JP2605708Y2 - Electrolytic cell - Google Patents

Electrolytic cell

Info

Publication number
JP2605708Y2
JP2605708Y2 JP1993008014U JP801493U JP2605708Y2 JP 2605708 Y2 JP2605708 Y2 JP 2605708Y2 JP 1993008014 U JP1993008014 U JP 1993008014U JP 801493 U JP801493 U JP 801493U JP 2605708 Y2 JP2605708 Y2 JP 2605708Y2
Authority
JP
Japan
Prior art keywords
electrolytic cell
chamber frame
chamber
pipe
frame
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
JP1993008014U
Other languages
Japanese (ja)
Other versions
JPH0661970U (en
Inventor
秀司 中松
善則 錦
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.)
De Nora Permelec Ltd
Original Assignee
Permelec Electrode 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 Permelec Electrode Ltd filed Critical Permelec Electrode Ltd
Priority to JP1993008014U priority Critical patent/JP2605708Y2/en
Publication of JPH0661970U publication Critical patent/JPH0661970U/en
Application granted granted Critical
Publication of JP2605708Y2 publication Critical patent/JP2605708Y2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • Y02E60/50Fuel cells

Landscapes

  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Sealing Battery Cases Or Jackets (AREA)
  • Filling, Topping-Up Batteries (AREA)

Description

【考案の詳細な説明】[Detailed description of the invention]

【0001】[0001]

【産業上の利用分野】本考案は、電気分解や電池等の電
気化学工業の分野において使用される電解槽に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolytic cell used in the electrochemical industry such as electrolysis and batteries.

【0002】[0002]

【従来技術とその問題点】水電解、食塩電解、芒硝電
解、海水電解、有機電解又は燃料電池等の電気化学的プ
ロセスでは、目的及び用途に応じて種々の電解槽が利用
されているが、該電解槽は電力原単位の低減、設備コス
トの低減のため、複数の単位電解槽を積層させた構造で
あり(例えば特開昭57−210980号)、これらの極間距離
や各構成部品間の厚さは極力小さくし組み立てられて製
造される電解槽の小型化を図ることが望ましい。一方単
位電解槽への気液流通のためにノズルや配管を設けるの
が一般的であるが、その加工は複雑かつ高価であり、該
ノズル等の存在は極間距離や部品厚減少の妨げになって
いる。更に従来の硬質の電解室枠を使用し積層型電解槽
を組み立てる際には積層方向に向かって加圧する必要が
あり該加圧による室枠間の接触による磨耗等を防止する
ために、室枠間の空間にガスケットを設置しているが、
該ガスケットを設置するために手間が掛かりかつ該ガス
ケットは前述の電解槽の小型化の障害となっている。
2. Description of the Related Art Various electrochemical cells are used in electrochemical processes such as water electrolysis, salt electrolysis, sodium salt electrolysis, seawater electrolysis, organic electrolysis, and fuel cells, depending on the purpose and application. The electrolyzer has a structure in which a plurality of unit electrolyzers are stacked in order to reduce the unit power consumption and the equipment cost (for example, JP-A-57-210980). It is desirable to reduce the thickness of the electrolytic cell as much as possible so as to reduce the size of the assembled electrolytic cell. On the other hand, nozzles and pipes are generally provided for gas-liquid circulation to the unit electrolytic cell, but the processing is complicated and expensive, and the presence of the nozzles and the like hinders the reduction of the distance between the electrodes and the thickness of parts. Has become. Furthermore, when assembling a laminated electrolytic cell using a conventional hard electrolytic chamber frame, it is necessary to pressurize in the laminating direction. Gaskets are installed in the space between
It takes time and effort to install the gasket, and the gasket is an obstacle to the miniaturization of the aforementioned electrolytic cell.

【0003】本考案は、上述の電解槽の小型化を阻害す
る各原因を除去し、特に部品数の減少を意図しこれによ
り構造を簡略にした前述の各種電解用電解槽を提供する
ことを目的とする。
An object of the present invention is to provide various electrolytic cells for electrolysis as described above, which eliminate the above-mentioned factors which hinder the miniaturization of the electrolytic cell, and in particular reduce the number of parts and thereby simplify the structure. Aim.

