JPH025824B2 - - Google Patents

Info

Publication number
JPH025824B2
JPH025824B2 JP57007088A JP708882A JPH025824B2 JP H025824 B2 JPH025824 B2 JP H025824B2 JP 57007088 A JP57007088 A JP 57007088A JP 708882 A JP708882 A JP 708882A JP H025824 B2 JPH025824 B2 JP H025824B2
Authority
JP
Japan
Prior art keywords
cathode
electrolytic cell
plate
conductive
exchange membrane
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
Application number
JP57007088A
Other languages
Japanese (ja)
Other versions
JPS58123883A (en
Inventor
Takao Ebina
Keigo Morya
Kenji Okada
Toshihiko Kuroda
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.)
Kanto Denka Kogyo Co Ltd
Original Assignee
Kanto Denka Kogyo Co 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 Kanto Denka Kogyo Co Ltd filed Critical Kanto Denka Kogyo Co Ltd
Priority to JP57007088A priority Critical patent/JPS58123883A/en
Publication of JPS58123883A publication Critical patent/JPS58123883A/en
Publication of JPH025824B2 publication Critical patent/JPH025824B2/ja
Granted legal-status Critical Current

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  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Electrodes For Compound Or Non-Metal Manufacture (AREA)

Description

【発明の詳細な説明】 本発明は塩化アルカリ電解槽の改造方法に関す
るものである。さらに詳しくは隔膜法単極式堅型
電解槽を改造しイオン交換膜法電解槽とする方法
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for modifying an alkaline chloride electrolytic cell. More specifically, the present invention relates to a method of modifying a diaphragm method monopolar type rigid electrolytic cell to make it into an ion exchange membrane method electrolytic cell.

塩化アルカリの電解、特に食塩水の電解による
苛性ソーダの製造法には水銀法、隔膜法及びイオ
ン交換膜法の3法がある。水銀法は得られる苛性
ソーダの濃度が高く、また食塩の含量も少ないこ
とから一時期我が国において全盛を誇つたが、現
在は環境汚染の問題から全面廃止の運命にあり、
それに代るものとして隔膜法への転換が急速に進
んだ。しかしこの隔膜法においては得られる電解
液が希薄なため濃縮として約50%の苛性ソーダに
しなければならない上に食塩が通常1%程度含ま
れており、この苛性ソーダを使用する需要家の製
品または装置材料に悪影響を及ぼす原因になる。
これらの欠点を改良したものとして近年脚光を浴
びているのがイオン交換膜法であり、アスベスト
等の隔膜に代えて陽イオン交換膜樹脂膜を陰陽両
極間に設置し、高純度の苛性ソーダを高濃度で得
る方法である。
There are three methods for producing caustic soda by electrolysis of alkali chloride, especially salt water: the mercury method, the diaphragm method, and the ion exchange membrane method. The mercury method was at its peak in Japan for a time because it produced a high concentration of caustic soda and a low salt content, but it is now destined to be completely abolished due to environmental pollution issues.
As an alternative, the conversion to the diaphragm method rapidly progressed. However, in this diaphragm method, the electrolyte obtained is dilute, so it must be concentrated to about 50% caustic soda, and it usually contains about 1% salt. It may cause an adverse effect on.
The ion-exchange membrane method has been attracting attention in recent years as a method that improves these shortcomings.In place of a diaphragm made of asbestos, a cation-exchange membrane is installed between the negative and anode electrodes, and high-purity caustic soda is This is a method of obtaining concentration.

従つて品質の良い苛性ソーダを得るためにはイ
オン交換膜法を採用するのが現状では最良の方法
であるが、既に隔膜法電解槽を設置している場合
には、全面的に転換をするには大きな負担にな
る。そのため一方では隔膜法で得られた苛性ソー
ダを精製し、品位を向上させる工夫がなされてお
り、また一方では既設の隔膜電解槽をイオン交換
膜電解槽へと改造する検討がなされている。本発
明はその隔膜法電解槽をイオン交換膜電解槽に改
造する方法に係るものである。
Therefore, currently the best way to obtain high-quality caustic soda is to use the ion exchange membrane method, but if you have already installed a diaphragm method electrolyzer, it is not recommended to completely switch over. becomes a big burden. Therefore, on the one hand, efforts are being made to refine and improve the quality of caustic soda obtained by the diaphragm method, and on the other hand, studies are being made to modify existing diaphragm electrolytic cells into ion-exchange membrane electrolytic cells. The present invention relates to a method for converting the diaphragm method electrolytic cell into an ion exchange membrane electrolytic cell.

