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JPS6240438B2 - - Google Patents
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JPS6240438B2 - - Google Patents

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Publication number
JPS6240438B2
JPS6240438B2 JP54086397A JP8639779A JPS6240438B2 JP S6240438 B2 JPS6240438 B2 JP S6240438B2 JP 54086397 A JP54086397 A JP 54086397A JP 8639779 A JP8639779 A JP 8639779A JP S6240438 B2 JPS6240438 B2 JP S6240438B2
Authority
JP
Japan
Prior art keywords
electrolytic cell
jumper switch
circuit
electrolytic
anode
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
JP54086397A
Other languages
Japanese (ja)
Other versions
JPS5613489A (en
Inventor
Eiji Itoi
Hiroshi Kimura
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.)
AGC Inc
Original Assignee
Asahi Glass 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 Asahi Glass Co Ltd filed Critical Asahi Glass Co Ltd
Priority to JP8639779A priority Critical patent/JPS5613489A/en
Publication of JPS5613489A publication Critical patent/JPS5613489A/en
Publication of JPS6240438B2 publication Critical patent/JPS6240438B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/34Simultaneous production of alkali metal hydroxides and chlorine, oxyacids or salts of chlorine, e.g. by chlor-alkali electrolysis
    • C25B1/46Simultaneous production of alkali metal hydroxides and chlorine, oxyacids or salts of chlorine, e.g. by chlor-alkali electrolysis in diaphragm cells

