JPH055196A - Electrolytic cell and production thereof - Google Patents

Electrolytic cell and production thereof

Info

Publication number
JPH055196A
JPH055196A JP3154688A JP15468891A JPH055196A JP H055196 A JPH055196 A JP H055196A JP 3154688 A JP3154688 A JP 3154688A JP 15468891 A JP15468891 A JP 15468891A JP H055196 A JPH055196 A JP H055196A
Authority
JP
Japan
Prior art keywords
electrolytic cell
partition
partition wall
chamber
cathode
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP3154688A
Other languages
Japanese (ja)
Other versions
JP3082308B2 (en
Inventor
Shinji Katayama
真二 片山
Yoshinari Take
義成 竹
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.)
ThyssenKrupp Uhde Chlorine Engineers Japan Ltd
Original Assignee
Chlorine Engineers Corp 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 Chlorine Engineers Corp Ltd filed Critical Chlorine Engineers Corp Ltd
Priority to JP03154688A priority Critical patent/JP3082308B2/en
Priority to DE69213362T priority patent/DE69213362T2/en
Priority to EP92110670A priority patent/EP0521386B1/en
Priority to US07/904,251 priority patent/US5314591A/en
Publication of JPH055196A publication Critical patent/JPH055196A/en
Application granted granted Critical
Publication of JP3082308B2 publication Critical patent/JP3082308B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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

Abstract

PURPOSE:To obtain the electrolytic cell having excellent performance by providing a electrolyte dispersing and supplying chamber formed of members integral with partition walls in the upper part of an electrolytic cell unit. CONSTITUTION:Rugged parts 5, 6, 7, 8 fitting to each other are formed on the partition wall 2 on the anode side and partition wall 3 on the cathode side of the vertical type electrolytic cell unit 1. Electrode plates 9, 10 are coupled to the projecting parts 6, 8 of the partition wall plate integrated by superposing the two partition walls 2, 3 on each other. The electrolyte dispersing and separating chamber 11 formed of the members integral with the partition walls 2, 3 is provided in the lower part of the electrolytic cell unit 1. The outer surface of the electrolyte dispersing and supplying chamber 11 forms a flange surface for lamination of the electrolytic cell unit 1. The concn. distribution and temp. distribution of the electrolyte are uniformized in this way.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、フィルタープレス型の
電解槽に関し、特に隣接する電極室間の電解液を分離す
る隔壁に特徴を有する電解槽に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter press type electrolytic cell, and more particularly to an electrolytic cell having a partition wall for separating an electrolytic solution between adjacent electrode chambers.

【0002】[0002]

【従来の技術】フィルタープレス型電解槽は食塩の電気
分解による塩素と苛性ソーダの製造をはじめとして、有
機物の電解製造、海水の電解等に広く用いられている。
2. Description of the Related Art A filter press type electrolytic cell is widely used for production of chlorine and caustic soda by electrolysis of salt, electrolysis production of organic substances, electrolysis of seawater and the like.

【0003】フィルタープレス型電解槽を使用する代表
的な電解方法である食塩のフィルタープレス型の電解槽
には隣接する陽極室と陰極室とを隔壁を介して電気的お
よび機械的に結合した複極式電解槽ユニットを陽イオン
交換膜を介して多数積層し、両端には陽極あるいは陰極
のいずれかを片面に有する端部電極室ユニットを積層し
て油圧式のプレス等で固定した複極式フィルタープレス
型電解槽と、額縁状の電極室枠の両面に同一の電極を有
する陽極室ユニットおよび陰極室ユニットを陽イオン交
換膜を介して多数積層し、両端部には陽極または陰極を
片面に有する電極室ユニットを積層した単極式フィルタ
ープレス型電解槽がある。単極式の電解槽の電極室ユニ
ットは額縁状の電極室枠を補強するとともに電解液の循
環を促進する作用をするダウンカマーやリブ等を設けこ
れらのリブ等に電極を取り付けており、通常は電解液を
分離する隔壁は有していない。
A typical salt electrolysis method using a filter-press type electrolytic cell is a salt-type filter-press type electrolytic cell in which a plurality of adjacent anode and cathode chambers are electrically and mechanically connected via a partition wall. A multi-pole type in which a large number of polar electrolytic cell units are stacked with a cation exchange membrane, and end electrode chamber units with either an anode or a cathode on one side are stacked at both ends and fixed with a hydraulic press, etc. A filter press type electrolytic cell and a large number of anode chamber units and cathode chamber units having the same electrodes on both sides of a frame-shaped electrode chamber frame are laminated with a cation exchange membrane, and the anode or cathode is on one side at both ends. There is a single-pole filter press type electrolytic cell in which the electrode chamber units are stacked. The electrode chamber unit of a monopolar electrolytic cell is equipped with downcomers and ribs that reinforce the frame-shaped electrode chamber frame and promote the circulation of the electrolytic solution, and the electrodes are attached to these ribs. Does not have a partition for separating the electrolyte.

