G-H, where (B) is an exploded cross-sectional view showing the N arrow portion, and (A) of FIG. The structure of the electrolysis chamber and its distribution path for obtaining
Shows the structure of an electrolysis chamber for obtaining alkaline water and its distribution route.

【0026】また、上述した各図に於いて16…は隔膜
プレート13…を取付けるためのシールパッキンを示
し、図7に於いて13a…は隔膜プレート13の四隅に
形成したボス状通孔2,5及び筒状通孔3,4を挿通す
るための各嵌込穴を示す。
Further, in each of the above-mentioned drawings, 16 indicates a seal packing for attaching the diaphragm plate 13, and in FIG. 7, 13a indicates a boss-shaped through hole 2 formed at the four corners of the diaphragm plate 13. 5 and the fitting holes for inserting the cylindrical through holes 3 and 4 are shown.

【0027】本発明に係る電解槽は以上述べた如き構成
であるから、図3乃至図6に示すように複数枚の電極板
1…を重ねて電解槽を組立て、且つ、上方に突出してい
る各フランジ1T,1Tの穴1Ta,1Taにプラス極
の端子を接続し、下方に突出している各フランジ1T,
1Tの穴1Ta,1Taにマイナス極の端子を接続して
通電すると共に、各給水用のジヨイントパイプ8,9に
電解水の給水ホース(図示省略)を接続して給水すれ
ば、一方のジョイントパイプ8側から給水された電解水
は、図5の(イ)に示すようにボス状通孔2と5の各ス
プライン状の切り欠き溝2a…,5a…と、筒状通孔
3,4の直角流路3a,4aを通って各陽極室1Ha…
内を矢印に示すように順番に流通して電気分解され、取
出し用の一方のジョイントパイプ10側から酸性水を取
出すことができる。
Since the electrolytic cell according to the present invention has the structure as described above, as shown in FIGS. 3 to 6, a plurality of electrode plates 1 are stacked to assemble the electrolytic cell and project upward. A positive pole terminal is connected to the holes 1Ta and 1Ta of the flanges 1T and 1T, and the flanges 1T and 1T projecting downwardly.
Connect the negative pole terminal to the 1T holes 1Ta, 1Ta to energize, and connect the water supply hoses (not shown) to the water supply joint pipes 8 and 9 to supply water. The electrolyzed water supplied from the pipe 8 side is, as shown in FIG. 5A, each of the spline-shaped cutout grooves 2a ..., 5a ... Of the boss-shaped through holes 2 and 5, and the cylindrical through holes 3, 4. Each of the anode chambers 1Ha ...
The acidic water can be taken out from one of the joint pipes 10 for taking out by flowing in order as shown by an arrow and electrolyzed.

【0028】また、他方のジョイントパイプ9側から給
水ホース(図示省略)を通して給水された電解水は、図
6の(イ)に示す矢印の経路を辿って各陰極室1Hb…
内を順番に流通して電気分解され、取出し用の他方のジ
ョイントパイプ11側からアルカリ水を取出すことがで
きる。
The electrolyzed water supplied from the other joint pipe 9 side through a water supply hose (not shown) follows the path of the arrow shown in FIG. 6 (a) to each cathode chamber 1Hb ...
The alkaline water can be taken out from the other joint pipe 11 side for taking out by flowing through the inside sequentially and electrolyzed.

【0029】尚、図面では計4枚の電極板1…を重ねて
組付けることによって電解槽を構成しているが、これは
実施の一例であって、電解槽の用途や単位時間当りの取
出し量等によって、その組付枚数を必要に応じて任意に
設定して、その都度要求に応じた仕様で電解槽を組立て
ることができることは勿論である。
In the drawing, the electrolytic cell is constructed by assembling a total of four electrode plates 1 ..., This is an example of the embodiment, and the use of the electrolytic cell and the removal per unit time are shown. Of course, it is possible to assemble the electrolytic cell with the specifications according to the requirements by setting the number of the assembled sheets arbitrarily according to the amount and the like.