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  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明はイオン交換膜法電解装置の電解槽の運
転を停止するときの電気回路に関する。 更に詳しくは、陽イオン交換膜法電解装置の電
解槽を移動式ジヤンパースイツチを用いて停止す
る際、ジヤンパースイツチ回路の電圧降下をある
値以上に保つことにより、電解槽の陽極寿命を長
くするための電解槽停止時の電気回路に関する。 従来、塩化アルカリ金属塩水溶液の電解方法に
は、水銀法と隔膜法とが有り、近年においては、
更にイオン交換膜を隔膜として用いるイオン交換
膜法が開発され実用化されるに至つている。 我国においては、水銀による環境汚染の防止と
いう観点から、水銀法から非水銀法へ転換するこ
とを政府の指導のもとに実施されつつある。 非水銀法による電解方法は、アスベストを主体
とする隔膜法と陽イオン交換膜を用いるイオン交
換膜法とに大別される。電気的に多数直列に接続
されている隔膜法電解槽のある一つの電解槽の運
転を停止するとき、停止する電解槽に移動式ジヤ
ンパースイツチを並列に接続して、ジヤンパース
イツチを閉とし、電解槽に流れていた電解電流を
全部ジヤンパースイツチ回路に流して、電解槽の
運転を停止する。電解槽停止後も塩化アルカリ金
属塩水溶液を電解槽に供給して陰極室の苛性アル
カリと供給塩化アルカリ金属塩水溶液と置換して
苛性アルカリが陽極室に逆流して陽極(金属陽
極)の苛性アルカリによる劣化を防止している。
また、電気的に多数直列に接続されている水銀法
電解のある一つの電解槽の運転を停止するとき、
停止する電解槽に装着されている電解槽短絡スイ
ツチを閉とし電解槽に流れている電解電流を全部
短絡スイツチ回路に流して、電解槽の運転を停止
する。電解槽の電解電流を停止後も塩水アルカリ
金属塩水溶液を供給し、及び/又は水銀の循環を
継続して、水銀アマルガムを解汞塔で解汞して水
銀金属を電解槽に循環することにより、陽極(金
属陽極)の苛性アルカリによる劣化を防止してい
る。 一方、近年開発実用化されたイオン交換膜電解
槽においても、特にモノポーラー型イオン交換膜
電解槽において、電気的に多数直列に接続されて
いる電解槽群の中の一つの電解槽の運転を停止す
るとき、停止する電解槽に移動式ジヤンパースイ
ツチを当該電解槽に並列に接続して、ジヤンパー
スイツチを閉とし、当該電解槽に流れている電解
電流を全部ジヤンパースイツチ回路に流して、当
該電解槽の運転を停止する。当該電解槽には電解
電流が流れなくなつてからも塩化アルカリ金属塩
水溶液を供給し続けて、拡散によりイオン交換膜
を通過して陰極室から陽極室に移動してくる苛性
アルカリによる陽極(金属陽極)の劣化を防止し
ている。 しかし、本発明者等は電気的に多数直列に接続
されている陽イオン交換膜法電解槽群の中の一つ
の電解槽の運転を停止するとき、停止する電解槽
に移動式ジヤンパースイツチを当該電解槽に並列
に接続して、ジヤンパースイツチを閉とし、当該
電解槽に流れている電解電流を全部ジヤンパース
イツチ回路に流して、当該電解槽の運転を停止し
たとき、当該電解槽からジヤンパースイツチ回路
を通して大きなループ電流が流れていることを発
見した。 本発明者等は、この現象の原因を解明するため
に鋭意検討をした結果、運転中の陽イオン交換膜
法電解槽の電解電流を短絡スイツチを用いずに電
解電流の給電を停止すると陽極と陰極との間に陽
極がプラスとなるような起電力が発生しているこ
とまた再起動時の陽極ガス中の酸素の発生が多く
なつていることを発見した。起電力の大きさは電
解槽の液温度、陰極液濃度(苛性アルカリ金属濃
度)によつて異なるが、一槽当たり0.7V〜2.4V
に達する。この起動力が発生する原因については
明らかでないが、金属陽極のコーテイング材の還
元又は陰極金属材料の溶出等によるものと考えら
れる。 一方、陽極及び/又は陰極に付着しているガス
が溶解放電していることによることも考えられ
る。 移動式ジヤンパースイツチ回路の電圧降下は一
般に0.3V〜0.6V程度であるので、電解槽の起動
力が0.7V〜2.4Vあればジヤンパースイツチ回路
を通して電流が流れることは明白であり、起電力
の発生原因が陽極コーテイング材の還元及び/又
は陰極材の溶出に起因していると充分に考えられ
るので、この状態を長時間継続すれば、陽極及
び/又は陰極寿命が短縮される。 本発明者等は、このようなループ電流を防止す
る方法を検討した結果、電気的に多数直列に接続
されている陽イオン交換膜法電解槽群の中の一つ
の電解槽の運転を停止するとき、移動式ジヤンパ
ースイツチと直列に抵抗をジヤンパースイツチ回
路に挿入して、ジヤンパースイツチ回路の電圧降
下を0.7V以上、更に好ましくは2.4V以上にする
ことにより、停止電解槽の起電力によるループ電
流を防止することができることを見出した。 本発明を更に詳しく理解するために、添付図に
より説明する。 第1図は、従来の電解槽の電気的接続方法を示
す図であり、1−1,1−2,……,1−nは電
気的にブスバー6により、直列に接続されている
イオン交換膜法電解槽であり、整流器2からブス
バー4,5を通して電解電流が給電されて運転さ
れている。これ等の電解槽群の中の1つの電解
槽、例えば1−2の運転を停止するとき、移動式
ジヤンパースイツチ3を電解槽1−2と並列にジ
ヤンパースイツチのリードブスバー7及び8を電
解槽間ブスバー6にボルトで接続し、ジヤンパー
スイツチを閉とすることにより電解電流をジヤン
パースイツチに全部流して電解槽1−2の運転を
停止する。このとき、電解槽1−2に起電力が発
生して、その大きさがジヤンパースイツチ回路の
電圧降下より大きいときには、起電力による電流
が電解槽1−2→ブスバー7→ジヤンパースイツ
チ3→ブスバー8→電解槽1−2の閉ループ回路
を流れることになり、電解槽1−2の陽極及び/
又は陰極の劣化の原因になつていると考えられ
る。 第2図、第3図は、本発明の電解槽の電気的接
続方法を示す図であり、第2図はジヤンパースイ
ツチ回路に直列に抵抗9を挿入して、ジヤンパー
スイツチ回路の電圧降下を電解槽1−2の起電力
より大きくして、電解槽1−2の起電力による電
流を防止する電解槽の停止方法である。抵抗9は
ジヤンパースイツチと直列に別個に設けてもよ
く、または、ジヤンパースイツチのリードブスバ
ー7,8自身の抵抗を大きくしても良い。 第2図の電解槽停止方法では、電解電流がジヤ
ンパースイツチ回路に全部流れているので、電解
槽停止中挿入抵抗9による電力損失が大きく不経
済的である。 第3図は、第2図のジヤンパースイツチによる
電槽停止方式では電力損失が大きいので、ジヤン
パースイツチ回路の抵抗9に並列に更にもう一つ
のジヤンパースイツチ11を設けて、電解槽1−
2と電解槽間ブスバー6との電気的接続を外した
後にジヤンパースイツチ11を閉として電解電流
の流れを電解槽1−1→ブスバー6→ブスバー7
→抵抗9→ブスバー10→ジヤンパースイツチ3
→ブスバー8→ブスバー6→電解槽1−3(記載
なし)から電解槽1−1→ブスバー6→ブスバー
7→ブスバー12→ジヤンパースイツチ11→ブ
スバー13→ブスバー10→ジヤンパースイツチ
3→ブスバー8→ブスバー6→電解槽1−3(記
載なし)に変えることにより、抵抗9による電力
損失を小さくすることができる。 実施例 1 5cm×5cmの小型電解槽を用いて、陽極にはチ
タンに酸化ルテニウムをコーテイングした陽極を
用い、陰極にはステンレスを用いて、陽極室と陰
極室との間にはイオン交換基がカルボン酸型であ
る弗素系陽イオン交換膜を使用した電解槽を下記
の条件で運転を行い、運転を停止したときの起電
力を表1に示した。 運転条件 電流密度:20A/dm2 供給塩水濃度(食塩):310g/ 電解槽温度:90℃ 苛性アルカリ濃度(NaOH):40%
The present invention relates to an electric circuit for stopping operation of an electrolytic cell of an ion-exchange membrane electrolyzer. More specifically, when stopping the electrolytic cell of a cation exchange membrane electrolyzer using a mobile jumper switch, the life of the anode of the electrolytic cell can be extended by keeping the voltage drop in the jumper switch circuit above a certain value. This relates to an electric circuit when the electrolytic cell is stopped. Conventionally, there are two methods for electrolyzing an aqueous alkali metal chloride solution: the mercury method and the diaphragm method.