【0004】一方、複極式の電解槽のユニットには、陽
極室と陰極室とを分離するとともに電解電流の伝達の作
用をする隔壁が設けられている。陽極室と陰極室とを分
離する隔壁にはそれぞれ陽極および陰極が取り付けられ
ている。陽極室と陰極室は対象となる電解反応によっ
て、一方は酸化性の環境にあり他方が還元性の環境とな
る。とくに代表的なイオン交換膜を利用した電解方法で
ある食塩電解においては陽極では塩素が発生し、陰極で
は高濃度の水酸化ナトリウムと水素が生成するので、陽
極室には塩素などに耐食性の大きなチタン、タンタル、
ジルコニウムなどの薄膜形成性金属あるいはその合金を
使用している。また、陰極室の雰囲気ではチタンは水素
を吸収して脆化するので耐食性が大きなチタンも陰極室
には使用できない。このため、陰極室には鉄、ニッケ
ル、ステンレス等の鉄系の金属あるいはその合金を使用
している。各々の電極室を金属材料の隔壁で形成し両者
を接合することにより電気的接合を形成することができ
るが、陽極室側のチタンと陰極室側の鉄、ニッケル、ス
テンレスなどを直接に溶接によって接合しようとすると
チタンと陰極室側の鉄系の金属が金属間化合物を形成す
るために実用的な強度を有する接合体を得ることはでき
なかった。
On the other hand, the unit of the bipolar electrode type electrolytic cell is provided with a partition for separating the anode chamber and the cathode chamber and for transmitting the electrolytic current. An anode and a cathode are attached to the partition that separates the anode chamber and the cathode chamber, respectively. One of the anode chamber and the cathode chamber is in an oxidizing environment and the other is in a reducing environment depending on the target electrolytic reaction. Particularly, in salt electrolysis, which is an electrolysis method using a typical ion exchange membrane, chlorine is generated at the anode and high-concentration sodium hydroxide and hydrogen are generated at the cathode. Titanium, tantalum,
A thin film forming metal such as zirconium or its alloy is used. Further, in the atmosphere of the cathode chamber, titanium absorbs hydrogen and becomes brittle, so that titanium having a large corrosion resistance cannot be used in the cathode chamber. For this reason, iron-based metals such as iron, nickel and stainless steel or alloys thereof are used in the cathode chamber. Electrical connection can be formed by forming each electrode chamber with a partition wall made of a metal material and joining them together, but by directly welding titanium on the anode chamber side and iron, nickel, stainless steel, etc. on the cathode chamber side. When joining was attempted, a joined body having practical strength could not be obtained because titanium and the iron-based metal on the cathode chamber side formed an intermetallic compound.

【0005】そこで、複極式の電解槽では多くの提案が
行われている。例えば、特公昭53−5880号公報に
は合成樹脂材料の隔壁を貫通するボルトで陽極室側の部
材と陰極室側の部材とを結合することを記載している。
Therefore, many proposals have been made for a bipolar electrode type electrolytic cell. For example, Japanese Patent Publication No. 53-5880 describes that a member on the anode chamber side and a member on the cathode chamber side are connected by a bolt penetrating a partition wall made of a synthetic resin material.