隔膜法電解槽をイオン交換膜電解槽に転換する
例としては特開昭53−10399号公報に開示されて
いる方法が挙げられる。本方法は隔膜を陽イオン
交換膜に取替え電解液及びガス流路を変更するこ
とによりイオン交換膜電解槽として使用するもの
で何等手を加えずにイオン交換膜法電解槽として
使用できる利点を有する反面極間距離については
何等配慮はなされず、効率化の面では何等工夫が
なされていない(隔膜と陽イオン交換膜ではその
厚さが異なる)と云う欠点を有している。
An example of converting a diaphragm electrolytic cell into an ion exchange membrane electrolytic cell is the method disclosed in Japanese Patent Application Laid-Open No. 10399/1983. This method is used as an ion exchange membrane electrolytic cell by replacing the diaphragm with a cation exchange membrane and changing the electrolyte and gas flow paths, and has the advantage that it can be used as an ion exchange membrane electrolytic cell without any modification. On the other hand, it has the disadvantage that no consideration is given to the distance between the electrodes, and no efforts have been made in terms of efficiency (the diaphragm and the cation exchange membrane have different thicknesses).

本発明者らは上記欠点を解消し、しかも改造費
用も少なく合理的な塩化アルカリ電解槽の改造方
法を見い出すべく鋭意研究の結果本発明に到達し
た。即ち、本発明は、単極式隔膜電解槽であつて
陰極は扁平管状をなし、各陰極管はその内部で複
数個の電導板と電気的に接続し該電導板は該扁平
陰極管を貫通し、その両端部は陰極槽ブスバー接
続壁である両槽壁に直接接続し、各扁平陰極管の
両端は隣り合う陰極管同志を陰極槽と同質の電導
性物質で連結し共通の陰極室を形成させ、陽極は
電解槽底部で支持している形式の電解槽(具体的
には特公昭49−27749号公報記載の電解槽を挙げ
ることができる。)をイオン交換膜法電解槽に改
造するに当り 陽極を袋状陽イオン交換膜で包み、各々の陽
極室を複数形成し 各扁平管状陰極を個々に分離しさらに管状と
なつている上端部及び下端部等を切断すること
により2枚の板状陰極とし 該電導板を切りはなし、その平面が板状陰極
平面と平行になるように向きを変えて再配置し 該電導板と板状陰極の間に弾性を有する導電
性物質を挿入し、該弾性を有する導電性物質と
陰極活性面とを溶接することにより電導板と板
状陰極を電気的に接続すると同時に極間距離の
調節を行なうことを特徴とする塩化アルカリ電
解槽の改造方法を提供するものである。
The inventors of the present invention have arrived at the present invention as a result of extensive research to find a reasonable method for modifying an alkali chloride electrolytic cell that eliminates the above-mentioned drawbacks and also requires low modification costs. That is, the present invention provides a monopolar diaphragm electrolytic cell in which the cathode has a flat tube shape, and each cathode tube is electrically connected to a plurality of conductive plates inside the cell, and the conductive plates penetrate through the flat cathode tube. Both ends of the tubes are directly connected to both tank walls, which are cathode tank busbar connection walls, and both ends of each flat cathode tube connect adjacent cathode tubes with the same conductive material as the cathode tank to form a common cathode chamber. An electrolytic cell in which the anode is formed and the anode is supported at the bottom of the electrolytic cell (specifically, the electrolytic cell described in Japanese Patent Publication No. 49-27749 can be mentioned) is modified into an ion-exchange membrane method electrolytic cell. To do this, the anode is wrapped in a bag-shaped cation exchange membrane, each forming a plurality of anode chambers, each flat tubular cathode is separated individually, and the tubular upper and lower ends are cut to form two sheets. A plate-shaped cathode is obtained by cutting out the conductive plate, changing its orientation so that its plane is parallel to the plane of the plate-shaped cathode, and inserting an elastic conductive substance between the plate-shaped cathode and the plate-shaped cathode. A method for remodeling an alkali chloride electrolytic cell, which comprises electrically connecting a conductive plate and a plate-shaped cathode and simultaneously adjusting the distance between the electrodes by welding the elastic conductive substance and the cathode active surface. It provides:

従来、極間調節は陽極で行なわれているのが普
通であるが、陽極にはチタン等高価な金属が用い
られている上に支持棒とバネの接続部での電気抵
抗が大きく電圧ロスが大きい上に加工が困難であ
るという欠点がある。一方本発明においては通常
軟鋼が用いられている陰極を加工するのであるか
ら溶接、組立等が簡単である上に電気抵抗が少な
いので操業時の電圧ロスが少なく、大幅な電圧降
下が得られると云う利点を有している。
Conventionally, pole spacing adjustment has normally been performed using an anode, but the anode is made of expensive metal such as titanium, and the electrical resistance at the connection between the support rod and the spring is large, resulting in voltage loss. It has the disadvantages of being large and difficult to process. On the other hand, in the present invention, since the cathode, which is usually made of mild steel, is processed, welding and assembly are simple, and the electric resistance is low, so there is little voltage loss during operation, and a large voltage drop can be obtained. It has the advantage of

以下に本発明の典型的な実施例について図面を
用いて説明する。第1図は改造前の隔膜法電解槽
の一例であり、垂直方向の断面図を示している。
第2図はそのA部分からの水平方向断面図を示し
ている。図において1は陰極であり通常網状構造
をしている。この表面に褐膜3がデポジツト或い
は被覆されている。陰極は電導板4と数点で電気
的に接続されている。2は陽極を示す。第3図は
第2図と同部分の本発明方法による改造後のイオ
ン交換膜電解槽の例を示している。即ち陰極1を
第1図のa部分及び第2図のb部分から切りはな
すことにより陰極を二枚の板とし、一方陽極2は
袋状の陽イオン交換膜3′で包み、袋状陽イオン
交換膜の口の部分は上部に来る、一個あるいは並
列にならぶ複数個の陽極が包み込まれた各個の陽
極室を構成させる。尚、陽イオン交換膜は通常塩
化アルカリに使用されるものであればいずれでも
良い。電導板4は改造前の設置状態のままでも良
いが図示する様に90゜回転させてその平面が板状
陰極平面と平行になるように向きを変えて再配置
し槽体と接続させる方が極間調節が容易になるの
で好ましい。そして陰極1と電導板4との間に弾
性を有する導電性物質5を挿入して極間を調節
し、陰極を陽極に接近させる。即ち陽極を陽イオ
ン交換膜で包み込む形式の電解槽においては陰極
により極間距離が調節され得るので槽全体の組立
が容易になると云う利点もある。尚、弾性を有す
る導電性物質は材質的には特に限定はないが電導
板と同じ材質であることが好ましい。また形状に
ついては特に限定はなく図示したカマボコ状であ
つてもバネ状であつても本発明の効果を挙げるこ
とができるが、電気抵抗を考慮してその形状を決
定すべきである。
Typical embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows an example of a diaphragm electrolytic cell before remodeling, and shows a vertical cross-sectional view.
FIG. 2 shows a horizontal sectional view from part A thereof. In the figure, 1 is a cathode, which usually has a network structure. A brown film 3 is deposited or coated on this surface. The cathode is electrically connected to the conductive plate 4 at several points. 2 indicates an anode. FIG. 3 shows an example of an ion exchange membrane electrolytic cell after modification by the method of the present invention in the same part as FIG. 2. That is, the cathode 1 is cut out from the section a in FIG. 1 and the section b in FIG. The mouth part of the exchange membrane is located at the upper part and forms an individual anode chamber in which one or a plurality of anodes arranged in parallel are enclosed. The cation exchange membrane may be any membrane normally used for alkali chloride. The conductive plate 4 may be left in its installed state before modification, but it is better to rotate it 90 degrees as shown in the figure, change its orientation so that its plane is parallel to the plane of the plate cathode, and connect it to the tank body. This is preferable because the electrode spacing can be easily adjusted. Then, an elastic conductive material 5 is inserted between the cathode 1 and the conductive plate 4 to adjust the distance between the electrodes and bring the cathode closer to the anode. That is, in an electrolytic cell in which the anode is surrounded by a cation exchange membrane, the distance between the electrodes can be adjusted by the cathode, which has the advantage that the entire cell can be assembled easily. The elastic conductive substance is not particularly limited in terms of material, but is preferably the same material as the conductive plate. Further, the shape is not particularly limited, and the effects of the present invention can be obtained even if the shape is a semicylindrical shape or a spring shape as shown in the drawings, however, the shape should be determined in consideration of electrical resistance.