Furthermore, an ion exchange membrane method using an ion exchange membrane as a diaphragm has been developed and put into practical use. In Japan, from the perspective of preventing environmental pollution caused by mercury, a shift from mercury laws to mercury-free laws is being implemented under the guidance of the government. Non-mercury electrolysis methods are broadly divided into diaphragm methods, which mainly use asbestos, and ion exchange membrane methods, which use cation exchange membranes. When stopping the operation of one electrolytic cell that has many diaphragm electrolytic cells electrically connected in series, connect a mobile jumper switch in parallel to the electrolytic cell to be stopped and close the jumper switch. , all the electrolytic current flowing in the electrolytic cell is passed through the jumper switch circuit, and the operation of the electrolytic cell is stopped. Even after the electrolytic cell is stopped, an aqueous alkali metal chloride salt solution is supplied to the electrolytic cell to replace the caustic alkali in the cathode chamber with the supplied aqueous alkali metal chloride solution, and the caustic alkali flows back into the anode chamber and replaces the caustic alkali in the anode (metal anode). This prevents deterioration due to
Also, when stopping the operation of one electrolytic cell with mercury method electrolysis that is electrically connected in series,
The electrolytic cell short-circuit switch attached to the electrolytic cell to be stopped is closed, and all the electrolytic current flowing in the electrolytic cell is passed through the short-circuit switch circuit, thereby stopping the operation of the electrolytic cell. By supplying the salt water alkali metal salt aqueous solution and/or continuing the circulation of mercury even after stopping the electrolytic current in the electrolytic cell, the mercury amalgam is decomposed in the decomposition tower, and the mercury metal is circulated to the electrolytic cell. , prevents deterioration of the anode (metal anode) due to caustic alkali. On the other hand, even in ion-exchange membrane electrolyzers that have been developed and put into practical use in recent years, especially in monopolar ion-exchange membrane electrolyzers, it is difficult to operate one electrolyzer in a group of electrolyzers that are electrically connected in series. When stopping, a mobile jumper switch is connected in parallel to the electrolytic tank to be stopped, the jumper switch is closed, and all the electrolytic current flowing in the electrolytic tank is passed through the jumper switch circuit. , stop the operation of the electrolytic cell. The aqueous alkali metal chloride solution is continued to be supplied to the electrolytic cell even after the electrolytic current stops flowing, and the anode (metallic This prevents deterioration of the anode). However, when stopping the operation of one electrolytic cell in a group of cation-exchange membrane electrolytic cells electrically connected in series, the inventors installed a mobile jumper switch on the electrolytic cell to be stopped. When the electrolytic cell is connected in parallel with the electrolytic cell, the jumper switch is closed, and all the electrolytic current flowing in the electrolytic cell is passed through the jumper switch circuit, and the operation of the electrolytic cell is stopped, the voltage from the electrolytic cell is It was discovered that a large loop current flows through the jumper switch circuit. As a result of intensive studies to elucidate the cause of this phenomenon, the present inventors found that if the electrolytic current of the cation-exchange membrane electrolytic cell in operation is stopped without using a short-circuit switch, the anode It was discovered that an electromotive force was generated between the cathode and the anode so that the anode became positive, and that more oxygen was generated in the anode gas during restart. The magnitude of the electromotive force varies depending on the electrolytic tank liquid temperature and catholyte concentration (caustic alkali metal concentration), but is 0.7V to 2.4V per tank.