【0006】また、特公昭52−32866号公報では
鉄系の金属とチタンとを爆着により接合した板状体を隔
壁とし、各々の面にリブを溶接し、リブに陽極および陰
極を溶接している。特公昭56−36231号公報には
チタンと鉄を銅を挟んで三者を接合した複合材料を使用
し、複合材料のチタンと複極式電解槽ユニットの陽極側
隔壁のチタンとを溶接し、同様に該複合材料の鉄と陰極
側の鉄系の金属の隔壁とを溶接によって結合している。
Further, in Japanese Patent Publication No. 52-32866, a plate-shaped body in which an iron-based metal and titanium are joined by explosive welding is used as partition walls, ribs are welded to each surface, and an anode and a cathode are welded to the ribs. ing. In Japanese Examined Patent Publication No. 56-36231, a composite material is used in which titanium and iron are sandwiched between copper and three members are joined, and titanium of the composite material and titanium of the partition wall on the anode side of the bipolar electrode unit are welded, Similarly, the iron of the composite material and the iron-based metal partition wall on the cathode side are joined by welding.

【0007】[0007]

【発明が解決しようとする課題】複極式電解槽の隔壁に
は各種のものがあるが、いずれの電解槽においてもリブ
を隔壁に結合し、リブに電極を溶接などの方法によって
取り付けることが行われているが、リブによる電圧の降
下が避けられない。また、陰極側の金属と陽極側の金属
とを接合するためには特殊な方法を用いる必要があっ
た。
Although there are various types of partition walls of a bipolar electrode electrolytic cell, in any electrolytic cell, ribs can be joined to the partition walls and electrodes can be attached to the ribs by a method such as welding. However, the voltage drop due to the rib is unavoidable. Further, it is necessary to use a special method for joining the metal on the cathode side and the metal on the anode side.

【0008】このような問題を解決するために、互いに
嵌合する凹凸を形成した隔壁板をプレス加工によって製
造し、凸部に電極を接合した電解槽ユニットを有する構
造および製造方法が簡単な複極式電解槽を特願平2−4
5855号として提案した。食塩のイオン交換膜法によ
る電気分解のように、電極面積が大きな電解槽において
は、電極室内での電流分布が不均一化すると、電極の部
分的な消耗が進んだり、イオン交換膜が部分的に劣化す
る等の電解槽の性能に好ましくない現象が起こるので、
陽極−隔壁−陰極−陽極という電流の流れる通路がほぼ
等しくなるように電極と集電部材との取り付け位置を工
夫し、電極室内での電流分布が均一とすることが行われ
ている。
In order to solve such a problem, a partition plate having concave and convex portions to be fitted to each other is manufactured by press working, and a structure having an electrolytic cell unit in which an electrode is bonded to the convex portion and a manufacturing method are simple. Japanese Patent Application No. 2-4
Proposed as No. 5855. In an electrolytic cell with a large electrode area, such as electrolysis of salt by the ion-exchange membrane method, if the current distribution in the electrode chamber becomes uneven, partial wear of the electrode will proceed or the ion-exchange membrane will partially As it causes unfavorable phenomena such as deterioration of the electrolytic cell performance,
It has been attempted to make the current distribution in the electrode chamber uniform by devising the attachment positions of the electrode and the current collecting member so that the current passages of the anode-partition wall-cathode-anode are almost equal.

【0009】また、電解槽を電流分布が均一となる構造
とするとともに、電極室内での電解液の濃度や温度の分
布を小さくすることが行われている。電解液の濃度や温
度の分布を小さくするためには、電極室内へ外部から供
給され、外部へ取り出される電解液の循環速度あるいは
循環量を大きくすることが行われているが、循環量を多
くするためには大型の循環装置を必要とするとともに、
電解液の濃度あるいは温度の均一化という面では必ずし
も十分な効果が得られない。
Further, it has been attempted that the electrolytic cell has a structure in which the current distribution is uniform and the concentration and temperature distribution of the electrolytic solution in the electrode chamber are reduced. In order to reduce the concentration and temperature distribution of the electrolytic solution, it has been attempted to increase the circulation rate or the circulation rate of the electrolytic solution that is supplied from the outside into the electrode chamber and taken out to the outside. To do so requires a large circulation device,
In terms of making the concentration or temperature of the electrolytic solution uniform, a sufficient effect cannot always be obtained.