【0030】[0030]

【発明の効果】以上述べた次第で、本発明に係る電解槽
によれば汎用化した電極板を必要枚数重ねて組付けるこ
とによって、要求に応じた仕様の電解槽を提供すること
ができるのであるが、本発明では特に、各電極板を重ね
て電解水の流路を形成するに当って、各種パッキン等の
流路形成用の部材及び部品類を必要とせず、各電極板を
上下を逆さにして交互に重ねて組付けるだけで、陽極室
と陰極室と、これ等各室に通じる各流路を形成できるた
め、あらゆる用途に対応できる電解槽を必要最小限の部
品を用いて極めて簡単に組立てることができる経済性を
発揮できるものであって、コストダウンを可能にした
点、並びに、チタンの溶解防止と電解槽の水漏れも防止
できる点と相俟って、信頼性の高い電解槽を提供するこ
とができる。
As described above, according to the electrolytic cell of the present invention, it is possible to provide the electrolytic cell having the specifications according to the requirements by assembling the required number of general-purpose electrode plates in an overlapping manner. However, in the present invention, in particular, in forming the flow path of the electrolytic water by stacking the electrode plates, the members and parts for forming the flow path such as various packings are not required, and The anode chamber, cathode chamber, and each flow path leading to these chambers can be formed by simply assembling them upside down and alternately. It is easy to assemble and economically effective, and it is highly reliable in combination with the fact that it is possible to reduce the cost, as well as preventing the dissolution of titanium and preventing water leakage from the electrolytic cell. An electrolytic cell can be provided.

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

【図1】(イ)は本発明で用いる電極板の正面図で、
(ロ)はその側面図である。
FIG. 1A is a front view of an electrode plate used in the present invention.
(B) is a side view thereof.

【図2】(イ)は図1(イ)のY−Y線に沿った断面図
で、(ロ)は同じくX−X線に沿った断面図、(ハ)は
同じくW−W線に沿った断面図で、(ニ)は同じくZ−
Z線に沿った断面図である。
2A is a sectional view taken along line YY of FIG. 1A, FIG. 2B is a sectional view taken along line XX, and FIG. 2C is a sectional view taken along line WW. In the sectional view along, (d) is also Z-
It is sectional drawing which followed the Z line.

【図3】(イ)は組立てられた本発明に係る電解槽の一
部断面側面図で、(ロ)はその一部断面平面図である。
FIG. 3A is a partially sectional side view of the assembled electrolytic cell according to the present invention, and FIG. 3B is a partially sectional plan view thereof.

【図4】本発明に係る電解槽の正面図である。FIG. 4 is a front view of an electrolytic cell according to the present invention.

【図5】(イ)は図4に於けるA−B−C−D−E−F
−G−H線に沿った断面図で、(ロ)はそのM視部分を
取出して示した分解断面図である。
FIG. 5 (A) is A-B-C-D-E-F in FIG.
It is a sectional view taken along the line -GH, and (B) is an exploded sectional view showing an M view portion thereof.

【図6】(イ)は図4に於けるA−B−J−E−D−K
−G−H線に沿った断面図で、(ロ)はそのN矢視部分
を取出して示した分解断面図である。
FIG. 6A is ABJDEK in FIG.
It is a sectional view taken along the line -GH, and (B) is an exploded sectional view showing the portion viewed from the arrow N.

【図7】隔膜プレートの一部破断正面図である。FIG. 7 is a partially cutaway front view of the diaphragm plate.

【図8】従来の電解槽を説明した構成図である。FIG. 8 is a configuration diagram illustrating a conventional electrolytic cell.

【符号の説明】[Explanation of symbols]

1 電極板 1Ha 陽極室 1Hb 陰極室 2,5 ボス状の通孔 2a,5a スプライン状の切り欠き溝 3,4 筒状の通孔 3a,4a 直角流路 13 隔膜プレート 1 electrode plate 1 Ha anode chamber 1Hb cathode chamber 2,5 Boss-shaped through hole 2a, 5a Spline-shaped notch groove 3,4 Cylindrical through hole 3a, 4a right-angled flow path 13 diaphragm plate

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C02F 1/46 ─────────────────────────────────────────────────── ─── Continuation of the front page (58) Fields surveyed (Int.Cl. 7 , DB name) C02F 1/46