reach. The cause of this starting force is not clear, but it is thought to be due to reduction of the coating material of the metal anode or elution of the cathode metal material. On the other hand, it is also possible that the gas adhering to the anode and/or cathode is dissolving and discharging. Since the voltage drop in a mobile jumper switch circuit is generally about 0.3V to 0.6V, it is obvious that if the starting force of the electrolytic cell is 0.7V to 2.4V, a current will flow through the jumper switch circuit, and the electromotive force will be It is fully believed that the cause of this is due to the reduction of the anode coating material and/or the elution of the cathode material, so if this state continues for a long time, the life of the anode and/or cathode will be shortened. As a result of studying methods to prevent such loop currents, the present inventors decided to stop the operation of one electrolytic cell in a group of cation exchange membrane electrolytic cells electrically connected in series. By inserting a resistor into the jumper switch circuit in series with the mobile jumper switch to make the voltage drop in the jumper switch circuit 0.7V or more, more preferably 2.4V or more, the electromotive force of the stopped electrolytic cell can be reduced. It has been found that loop current caused by this can be prevented. For a more detailed understanding of the invention, reference is made to the accompanying drawings. FIG. 1 is a diagram showing the electrical connection method of a conventional electrolytic cell, where 1-1, 1-2, ..., 1-n are electrically connected in series by a bus bar 6. This is a membrane method electrolytic cell, and is operated by being supplied with electrolytic current from a rectifier 2 through bus bars 4 and 5. When stopping the operation of one electrolytic cell, for example 1-2, in these electrolytic cell groups, the mobile jumper switch 3 is connected in parallel with the electrolytic cell 1-2, and the lead busbars 7 and 8 of the jumper switch are connected. By connecting to the inter-electrolytic cell bus bar 6 with a bolt and closing the jumper switch, the entire electrolytic current flows through the jumper switch and the operation of the electrolytic cell 1-2 is stopped. At this time, when an electromotive force is generated in the electrolytic cell 1-2 and its magnitude is larger than the voltage drop of the jumper switch circuit, the current due to the electromotive force is transferred from the electrolytic cell 1-2 → bus bar 7 → jumper switch 3 → It will flow through a closed loop circuit from bus bar 8 to electrolytic cell 1-2, and the anode and/or
Or, it is thought that it is a cause of deterioration of the cathode. 2 and 3 are diagrams showing the electrical connection method of the electrolytic cell of the present invention. In FIG. 2, a resistor 9 is inserted in series with the jumper switch circuit to reduce the voltage drop of the jumper switch circuit. This is a method of stopping an electrolytic cell in which the electromotive force of the electrolytic cell 1-2 is made larger than the electromotive force of the electrolytic cell 1-2 to prevent a current from flowing due to the electromotive force of the electrolytic cell 1-2. The resistor 9 may be provided separately in series with the jumper switch, or the resistance of the lead busbars 7, 8 of the jumper switch itself may be increased. In the method of stopping the electrolytic cell shown in FIG. 2, all of the electrolytic current flows through the jumper switch circuit, so that the power loss caused by the insertion resistor 9 while the electrolytic cell is stopped is large and uneconomical. In FIG. 3, since power loss is large in the electrolytic cell stop method using the jumper switch shown in FIG.
After disconnecting the electrical connection between the electrolytic cell bus bar 6 and the electrolytic cell bus bar 6, the jumper switch 11 is closed and the flow of electrolytic current is changed from the electrolytic cell 1-1 to the bus bar 6 to the bus bar 7.
→ Resistor 9 → Busbar 10 → Jumper switch 3
→ Busbar 8 → Busbar 6 → Electrolytic cell 1-3 (not described) to Electrolytic cell 1-1 → Busbar 6 → Busbar 7 → Busbar 12 → Jumper switch 11 → Busbar 13 → Busbar 10 → Jumper switch 3 → Busbar 8 By changing → bus bar 6 → electrolytic cell 1-3 (not shown), power loss due to resistor 9 can be reduced. Example 1 A small electrolytic cell measuring 5 cm x 5 cm was used, the anode was made of titanium coated with ruthenium oxide, the cathode was made of stainless steel, and an ion exchange group was placed between the anode chamber and the cathode chamber. An electrolytic cell using a carboxylic acid type fluorine-based cation exchange membrane was operated under the following conditions, and the electromotive force when the operation was stopped is shown in Table 1. Operating conditions Current density: 20A/dm 2 Supply brine concentration (salt): 310g/ Electrolyzer temperature: 90℃ Caustic alkali concentration (NaOH): 40%