【0004】[0004]

【問題点を解決するための手段】本考案は、額縁状の室
枠及び該室枠の周縁を貫通し室枠構成材料より弾性率の
大きい材料から成る電解液導入配管及び電解液排出用配
管を含んで成ることを特徴とする電解である。以下本
考案を詳細に説明する。
[Means for Solving the Problems] The present invention provides a frame-shaped chamber.
An electrolytic cell which is characterized in that it comprises a frame and the chamber frame rim electrolyte inlet pipe and an electrolyte discharge pipe comprising a material having a large elastic modulus from penetrating chamber frame component material. Hereinafter, the present invention will be described in detail.

【0005】本考案に係わる電解槽の室枠は、電解液導
入及び排出用配管を有する電解槽の室枠にシール材(ガ
スケット)としての機能を合わせ持たせることにより、
ガスケットを別個に設置する手間を省略し、部品数を減
少させて前記室枠を使用して電解槽を組み立てた際の装
置全体の厚さも減少させて小型化を図るようにしたこと
を特徴としている。この特徴を実現するためには、前記
配管及び室枠と、前記イオン交換膜と室枠の周縁部とが
十分に密着して電解液やガスの漏洩が生じないようにし
なければならない。従って室枠及び配管を構成する材料
は弾性体とし、その材質は使用する環境によって選択さ
れるが、耐蝕性及び高温耐性の点からフッ素ゴムが望ま
しい。この室枠には配管貫通孔を穿設しあるいは2分割
した室枠の分割面に配管固定用の溝を形成するが、後者
の場合には平滑な分割面の間に配管を位置させ単位電解
槽の積層方向の加圧により密閉できるのであれば溝の形
成を省略してもよい。
The chamber frame of the electrolytic cell according to the present invention has a function as a sealing material (gasket) by being combined with the chamber frame of the electrolytic cell having a pipe for introducing and discharging the electrolyte.
The step of separately installing the gasket is omitted, the number of parts is reduced, and the thickness of the entire apparatus when the electrolytic cell is assembled using the chamber frame is also reduced to reduce the size. I have. In order to realize this feature, the piping and the chamber frame, the ion exchange membrane and the peripheral edge of the chamber frame must be sufficiently adhered to each other so that leakage of the electrolytic solution and gas does not occur. Therefore, the material constituting the chamber frame and the piping is an elastic body, and the material is selected depending on the environment in which it is used. However, fluorine rubber is desirable from the viewpoint of corrosion resistance and high temperature resistance. In this chamber frame, a pipe through hole is formed or a groove for fixing the pipe is formed in the divided surface of the divided chamber frame. In the latter case, the pipe is positioned between the smooth divided surfaces and the unit electrolysis is performed. The formation of the groove may be omitted as long as it can be hermetically sealed by pressing in the laminating direction of the tank.

【0006】又配管構成材料は前記室枠構成材料より弾
性率の大きい材料から選択され、特に室枠内に存在する
部分は電解液及び発生ガスに耐性を有する材料で構成す
る。これらの材料としては金属や樹脂等がある。配管を
複数本設置する場合にはモジュール化した配管を使用す
ることが好ましい。この配管の室枠側先端は室枠の内縁
から数センチの範囲で室枠内に位置するように固定する
ことが望ましい。又後述の通り該室枠を含む複数の単位
電解槽を加圧して一体化する際のシール性を向上させる
ために、配管径tP は室枠厚tG より小さくすべきであ
り、好ましくはtP ×1.5 <tG となるように設計す
る。
The piping material is selected from materials having a higher elastic modulus than the material of the chamber frame. In particular, the portion existing in the chamber frame is made of a material having resistance to the electrolytic solution and generated gas. These materials include metals and resins. When installing a plurality of pipes, it is preferable to use modularized pipes. It is desirable that the front end of the pipe on the chamber frame side is fixed so as to be positioned within the chamber frame within a range of several centimeters from the inner edge of the chamber frame. Further, as described later, in order to improve the sealing property when a plurality of unit electrolytic cells including the chamber frame are integrated by pressurizing, the pipe diameter t P should be smaller than the chamber frame thickness t G , preferably is designed in such a way that t P × 1.5 <t G.