【0010】また、電解液の濃度あるいは温度を均一化
するために、電解液を均一に電極室に供給することも効
果がある方法であるが、平板をプレス成形した電解槽ユ
ニットにおいては電解液を分散する手段を設けることは
行われていない。
It is also an effective method to uniformly supply the electrolytic solution to the electrode chamber in order to make the concentration or temperature of the electrolytic solution uniform, but in the electrolytic cell unit in which a flat plate is press-molded, the electrolytic solution is No means is provided to disperse.

【0011】また、図6には、平板をプレス成形した電
解槽ユニットの下部の断面図を示すが、電解槽ユニット
31の下部には電解槽枠体32が設けられており、電極
室33を形成する隔壁34が電解槽枠体に取り付けられ
ている。また、電極35が隔壁に結合されている。この
ように電極室の下部は、剛体からなる電解槽枠体32で
構成されているので、電解液を均一に分散する手段を設
けることは構造上困難である。
FIG. 6 shows a sectional view of the lower portion of the electrolytic cell unit obtained by press-molding a flat plate. An electrolytic cell frame 32 is provided below the electrolytic cell unit 31, and an electrode chamber 33 is provided. The partition wall 34 to be formed is attached to the electrolytic cell frame. Further, the electrode 35 is connected to the partition. As described above, since the lower part of the electrode chamber is constituted by the electrolytic cell frame body 32 made of a rigid body, it is structurally difficult to provide a means for uniformly dispersing the electrolytic solution.

【0012】[0012]

【課題を解決するための手段】本発明は、竪型の電解槽
ユニットの陽極側の隔壁と陰極側の隔壁に互いに嵌合す
る凹凸を形成し、両隔壁を重ね併せて一体化した隔壁板
の凸部に電極板を結合した電解槽において、隔壁の下部
を折り曲げて、隔壁と一体の部材からなり、電解液の均
一に高速に電極室内へ供給する断面積が小さい通路を均
一に配置した電解液分散供給室を形成するものであり、
更に電解液分散供給室の外側は電解槽ユニットを積層す
る際に隣接する電解槽との間のフランジ面としたもので
ある。
DISCLOSURE OF THE INVENTION According to the present invention, a partition plate is formed by forming recesses and projections which are fitted to the partition wall on the anode side and the partition wall on the cathode side of a vertical type electrolytic cell unit, and both partition walls are superposed and integrated. In the electrolytic cell in which the electrode plate is connected to the convex portion of the partition wall, the lower part of the partition wall is bent, and a passage having a small cross-sectional area which is made of a member integrated with the partition wall and supplies the electrolyte solution into the electrode chamber uniformly and at high speed is arranged uniformly. To form the electrolyte dispersion supply chamber,
Further, the outside of the electrolytic solution dispersion supply chamber is a flange surface between adjacent electrolytic cells when the electrolytic cell units are stacked.

【0013】[0013]

【作用】竪型の電解槽ユニットの陽極側の隔壁と陰極側
の隔壁に互いに嵌合する凹凸を形成し、両隔壁を重ね併
せて一体化した隔壁板の凸部に電極板を結合した電解槽
において、陽極側の隔壁および陰極側の隔壁の下部を成
形加工して、隔壁と一体の電解液分散供給室を形成した
電解槽であり、製造方法が簡単であるとともに電解液の
供給が均一に行われるので、電解液の濃度分布および温
度分布が均一化されるので高い電解性能が得られる。
Operation: Electrolysis in which an electrode plate is connected to the protrusion of a partition plate in which the partition wall on the anode side and the partition wall on the cathode side of the vertical electrolytic cell unit are formed to fit with each other, and both partition walls are superposed and integrated. This is an electrolytic cell in which the lower part of the partition wall on the anode side and the lower part of the partition wall on the cathode side are molded to form an electrolytic solution dispersion supply chamber integrated with the partition wall.The manufacturing method is simple and the supply of the electrolytic solution is uniform. Therefore, since the concentration distribution and temperature distribution of the electrolytic solution are made uniform, high electrolytic performance can be obtained.