【表】 実施例 2 実施例1と同じ電解槽を用いて、運転停止後陽
極室の塩水を供給塩水で置換したときの電解槽の
起電力を表2に示す。
[Table] Example 2 Using the same electrolytic cell as in Example 1, Table 2 shows the electromotive force of the electrolytic cell when the salt water in the anode chamber was replaced with the supplied salt water after the operation was stopped.

【表】 実施例 3 実施例1において、電解槽温度75℃で起電力が
1.5Vのとき、第1図のような短絡回路を作り、
短絡スイツチを閉としたとき短絡回路に流れた電
流は表3の通りであつた。また、再起動時に陽極
液のPHが極端に低下した。
[Table] Example 3 In Example 1, the electromotive force was
When the voltage is 1.5V, create a short circuit as shown in Figure 1,
The current flowing through the short circuit when the short circuit switch was closed was as shown in Table 3. Additionally, the pH of the anolyte dropped dramatically upon restart.

【表】 実施例 4 実施例2において、電解槽温度70℃で起電力が
1.5Vのとき、第1図のような短絡回路を作り、
短絡スイツチを閉としたとき、短絡回路に流れた
電流は表4の通りであつた。また、再起動時に陽
極液のPHが極端に低下した。
[Table] Example 4 In Example 2, the electromotive force was
When the voltage is 1.5V, create a short circuit as shown in Figure 1,
When the short circuit switch was closed, the current flowing through the short circuit was as shown in Table 4. Additionally, the pH of the anolyte dropped dramatically upon restart.

【表】 以上のように、短絡回路側の電圧降下が小さい
と、電解槽の起電力の大小によつて電解槽へは大
小の逆電流が流れ、逆電流が大きいほど陽極コー
テイング材に与える影響が大きいことが分つた。 実施例 5 実施例3において、第2図に示す電気的結線方
法で電解槽の停止を行つた。短絡回路に挿入する
抵抗は約0.14Ωで、短絡回路の電圧降下は約0.7V
であつた。この時の短絡回路に流れた電流は表5
の通りであつた。また、再起動時の陽極液のPHは
停止前とほとんど変化がなかつた。
[Table] As shown above, when the voltage drop on the short circuit side is small, a reverse current of varying magnitude will flow into the electrolytic tank depending on the electromotive force of the electrolytic tank, and the larger the reverse current, the more it will affect the anode coating material. It turns out that there is a large amount. Example 5 In Example 3, the electrolytic cell was stopped using the electrical connection method shown in FIG. The resistance inserted into the short circuit is approximately 0.14Ω, and the voltage drop in the short circuit is approximately 0.7V.
It was hot. The current flowing through the short circuit at this time is shown in Table 5.
It was hot on the street. Furthermore, the pH of the anolyte upon restart was almost unchanged from before the shutdown.