【0007】このような構成から成る前記室枠は通常の
電解用の電解槽や電気透析槽等を構成する単位部材とし
て使用することができる。該室枠は通常の電解槽の場合
には中間室として使用する際を除いて電極を設置し、電
気透析槽の両端室以外や通常の電解槽の中間室として使
用する場合には電極を設置せずに使用する。電極を設置
する場合には額縁状の前記室枠の開口部を閉塞するよう
設置することが望ましく、所定の電解反応に応じた電極
物質例えば白金族金属酸化物が被覆されたプレート又は
エキスパンドメタル等を使用する。なお単位電解槽の厚
さを一定に保持するために剛性のスペーサーを室枠間に
位置させてもよい。
The above-mentioned chamber frame having such a structure can be used as a unit member constituting an ordinary electrolytic cell or electrodialysis cell for electrolysis. In the case of a normal electrolytic cell, the electrode is installed except when it is used as an intermediate chamber in the case of a normal electrolytic cell. Use without. When installing an electrode, it is desirable to install so as to close the opening of the frame-shaped chamber frame, an electrode material corresponding to a predetermined electrolytic reaction, for example, a plate or an expanded metal coated with a platinum group metal oxide, etc. Use Note that a rigid spacer may be located between the chamber frames in order to keep the thickness of the unit electrolytic cell constant.

【0008】前記室枠はイオン交換膜を介して積層しか
つ積層方向に加圧して一体化して電解槽を構成すること
が望ましい。該一体化は例えば前記複数の室枠の両端に
位置する端壁の締着孔間をタイロッドで締着することに
より行うことができる。この締着の際に従来の室枠の締
着では隣接する1対の金属製室枠間にガスケットを挿入
して前記両室枠の接触を防止していたが、本考案では弾
性体から成る室枠の周縁部の室枠がガスケットも兼ねる
ため、別個にガスケットを設置する必要がなく、これに
より部品点数と全体の電解槽の厚さを減少することがで
きる。
It is desirable that the chamber frames are laminated via an ion exchange membrane and pressurized in the laminating direction to be integrated to constitute an electrolytic cell. The integration can be performed, for example, by fastening between the fastening holes of the end walls located at both ends of the plurality of chamber frames with a tie rod. At the time of this fastening, in the conventional fastening of the chamber frame, a gasket is inserted between a pair of adjacent metal chamber frames to prevent the contact between the two chamber frames, but in the present invention, it is made of an elastic body. Since the chamber frame at the peripheral edge of the chamber frame also serves as a gasket, it is not necessary to separately provide a gasket, thereby reducing the number of parts and the thickness of the entire electrolytic cell.

【0009】次に添付図面に示す実施例に基づいて本考
案に係わる電解槽を説明する。図1は本考案に係わる室
枠を電極及びイオン交換膜とともに積層して構成した電
解槽の一例を示す斜視図、図2は図1のA−A線縦断面
図、図3は図1のB−B線横断面図である。単位電解槽
1は、開口部2を有する額縁状のフッ素ゴム等の材料か
ら成り、該単位電解槽1は外縁形状が一致するイオン交
換膜3により隣接する単位電解槽(図示略)と積層さ
れ、同様にして複数の単位電解槽がイオン交換膜を介し
て積層されている。
Next, an electrolytic cell according to the present invention will be described based on an embodiment shown in the accompanying drawings. FIG. 1 is a perspective view showing an example of an electrolytic cell in which a chamber frame according to the present invention is laminated with electrodes and an ion exchange membrane, FIG. 2 is a longitudinal sectional view taken along the line AA of FIG. 1, and FIG. It is a BB cross-sectional view. The unit electrolytic cell 1 is made of a material such as a frame-shaped fluororubber having an opening 2 and the unit electrolytic cell 1 is laminated with an adjacent unit electrolytic cell (not shown) by an ion-exchange membrane 3 having the same outer edge shape. Similarly, a plurality of unit electrolytic cells are stacked via an ion exchange membrane.