陽イオン交換膜の固定は電解槽上部に支持枠を
設けることにより行なうが、その形式については
特に限定はなく、例えば第4図及び第5図に示す
様な支持枠を槽体と槽蓋との間に介在させること
により行なうことができる。第4図は支持枠の部
分平面図、第5図はそのB部分での部分断面図で
ある。図中、10は空間部であり、11はイオン
交換膜を介在させて陽極ガスを導くキヤツプをは
め込む部分であり(第6図参照)、上方に向いて
やや開いた形状になつている。また12は電解槽
槽体の側壁に乗る部分である。
The cation exchange membrane is fixed by providing a support frame on the top of the electrolytic cell, but there are no particular limitations on the format. This can be done by interposing it between the two. FIG. 4 is a partial plan view of the support frame, and FIG. 5 is a partial sectional view at section B thereof. In the figure, numeral 10 is a space, and numeral 11 is a part into which a cap for guiding anode gas with an ion exchange membrane interposed (see Fig. 6) is slightly opened upward. Further, 12 is a part that rides on the side wall of the electrolytic cell body.

上記構成の支持枠6及びキヤツプ7により第6
図に示す如く陽イオン交換膜3′を固定し、陰極
室を構成させる。尚、この上に槽蓋をかぶせる。
これらは5の弾性を有する導電性物質をも含め、
総て一例として挙げたものであり、本発明を限定
的に示したものではない。
The support frame 6 and cap 7 configured as described above provide a sixth
As shown in the figure, a cation exchange membrane 3' is fixed to form a cathode chamber. In addition, cover this with a tank lid.
These include conductive substances with an elasticity of 5,
All of these examples are given as examples, and do not limit the present invention.

以上の通り本発明に従えば比較的に安価に、し
かもあまり手を加えることなく隔膜法電解槽をイ
オン交換膜法電解槽に改造することが可能であ
り、本改造電解槽を用いることにより効率良く塩
化アルカリ水溶性の電解を行なうことができ、し
かも高品位の水酸化アルカリ水溶液を得ることが
できる。
As described above, according to the present invention, it is possible to modify a diaphragm method electrolytic cell into an ion exchange membrane method electrolytic cell relatively inexpensively and without much modification, and by using this modified electrolytic cell, efficiency can be improved. Electrolysis of aqueous alkali chloride can be carried out well, and a high-quality aqueous alkali hydroxide solution can be obtained.

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

第1図は改造前の隔膜法電解槽垂直方向の部分
断面図、第2図はそのA部分での水平方向部分断
面図、第3図は本発明方法による改造後の電解槽
水平方向部分断面図、第4図は支持枠の部分平面
図、第5図はそのB部分での部分断面図、第6図
は本発明方法による改造後の電解槽垂直方向部分
断面図である。 1…陰極、2…陽極、3…隔膜、3′…陽イオ
ン交換膜、4…電導板、5…弾性を有す導電性物
質、6…支持枠、7…キヤツプ。
Fig. 1 is a vertical partial cross-sectional view of the diaphragm method electrolytic cell before modification, Fig. 2 is a horizontal partial cross-sectional view at part A, and Fig. 3 is a horizontal partial cross-section of the electrolytic cell after modification by the method of the present invention. 4 is a partial plan view of the support frame, FIG. 5 is a partial cross-sectional view at part B thereof, and FIG. 6 is a vertical partial cross-sectional view of the electrolytic cell after modification by the method of the present invention. DESCRIPTION OF SYMBOLS 1... Cathode, 2... Anode, 3... Diaphragm, 3'... Cation exchange membrane, 4... Conductive plate, 5... Elastic conductive material, 6... Support frame, 7... Cap.