【表】 以上の如く、本発明の方法により、短絡電流を
大きく減少することが可能になつた。
[Table] As described above, the method of the present invention has made it possible to significantly reduce short circuit current.

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

第1図は、従来の電解槽の電気的接続図であ
る。第2図は、本発明の電解槽の電気的接続図で
ある。第3図は、本発明の他の電解槽の電気的接
続図である。
FIG. 1 is an electrical connection diagram of a conventional electrolytic cell. FIG. 2 is an electrical connection diagram of the electrolytic cell of the present invention. FIG. 3 is an electrical connection diagram of another electrolytic cell of the present invention.

Claims (1)

【特許請求の範囲】 1 陽イオン交換膜で陽極室と陰極室とに区分さ
れた電解槽を移動式ジヤンパースイツチを用いて
停止するとき、ジヤンパースイツチ回路に抵抗を
挿入して当該ジヤンパースイツチ回路の電圧降下
が0.7V以上とすることを特徴とする電解槽停止
時の電気回路。 2 ジヤンパースイツチ回路に挿入した抵抗を短
絡するもう一つのジヤンパースイツチを抵抗に並
列に設けることを特徴とする第1項記載の電解槽
停止時の電気回路。 3 ジヤンパースイツチ回路に挿入した抵抗がジ
ヤンパースイツチ回路の電気導電体自身の抵抗で
あることを特徴とする第1項記載の電解槽停止時
の電気回路。
[Claims] 1. When stopping an electrolytic cell divided into an anode chamber and a cathode chamber by a cation exchange membrane using a mobile jumper switch, a resistor is inserted into the jumper switch circuit to shut down the jumper. An electric circuit when the electrolyzer is stopped, characterized in that the voltage drop in the switch circuit is 0.7V or more. 2. The electric circuit when the electrolytic cell is stopped according to item 1, characterized in that another jumper switch is provided in parallel with the resistor to short-circuit the resistor inserted in the jumper switch circuit. 3. The electric circuit when the electrolytic cell is stopped according to item 1, wherein the resistance inserted in the jumper switch circuit is the resistance of the electric conductor itself of the jumper switch circuit.
JP8639779A 1979-07-10 1979-07-10 Electric circuit at stop time of electrolytic bath Granted JPS5613489A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8639779A JPS5613489A (en) 1979-07-10 1979-07-10 Electric circuit at stop time of electrolytic bath

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8639779A JPS5613489A (en) 1979-07-10 1979-07-10 Electric circuit at stop time of electrolytic bath

Publications (2)

Publication Number Publication Date
JPS5613489A JPS5613489A (en) 1981-02-09
JPS6240438B2 true JPS6240438B2 (en) 1987-08-28

Family

ID=13885734

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8639779A Granted JPS5613489A (en) 1979-07-10 1979-07-10 Electric circuit at stop time of electrolytic bath

Country Status (1)

Country Link
JP (1) JPS5613489A (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5794586A (en) * 1980-12-03 1982-06-12 Chlorine Eng Corp Ltd Method for stopping conduction of electricity of electrolytic cell
JPS58169103U (en) * 1982-05-10 1983-11-11 東京濾器株式会社 Oil filter device with bypass filter for internal combustion engines
GB2202164B (en) * 1987-02-20 1991-04-03 Sartorius Gmbh Testing fluid filter apparatus
US5079236A (en) * 1987-05-27 1992-01-07 Hyal Pharmaceutical Corporation Pure, sterile, pyrogen-free hyaluronic acid formulations their methods of preparation and methods of use
US5078877A (en) * 1989-09-25 1992-01-07 Baldwin Filters, Inc. Dual flow and dual stage lubricant filter assembly
DE102022204924A1 (en) * 2022-05-18 2023-11-23 Siemens Energy Global GmbH & Co. KG Electrolysis system, method for operating an electrolysis system and system network comprising an electrolysis system and a wind turbine

Also Published As

Publication number Publication date
JPS5613489A (en) 1981-02-09

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