【0010】前記単位電解槽1の室枠4は前記イオン交
換膜3と平行に2分割されて1対の半割室枠4aが形成
され、該半割室枠4aの分割面の上下の周縁部には各3
個の縦方向の半円状の溝5が形成されている。又半割室
枠4aの一方の前記開口部2(図2では左側)の周縁に
は段部6が形成され、該段部6には電極活性物質である
白金族金属酸化物が被覆されたチタン製基材である電極
構造体7の周縁部が固定されている。両半割室枠4aは
それぞれの分割面が接触して前記1対の溝5により円形
の貫通孔が形成され、該貫通孔には中空で前記室枠より
弾性率の大きい材料により構成された配管8が挿入され
ている。
The chamber frame 4 of the unit electrolytic cell 1 is divided into two parts in parallel with the ion exchange membrane 3 to form a pair of half chamber frames 4a, and the upper and lower peripheral edges of the divided surface of the half chamber frame 4a. Each part is 3
A plurality of vertical semicircular grooves 5 are formed. A step 6 is formed at the periphery of one of the openings 2 (left side in FIG. 2) of the half chamber frame 4a, and the step 6 is coated with a platinum group metal oxide which is an electrode active substance. The periphery of the electrode structure 7, which is a titanium base material, is fixed. The two divided chamber frames 4a are in contact with their respective divided surfaces to form a circular through-hole by the pair of grooves 5, and the through-hole is formed of a hollow material having a higher elastic modulus than the chamber frame. The pipe 8 is inserted.

【0011】図1の複数の単位電解槽1を積層方向に加
圧すると、各単位電解槽1及びイオン交換膜3が部分的
に変形しかつ密着して一体化された電解槽が構成され
る。前記変形により単位電解槽1の室枠4とイオン交換
膜3が密着しかつ配管8が周囲の半割室枠4aにより加
圧されて両者が強固な気密状態が形成されて電解液や発
生ガスの漏洩のない電解槽が構成される。図4は、本考
案の電解槽の他の実施例に係わる室枠の正面図である。
この単位電解槽1aの5本の配管は互いにその基端部が
束ねられてモジュール化している以外は図1〜3の単位
電解槽と同一である。図4の単位電解槽1aでは、電解
液の導入及び排出を束ねられた主導入配管8a及び主排
出配管8bにより行うことがてき、図1〜3の単位電解
槽のように各配管ごとに行う必要がないため、より有利
である。
When a plurality of unit electrolytic cells 1 in FIG. 1 are pressurized in the laminating direction, each of the unit electrolytic cells 1 and the ion exchange membrane 3 are partially deformed and closely adhered to form an electrolytic cell. . Due to the deformation, the chamber frame 4 of the unit electrolytic cell 1 and the ion-exchange membrane 3 come into close contact with each other, and the pipe 8 is pressurized by the surrounding half-chamber frame 4a, so that both are formed in a tight airtight state. An electrolyzer with no leakage is constructed. FIG. 4 is a front view of a chamber frame according to another embodiment of the electrolytic cell of the present invention.
The five pipes of the unit electrolytic cell 1a are the same as the unit electrolytic cells of FIGS. 1 to 3 except that their base ends are bundled and modularized. In the unit electrolytic cell 1a of FIG. 4, the introduction and discharge of the electrolytic solution can be performed by the bundled main introduction pipe 8a and the main discharge pipe 8b, and performed for each pipe as in the unit electrolytic cells of FIGS. It is more advantageous because there is no need.