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 同じ形状に形成した陽極板と陰極板を中
間に隔膜プレートを介在させて重ねて取付け、陽極板と
隔膜プレートの間を陽極室とし、陰極板と隔膜プレート
の間を陰極室として、これ等陽極室と陰極室に電解水を
送り込んで電気分解することにより、陽極室から酸性水
を取出し、陰極室からはアルカリ水を取出すように構成
した電解槽であって、 上記陽極板と陰極板の双方を構成する電極板の四隅対称
位置に電解水用の4個の通孔を穿設し、これ等の通孔の
うち一方の対角線上に位置する上下2つの通孔を、電極
板に対して直角方向への直角流路を備えた筒状の通孔と
成し、他方の対角線上に位置する上下2つの通孔を、電
極板に沿った方向に流れる迂回通路を備えたボス状の通
孔と成すと共に、上記の電極板を上下を逆さにして交互
に重ねて取付けることにより、上記筒状とボス状に形成
した各通孔口同士を連通接続自在に構成したことを特徴
とする電解槽。
1. An anode plate and a cathode plate, which are formed in the same shape, are mounted so as to overlap with each other with a diaphragm plate interposed therebetween, an anode chamber is provided between the anode plate and the diaphragm plate, and a cathode chamber is provided between the cathode plate and the diaphragm plate. As an electrolytic cell configured so as to extract acidic water from the anode chamber and alkaline water from the cathode chamber by sending electrolyzed water to the anode chamber and the cathode chamber for electrolysis, And four through holes for electrolyzed water are formed at four corner symmetrical positions of the electrode plate that constitutes both the cathode plate and two through holes located on one diagonal line of these through holes, A tubular through hole having a right-angled flow path in a direction perpendicular to the electrode plate is formed, and upper and lower two through holes located on the other diagonal line are provided with detour passages flowing in a direction along the electrode plate. And the above electrode plate upside down. By attaching each other overlap, the electrolytic cell, characterized in that the connecting stub freely configure each through hole opening between formed in the cylindrical boss shape.
【請求項2】 電極板に沿った方向に流れる迂回通路を
備えたボス状の通孔が、ボスの周囲にスプライン状の切
り欠き溝を形成して成ることを特徴とする請求項1記載
の電解槽。
2. A boss-shaped through hole having a bypass passage that flows in a direction along the electrode plate is formed by forming a spline-shaped cutout groove around the boss. Electrolyzer.
【請求項3】 陽極板と陰極板の双方を構成する電極板
の全体をプラスチック材を用いて構成すると共に、この
プラスチック製電極板の少くとも電極を形成する部分に
白金層を形成したことを特徴とする請求項1記載の電解
槽。
3. An electrode plate constituting both an anode plate and a cathode plate is entirely made of a plastic material, and a platinum layer is formed on at least a portion of the plastic electrode plate where an electrode is formed. The electrolytic cell according to claim 1, which is characterized in that.
JP28258797A 1997-09-30 1997-09-30 Electrolytic cell Expired - Fee Related JP3497357B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28258797A JP3497357B2 (en) 1997-09-30 1997-09-30 Electrolytic cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28258797A JP3497357B2 (en) 1997-09-30 1997-09-30 Electrolytic cell

Publications (2)

Publication Number Publication Date
JPH11104641A JPH11104641A (en) 1999-04-20
JP3497357B2 true JP3497357B2 (en) 2004-02-16

Family

ID=17654451

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28258797A Expired - Fee Related JP3497357B2 (en) 1997-09-30 1997-09-30 Electrolytic cell

Country Status (1)

Country Link
JP (1) JP3497357B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004102710A1 (en) * 2003-05-16 2004-11-25 Hydrogenics Corporation Symmetrical flow field plates
KR100827929B1 (en) 2007-03-08 2008-05-08 순천대학교 산학협력단 Electrolytic cell

Also Published As

Publication number Publication date
JPH11104641A (en) 1999-04-20

Similar Documents

Publication Publication Date Title
JP2652609B2 (en) Electrolyzed water generator
JPH07115017B2 (en) Electrolytic unit for generating electrolyzed water
JPS60185375A (en) Galvanic cell
JP3497357B2 (en) Electrolytic cell
JPH0338293A (en) Apparatus for continuous production of electrolytic water
EP3186411A1 (en) Hydrogen and oxygen generator
US6200435B1 (en) Ion exchange membrane electrolyzer
JPH10309581A (en) Electrolytic cell of ionized water generator
JP3322988B2 (en) Electrolyzed water generator
JP3583329B2 (en) Electrolyzer for electrolyzed water generator
JP2944068B2 (en) Continuous electrolyzed water generator
JP2920345B2 (en) Electrolytic ionic water generator
CN218025539U (en) Salt chlorine machine shell and salt chlorine machine
JP2621070B2 (en) Continuous electrolyzed water generator
CA3125094C (en) Chamber frame element, electrolyzer, and electrodialysis cell
JP2580193Y2 (en) Electrolyzer for ion water generator
JPS5847994Y2 (en) Ionic water conditioner diaphragm
CN209804113U (en) Defoaming device for teaching bubble development
JPS5847993Y2 (en) Cylindrical electrolyzer
CN2743368Y (en) Fixture type electrolytic cell structure
JPH07595U (en) Ionized water generator electrolyzer unit panel
JPH064223Y2 (en) Plate type heat exchanger
KR20010078426A (en) Dialysis membrane cell unit for fresh-waterizing of sea-water
JPH03157188A (en) Apparatus for producing ionized water by electrolysis
JP3592095B2 (en) Electrolyzed water generator

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081128

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081128

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091128

Year of fee payment: 6

LAPS Cancellation because of no payment of annual fees