【0014】[0014]

【実施例】以下に図面を参照して本発明を説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to the drawings.

【0015】図1(A)は、本発明の電解槽の1実施例
を示す一部を切り欠いた陽極側からみた平面図を示し、
図1(B)は図1をA−A線で切断した断面図を示し、
図2は図1(A)でB−B線で示すように切断した縦方
向の下部の断面を示す断面図である。
FIG. 1A is a plan view showing one embodiment of the electrolytic cell of the present invention as seen from the partially cut-away anode side,
FIG. 1B shows a cross-sectional view taken along the line AA of FIG.
FIG. 2 is a cross-sectional view showing a cross section of a lower portion in the vertical direction cut along the line BB in FIG.

【0016】電解槽ユニット1の陽極側の隔壁2はチタ
ン、ジルコニウム、タンタルなどの薄膜形成性金属およ
びそれらの合金から選ばれる薄板を鍋状に成形加工し、
陰極側の隔壁3は鉄、ニッケル、ステンレス等の薄板を
同様に加工したものである。そして、それぞれの隔壁は
電解槽枠体4に取り付けられている。両隔壁には、互い
に嵌合する凹凸部を形成しており、陽極側の隔壁には溝
状の凹部5と凸部6を設けており、陰極側の隔壁にも陽
極側の凹凸と嵌合する位置に同様に溝状の凹部7と凸部
8を設けている。
The partition wall 2 on the anode side of the electrolytic cell unit 1 is formed by laminating a thin plate selected from thin film forming metals such as titanium, zirconium and tantalum and alloys thereof into a pot shape.
The partition wall 3 on the cathode side is a thin plate of iron, nickel, stainless steel or the like processed in the same manner. Each partition wall is attached to the electrolytic cell frame body 4. Both the partition walls are formed with concave and convex portions that fit with each other, and the partition walls on the anode side are provided with groove-shaped concave portions 5 and convex portions 6, and the partition walls on the cathode side are also fitted with the concave and convex portions on the anode side. Similarly, groove-shaped concave portions 7 and convex portions 8 are provided at the positions.

【0017】それぞれの電極室内部において、電解液の
循環路が形成されるように電極室の上下および左右の壁
面に隣接する部分には凹凸部は設けないようにすること
が好ましい。また、陽極側の隔壁の凸部には、エキスパ
ンデッド金属、多孔性板等に白金族の金属の酸化物等か
らなる陽極活性被覆を形成した陽極9が溶接等によって
設けられており、陰極側の隔壁の凸部には、エキスパン
デッド金属、多孔性板等にニッケル系、白金族の金属系
の物質からなる陰極活性被覆を形成した陰極10が溶接
等によって結合されている。
In each of the electrode chambers, it is preferable that no concavo-convex portion is provided in the portions adjacent to the upper, lower, left and right wall surfaces of the electrode chamber so that a circulation path for the electrolytic solution is formed. Further, an anode 9 in which an anode active coating made of an oxide of a platinum group metal is formed on an expanded metal, a porous plate or the like is provided on the convex portion of the partition wall on the anode side by welding or the like. A cathode 10 in which a cathode active coating made of a nickel-based material or a platinum-based metal-based material is formed on an expanded metal, a porous plate, or the like is joined to the convex portion of the side partition wall by welding or the like.

【0018】電解槽ユニットの下部には電極室内へ均一
に電解液を供給する電解液分散供給室11を形成してい
る。電解液分散供給室は電解槽の枠体4を包み込みよう
にして垂直に伸びた隔壁を水平な直線に沿って電極の取
付面側に直角に折り曲げ、更に電解液分散供給室の外面
が電解槽のフランジ12を形成するように電極室の厚み
に相当する長さで直角に折り曲げる。そして隔壁の先端
部13を電極と部分的に結合して電極を固定する。
An electrolytic solution dispersion supply chamber 11 for uniformly supplying the electrolytic solution into the electrode chamber is formed below the electrolytic cell unit. In the electrolyte dispersion supply chamber, a partition wall extending vertically so as to enclose the frame body 4 of the electrolysis tank is bent at a right angle to the electrode mounting surface side along a horizontal straight line, and the outer surface of the electrolyte dispersion supply chamber is an electrolytic tank. It is bent at a right angle with a length corresponding to the thickness of the electrode chamber so as to form the flange 12. Then, the tip portion 13 of the partition wall is partially coupled to the electrode to fix the electrode.