【0012】図5〜図7は、本考案に係わる室枠を使用
して他の電解槽を組立た例を示す模式図であり、図5は
隔膜型単極式電解槽、図6は無隔膜型複極式電解槽、図
7は中間室を有する隔膜式単極式電解槽をそれぞれ示し
ている。図5の電解槽では図1の場合と異なり室枠11は
分割されず、該室枠11の周縁に穿設された孔(図示略)
に配管12が挿入されている。各室枠11は左側から室枠11
−陽極13−室枠11−イオン交換膜14−室枠11−陰極15−
室枠11−イオン交換膜14の順に積層され電解槽を構成し
ている。配管12から供給される電解液は隣接するイオン
交換膜14の間に形成される電極室内で電解されて所望の
電解生成物が提供される。
FIGS. 5 to 7 are schematic views showing examples of assembling another electrolytic cell using the chamber frame according to the present invention. FIG. 5 is a diaphragm type monopolar electrolytic cell, and FIG. FIG. 7 shows a diaphragm type monopolar electrolytic cell having an intermediate chamber. In the electrolytic cell of FIG. 5, unlike the case of FIG. 1, the chamber frame 11 is not divided, and a hole (not shown) formed in the periphery of the chamber frame 11
A pipe 12 is inserted into the pipe. Each room frame 11 is from the left.
-Anode 13-Chamber 11-Ion exchange membrane 14-Chamber 11-Cathode 15-
The chamber 11 and the ion exchange membrane 14 are laminated in this order to constitute an electrolytic cell. The electrolytic solution supplied from the pipe 12 is electrolyzed in an electrode chamber formed between the adjacent ion exchange membranes 14 to provide a desired electrolytic product.

【0013】図6の電解槽の室枠11は図5の室枠と同一
であり、左側から電極16−室枠11−電極16−室枠11−電
極16−室枠11の順に積層され電解槽を構成している。配
管12から供給される電解液例えば塩化ナトリウム水溶液
が電解されて次亜塩素酸ナトリウムが提供される。図7
の電解槽の室枠も図5及び図6の室枠と同一であり、左
側からイオン交換膜14−室枠11−電極16−室枠11−イオ
ン交換膜14−室枠11−イオン交換膜14−室枠11−電極16
−室枠11−イオン交換膜14−室枠11−イオン交換膜14−
室枠11の順に積層され電解槽を構成している。この電解
槽の場合にも従来の芒硝電解等の場合と同様に水酸化ナ
トリウム等の電解生成物が提供される。
The chamber frame 11 of the electrolytic cell shown in FIG. 6 is the same as the chamber frame shown in FIG. 5, and is laminated in the order of electrode 16, chamber frame 11, electrode 16, chamber frame 11, electrode 16 and chamber frame 11 from the left side. Make up the tank. An electrolytic solution, for example, an aqueous sodium chloride solution supplied from the pipe 12 is electrolyzed to provide sodium hypochlorite. FIG.
5 and 6 are the same as those in FIGS. 5 and 6, and from the left, the ion exchange membrane 14, the chamber frame 11, the electrode 16, the chamber frame 11, the ion exchange membrane 14, the chamber frame 11, and the ion exchange membrane. 14-chamber 11-electrode 16
-Chamber 11-ion exchange membrane 14-Chamber 11-ion exchange membrane 14-
The electrolytic cells are stacked in the order of the chamber frame 11. In the case of this electrolytic cell, an electrolytic product such as sodium hydroxide is provided as in the case of conventional Glauber's salt electrolysis.