Claims (1)

【特許請求の範囲】 1 単極式隔膜電解槽であつて、陰極は扁平管状
をなし各陰極管はその内部で複数個の電導板と電
気的に接続し、該電導板は該扁平陰極管を貫通
し、その両端部は陰極槽ブスバー接続壁である両
槽壁に直接接続し、各陰極管の両端は隣合う陰極
管同志を同質の電導性物質で連結して陰極室を形
成させ、陽極は電解槽底部で支持している形式の
ものをイオン交換膜法電解槽に改造するに当り、 陽極を袋状陽イオン交換膜で包み、各々の陽
極室を複数形成し 各扁平管状陰極を個々に分離し、さらに管状
となつている上端部及び下端部等を切断するこ
とにより2枚の板状陰極とし 該電導板を切りはなし、その平面が板状陰極
平面と平行になるように向きを変えて再配置
し、 該電導板と板状陰極の間に弾性を有する電導
性物質を挿入し、該弾性を有する電導性物質と
陰極活性面とを溶接することにより電導板と板
状陰極を電気的に接続すると同時に極間距離の
調節を行なうことを特徴とする塩化アルカリ電
解槽の改造方法。 2 電解槽の上部に陽イオン交換膜支持枠を設け
る特許請求の範囲第1項記載の方法。
[Scope of Claims] 1. A monopolar diaphragm electrolytic cell, wherein the cathode has a flat tube shape, and each cathode tube is electrically connected to a plurality of conductive plates inside the cathode tube, and the conductive plates are connected to the flat cathode tubes. The two ends of each cathode tube are directly connected to the two tank walls, which are the cathode tank busbar connection walls, and the two ends of each cathode tube connect adjacent cathode tubes with the same conductive material to form a cathode chamber. When converting an electrolytic cell in which the anode is supported at the bottom of the electrolytic cell to an ion-exchange membrane electrolytic cell, the anode is wrapped in a bag-shaped cation-exchange membrane, each forming a plurality of anode chambers, and each flat tubular cathode Separate the conductive plates individually, and then cut the upper and lower ends of the tubular shape to obtain two plate-shaped cathodes. Cut the conductive plate and orient it so that its plane is parallel to the plane of the plate-shaped cathode. By changing the conductive plate and rearranging the conductive plate, inserting an elastic conductive material between the conductive plate and the plate-shaped cathode, and welding the elastic conductive substance and the cathode active surface, the conductive plate and the plate-shaped cathode are A method for modifying an alkaline chloride electrolytic cell, which comprises electrically connecting the electrodes and adjusting the distance between the electrodes at the same time. 2. The method according to claim 1, wherein a cation exchange membrane support frame is provided above the electrolytic cell.
JP57007088A 1982-01-20 1982-01-20 Method for reconstructing alkali chloride electrolytic cell and cell therefor Granted JPS58123883A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57007088A JPS58123883A (en) 1982-01-20 1982-01-20 Method for reconstructing alkali chloride electrolytic cell and cell therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57007088A JPS58123883A (en) 1982-01-20 1982-01-20 Method for reconstructing alkali chloride electrolytic cell and cell therefor

Publications (2)

Publication Number Publication Date
JPS58123883A JPS58123883A (en) 1983-07-23
JPH025824B2 true JPH025824B2 (en) 1990-02-06

Family

ID=11656324

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57007088A Granted JPS58123883A (en) 1982-01-20 1982-01-20 Method for reconstructing alkali chloride electrolytic cell and cell therefor

Country Status (1)

Country Link
JP (1) JPS58123883A (en)

Also Published As

Publication number Publication date
JPS58123883A (en) 1983-07-23

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