【0019】電解液分散供給室と電極室の間には電解液
を高速で電極室内へ供給できるように、電解液分散供給
室と電極室の間に断面積の小さい通路14を設ける。
A passage 14 having a small cross-sectional area is provided between the electrolytic solution dispersion supply chamber and the electrode chamber so that the electrolytic solution can be rapidly supplied into the electrode chamber between the electrolytic solution dispersion supply chamber and the electrode chamber.

【0020】図3には、電解液分散供給室部分の一部を
切り欠いた斜視図を示すが、隔壁を成形して通路14を
設けるとともに、電解槽ユニットのフランジ12の裏側
に接合して電解槽ユニットとしての機械的な強度を保持
する接合面15を設ける。また、隔壁には電解槽の枠体
を取り付ける凹所16を形成している。
FIG. 3 is a perspective view in which a part of the electrolytic solution dispersion supply chamber is cut away. A partition wall is formed to provide a passage 14 and is joined to the back side of the flange 12 of the electrolytic cell unit. A joint surface 15 is provided that maintains the mechanical strength of the electrolytic cell unit. Further, the partition wall is provided with a recess 16 for mounting the frame body of the electrolytic cell.

【0021】陽極側及び陰極側の隔壁に設ける凹凸部は
通常のプレス機によって1枚ずつ形成するが、陽極側と
陰極側の隔壁を同一の形状とすることができるので陽極
側、陰極側に同一のプレス用の金型を準備するのみで良
い。また、陽極側の隔壁と陰極側の隔壁のそれぞれの材
料を1枚ずつ積層した状態でプレスすることによって両
隔壁に凹凸を形成すると同時に両隔壁を一体化すること
ができるので、製造工程を単純化することが可能であ
る。
The uneven portions provided on the partition walls on the anode side and the cathode side are formed one by one by an ordinary press machine. However, since the partition walls on the anode side and the cathode side can have the same shape, they are formed on the anode side and the cathode side. All that is required is to prepare the same press mold. Also, by pressing the materials of the partition walls on the anode side and the partition walls on the cathode side one by one, it is possible to form concavities and convexities on both partition walls and at the same time to integrate both partition walls, which simplifies the manufacturing process. Is possible.

【0022】陽極側の隔壁と陰極側の隔壁は、直接にス
ポット溶接で接合しても良いし、陰極側の隔壁と陽極側
の隔壁の間に導電性グリースを介在させて溶接等の恒久
的な接続手段によらずとも、凹凸部分を嵌合させて電気
的及び機械的な接合を形成することもできる。
The partition wall on the anode side and the partition wall on the cathode side may be directly joined by spot welding, or a conductive grease may be interposed between the partition wall on the cathode side and the partition wall on the anode side for permanent welding. It is also possible to form an electrical and mechanical joint by fitting the concave and convex portions without using any connecting means.

【0023】また、電解槽ユニットを積層して電解槽を
組み立て電極室内を加圧し、両隔壁と外部との間に圧力
差を形成して陽極側の隔壁と陰極側の隔壁の接触性を高
めたり、両隔壁と電極室枠体とで形成される空間を気密
にし、この空間を減圧して電極室内との間で圧力差を形
成して両隔壁の接触性を高めても良い。
Further, the electrolytic cell unit is laminated to assemble the electrolytic cell to pressurize the inside of the electrode chamber to form a pressure difference between the both partition walls and the outside to enhance the contact between the partition wall on the anode side and the partition wall on the cathode side. Alternatively, the space formed by both partition walls and the electrode chamber frame may be made airtight, and this space may be decompressed to form a pressure difference between the space inside the electrode chamber and the contact property between both partition walls.