【0014】図8は、本考案の室枠の密閉度試験に使用
した実験装置の概略図である。硬度50で厚さ2mm、外
寸100 mm、内寸80mmの額縁状の2枚のシリコンゴム
シート21の間に上下2本のポリテトラフルオロエチレン
製配管22(外径2mm、内径1mm)をその先端が前記
シート内縁から5mm突出する位置になるよう挟み込
み、両シート21を厚さ5mmの鉄板で挟み、10kg/c
2 の圧力で締め付けた。上側配管22から空気を送り込
み他方の配管から空気が排出されていることを確認した
後、下側の配管12を閉じシート21内の空気を3気圧にし
更に上側配管も閉じた。その後の圧力変化はなくシート
内の密閉性は十分保持されていることが確認された。
FIG. 8 is a schematic view of an experimental apparatus used in the test for sealing degree of the chamber frame of the present invention. Two upper and lower two polytetrafluoroethylene pipes 22 (outer diameter 2 mm, inner diameter 1 mm) are placed between two frame-shaped silicon rubber sheets 21 having a hardness of 50, a thickness of 2 mm, an outer dimension of 100 mm and an inner dimension of 80 mm. 10 mm / c, sandwiching both sheets 21 between 5 mm-thick iron plates so that the leading ends project 5 mm from the inner edge of the sheet.
It was tightened with a pressure of m 2 . After confirming that air was sent in from the upper pipe 22 and air was discharged from the other pipe, the lower pipe 12 was closed to make the air in the sheet 21 3 atm, and the upper pipe was closed. There was no subsequent pressure change, and it was confirmed that the airtightness in the sheet was sufficiently maintained.

【0015】[0015]

【考案の効果】本考案は、額縁状の室枠及び該室枠の周
縁を貫通し室枠構成材料より弾性率の大きい材料から成
る電解液導入配管及び電解液排出用配管を含んで成るこ
とを特徴とする電解である。このような構成から成る
本考案の電解槽では、従来の積層型電解槽のガスケット
を兼用するため部品数が減少しかつ極間距離及び室枠自
体の厚さを減少させ装置の小型化を達成することがで
き、配管及び室枠を弾性材料で構成しているため電解液
や発生ガスの漏洩もない。
The present invention comprises a frame-shaped chamber frame and an electrolyte introduction pipe and an electrolyte discharge pipe which penetrate the periphery of the chamber frame and are made of a material having a higher elastic modulus than the material constituting the chamber frame. An electrolytic cell characterized by the following. In the electrolytic cell of the present invention having such a configuration, the number of parts is reduced because the gasket of the conventional laminated electrolytic cell is also used, and the distance between the electrodes and the thickness of the chamber frame itself are reduced, thereby reducing the size of the apparatus. Since the piping and the chamber frame are made of an elastic material, there is no leakage of the electrolytic solution and generated gas.

【0016】又前記複数の配管をモジュール化しておく
と、個々の配管に電解液を供給しかつ個々の配管から電
解液を取り出す手間を省き単一の配管への供給及び配管
からの排出が可能になり、作業効率を向上させることが
できる。
Further, when the plurality of pipes are modularized, it is possible to supply the electrolyte to each pipe and to take out the electrolyte from each pipe, so that the supply to a single pipe and the discharge from the pipe are possible. And work efficiency can be improved.

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

【図1】本考案に係わる電解槽の実施例に係わる単位電
解槽の一例を示す斜視図。
FIG. 1 is a perspective view showing an example of a unit electrolytic cell according to an embodiment of the electrolytic cell according to the present invention.

【図2】図1のA−A線縦断面図。FIG. 2 is a vertical sectional view taken along line AA of FIG.

【図3】図1のB−B線横断面図。FIG. 3 is a transverse sectional view taken along line BB of FIG. 1;

【図4】本考案の電解槽の他の実施例に係わる単位電解
槽の正面図。
FIG. 4 is a front view of a unit electrolytic cell according to another embodiment of the electrolytic cell of the present invention.

【図5】本考案に係わる室枠を使用して隔膜型複極式電
解槽を組立た例を示す模式図。
FIG. 5 is a schematic view showing an example of assembling a diaphragm type bipolar electrolytic cell using the chamber frame according to the present invention.

【図6】本考案に係わる室枠を使用して無隔膜型単極式
電解槽を組立た例を示す模式図。
FIG. 6 is a schematic diagram showing an example of assembling a non-diaphragm type monopolar electrolytic cell using the chamber frame according to the present invention.

【図7】本考案に係わる室枠を使用して隔膜型単極式電
解槽を組立た例を示す模式図。
FIG. 7 is a schematic view showing an example of assembling a diaphragm type monopolar electrolytic cell using the chamber frame according to the present invention.