【0024】また、図4(A)には、一部を切り欠いた
電解槽の平面図を示し、図4(B)にはC−C線での断
面図を示すが、図1および図2に示すような溝状の凹凸
に代えて椀状の凹凸21を形成しても良い。
Further, FIG. 4 (A) shows a plan view of an electrolytic cell with a part cut away, and FIG. 4 (B) shows a cross-sectional view taken along the line C--C. Instead of the groove-shaped unevenness as shown in 2, a bowl-shaped unevenness 21 may be formed.

【0025】また、図5には電解槽ユニットを積層して
電解槽を組み立てる場合の隣接する電解槽ユニットの断
面を示すが、一方の極性の凸部は同一直線状に配置し、
隣接する電解槽ユニット間ではイオン交換膜22を介し
て凸部と凹部が向かい合うように配置して電流の分布を
均一化することが好ましい。
FIG. 5 shows a cross section of adjacent electrolytic cell units when the electrolytic cell units are stacked to assemble the electrolytic cell. The convex portions of one polarity are arranged in the same straight line,
It is preferable that the adjacent electrolytic cell units are arranged such that the convex portions and the concave portions face each other via the ion exchange membrane 22 to make the current distribution uniform.

【0026】[0026]

【発明の結果】電解槽の隔壁用の薄板をプレス加工して
電極室とフランジ面を形成した電解槽ユニットにおい
て、電極室ユニットの下部に電解槽に供給される電解液
を均一に電極室内へ分散して供給する電解液分散供給室
を隔壁と一体の薄板をプレス加工することによって形成
したので、簡単な製造方法で電解性能の優れた電解槽を
得ることができる。
As a result, in the electrolytic cell unit in which the thin plate for the partition wall of the electrolytic cell is pressed to form the electrode chamber and the flange surface, the electrolytic solution supplied to the electrolytic cell is uniformly introduced into the electrode chamber under the electrode chamber unit. Since the electrolytic solution dispersion supply chamber to be dispersed and supplied is formed by pressing the thin plate integrated with the partition wall, an electrolytic cell having excellent electrolytic performance can be obtained by a simple manufacturing method.

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

【図1】本発明の1実施例を示す電解槽の平面図および
断面図である。
FIG. 1 is a plan view and a sectional view of an electrolytic cell showing an embodiment of the present invention.

【図2】図1でB−B線で示すように縦方向の断面の上
部を示す図である。
FIG. 2 is a diagram showing an upper portion of a vertical cross section as indicated by a line BB in FIG.

【図3】電解液分散供給室の一部を切り欠いた斜視図で
ある。
FIG. 3 is a perspective view in which a part of an electrolyte solution supply chamber is cut away.

【図4】本発明の他の実施例を示す電解槽の平面図およ
び断面図である。
FIG. 4 is a plan view and a sectional view of an electrolytic cell showing another embodiment of the present invention.

【図5】本発明の電解槽ユニットを積層した断面図であ
る。
FIG. 5 is a cross-sectional view in which the electrolytic cell units of the present invention are stacked.

【図6】平板をプレス成形した従来の電解槽ユニットの
下部の断面図である。
FIG. 6 is a sectional view of a lower portion of a conventional electrolytic cell unit in which a flat plate is press-molded.

【符号の説明】[Explanation of symbols]

1…電解槽ユニット、2…陽極側の隔壁、3…陰極側の
隔壁、4…電解槽枠体、5…凹部(陽極側)、6…凸部
(陽極側)、7…凹部(陰極側)、8…凸部(陰極
側)、9…陽極、10…陰極、11…電解液分散供給
室、12…フランジ、13…先端部、14…通路、15
…接合面、16…凹所、21…椀状の凹凸、22…イオ
ン交換膜、31…電解槽ユニット、32…電解槽枠体、
33…電極室、34…隔壁、35…電極
DESCRIPTION OF SYMBOLS 1 ... Electrolytic cell unit, 2 ... Anode side partition, 3 ... Cathode side partition, 4 ... Electrolyte cell frame, 5 ... Recessed part (anode side), 6 ... Convex part (anode side), 7 ... Recessed part (cathode side) ), 8 ... Convex part (cathode side), 9 ... Anode, 10 ... Cathode, 11 ... Electrolyte dispersion supply chamber, 12 ... Flange, 13 ... Tip part, 14 ... Passage, 15
... Joining surface, 16 ... Recess, 21 ... Bowl-shaped unevenness, 22 ... Ion exchange membrane, 31 ... Electrolytic cell unit, 32 ... Electrolytic cell frame,
33 ... Electrode chamber, 34 ... Partition wall, 35 ... Electrode