【図8】本考案の室枠の密閉度試験に使用した実験装置
の概略図。
FIG. 8 is a schematic diagram of an experimental apparatus used for a test of the degree of sealing of the chamber frame of the present invention.

【符号の説明】[Explanation of symbols]

1・・・単位電解槽 2・・・開口部 3・・・イオン
交換膜 4・・・室枠 4a・・・半割室枠 5・・・溝 6・・・段部 7・
・・電極構造体 8・・・配管 8a・・・主導入配管
8b・・・主排出配管 11・・・室枠 12・・・配管
13・・・陽極 14・・・イオン交換膜 15・・・陰極
16・・・電極 21・・・シリコンゴムシート 22・・・配管
DESCRIPTION OF SYMBOLS 1 ... Unit electrolytic cell 2 ... Opening 3 ... Ion exchange membrane 4 ... Chamber frame 4a ... Half-chamber frame 5 ... Groove 6 ... Step part 7.
..Electrode structure 8 ・ ・ ・ Piping 8a ・ ・ ・ Main introduction pipe 8b ・ ・ ・ Main discharge pipe 11 ・ ・ ・ Room frame 12 ・ ・ ・ Piping
13 ・ ・ ・ Anode 14 ・ ・ ・ Ion exchange membrane 15 ・ ・ ・ Cathode
16 ・ ・ ・ Electrode 21 ・ ・ ・ Silicon rubber sheet 22 ・ ・ ・ Piping

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C25B 1/00 - 15/08 H01M 2/02 H01M 2/36 106 H01M 8/02 ──────────────────────────────────────────────────続 き Continued on the front page (58) Fields surveyed (Int. Cl. 7 , DB name) C25B 1/00-15/08 H01M 2/02 H01M 2/36 106 H01M 8/02

Claims (2)

(57)【実用新案登録請求の範囲】(57) [Scope of request for utility model registration] 【請求項1】 額縁状の室枠及び該室枠の周縁を貫通し
室枠構成材料より弾性率の大きい材料から成る電解液導
入配管及び電解液排出用配管を含んで成ることを特徴と
する電解
1. A frame-shaped chamber frame and a penetrating edge of the chamber frame.
An electrolytic cell comprising: an electrolyte introduction pipe and an electrolyte discharge pipe made of a material having a higher elastic modulus than a chamber frame constituent material .
【請求項2】 配管がモジュール化されている請求項1
に記載の電解
2. The piping according to claim 1, wherein the piping is modularized.
The electrolytic cell according to 1 .
JP1993008014U 1993-02-04 1993-02-04 Electrolytic cell Expired - Fee Related JP2605708Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1993008014U JP2605708Y2 (en) 1993-02-04 1993-02-04 Electrolytic cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1993008014U JP2605708Y2 (en) 1993-02-04 1993-02-04 Electrolytic cell

Publications (2)

Publication Number Publication Date
JPH0661970U JPH0661970U (en) 1994-09-02
JP2605708Y2 true JP2605708Y2 (en) 2000-08-07

Family

ID=11681498

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1993008014U Expired - Fee Related JP2605708Y2 (en) 1993-02-04 1993-02-04 Electrolytic cell

Country Status (1)

Country Link
JP (1) JP2605708Y2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8808512B2 (en) * 2013-01-22 2014-08-19 GTA, Inc. Electrolyzer apparatus and method of making it
CN204999979U (en) * 2015-08-05 2016-01-27 林信涌 An electrolysis apparatus
JP6294991B1 (en) * 2017-04-14 2018-03-14 株式会社イープラン Bipolar electrolytic cell
EP4036277A4 (en) 2019-09-25 2022-12-07 De Nora Permelec Ltd Laminated structure including electrodes
KR102380793B1 (en) * 2021-08-25 2022-03-30 주식회사 네오에코 Pumping transfer type electrolyzer device with modular electrode fastening structure

Also Published As

Publication number Publication date
JPH0661970U (en) 1994-09-02

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