Claims (1)

【特許請求の範囲】 【請求項1】 竪型の電解槽ユニットの陽極側の隔壁と
陰極側の隔壁に互いに嵌合する凹凸を形成し、両隔壁を
重ね併せて一体化した隔壁板の凸部に電極板を結合した
電解槽において、電解槽ユニットの下部には隔壁と一体
の部材で形成された電解液分散供給室を有することを特
徴とする電解槽。 【請求項2】 電解液分散供給室の外側の面が電解槽ユ
ニットの積層用のフランジ面を形成することを特徴とす
る請求項1記載の電解槽。 【請求項3】 電解槽ユニットの陽極側の隔壁と陰極側
の隔壁に互いに嵌合する凹凸を形成し、両隔壁を重ね併
せて一体化した隔壁板を有する電解槽を製造する方法に
おいて、それぞれの隔壁の下部を折り曲げて隔壁板と一
体の部材で電解液分散供給室を形成したことを特徴とす
る電解槽の製造方法。
Claim: What is claimed is: 1. A projection of a partition plate, in which projections and recesses are formed on the anode-side partition and the cathode-side partition of a vertical electrolytic cell unit so as to fit with each other, and both partitions are superposed and integrated. An electrolyzer in which an electrode plate is coupled to a portion, wherein an electrolytic solution dispersion supply chamber formed of a member integrated with a partition is provided in a lower portion of the electrolyzer unit. 2. The electrolytic cell according to claim 1, wherein an outer surface of the electrolytic solution dispersion supply chamber forms a flange surface for laminating the electrolytic cell unit. 3. A method for producing an electrolytic cell having a partition plate in which projections and recesses are formed on the anode-side partition and the cathode-side partition of the electrolytic cell unit so as to be fitted to each other, and both partition walls are superposed and integrated. The method of manufacturing an electrolytic cell, wherein the lower part of the partition wall is bent to form the electrolytic solution dispersion supply chamber by a member integrated with the partition plate.
JP03154688A 1991-06-26 1991-06-26 Electrolytic cell and method for producing the same Expired - Lifetime JP3082308B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP03154688A JP3082308B2 (en) 1991-06-26 1991-06-26 Electrolytic cell and method for producing the same
DE69213362T DE69213362T2 (en) 1991-06-26 1992-06-25 Electrolyser and manufacture thereof
EP92110670A EP0521386B1 (en) 1991-06-26 1992-06-25 Electrolyzer and its production
US07/904,251 US5314591A (en) 1991-06-26 1992-06-25 Electrolyzer and method of production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03154688A JP3082308B2 (en) 1991-06-26 1991-06-26 Electrolytic cell and method for producing the same

Publications (2)

Publication Number Publication Date
JPH055196A true JPH055196A (en) 1993-01-14
JP3082308B2 JP3082308B2 (en) 2000-08-28

Family

ID=15589758

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03154688A Expired - Lifetime JP3082308B2 (en) 1991-06-26 1991-06-26 Electrolytic cell and method for producing the same

Country Status (1)

Country Link
JP (1) JP3082308B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100729281B1 (en) * 2005-10-21 2007-06-15 중앙아이엔티 주식회사 an electrode for electrolyzer
WO2024117732A1 (en) * 2022-11-28 2024-06-06 주식회사 엘지화학 Electrolysis device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100729281B1 (en) * 2005-10-21 2007-06-15 중앙아이엔티 주식회사 an electrode for electrolyzer
WO2024117732A1 (en) * 2022-11-28 2024-06-06 주식회사 엘지화학 Electrolysis device

Also Published As

Publication number Publication date
JP3082308B2 (en) 2000-08-28

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