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JPH0425351B2 - - Google Patents
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JPH0425351B2 - - Google Patents

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Publication number
JPH0425351B2
JPH0425351B2 JP59188236A JP18823684A JPH0425351B2 JP H0425351 B2 JPH0425351 B2 JP H0425351B2 JP 59188236 A JP59188236 A JP 59188236A JP 18823684 A JP18823684 A JP 18823684A JP H0425351 B2 JPH0425351 B2 JP H0425351B2
Authority
JP
Japan
Prior art keywords
hydrogen
hydrogen separator
electrolytic cell
caustic soda
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
JP59188236A
Other languages
Japanese (ja)
Other versions
JPS6167781A (en
Inventor
Masataka Takamura
Toshiro Oonishi
Tadayuki Myama
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP59188236A priority Critical patent/JPS6167781A/en
Publication of JPS6167781A publication Critical patent/JPS6167781A/en
Publication of JPH0425351B2 publication Critical patent/JPH0425351B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Prevention Of Electric Corrosion (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)

Description

【発明の詳細な説明】 本発明は、イオン交換膜式食塩電解槽の水素分
離器の電蝕防止法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for preventing galvanic corrosion of a hydrogen separator in an ion exchange membrane salt electrolyzer.

従来から食塩電解法としては、水銀電解法が得
られるカセイソーダ水溶液の純度および濃度が高
くできることから行なわれていたが、水銀公害問
題から隔膜式またはイオン交換膜式電解法に変更
されている。中でも高純度のカセイソーダ水溶液
が得られることからイオン交換膜式電解法が現在
主流となりつつあり、隔膜式電解法からも更にイ
オン交換膜式法に転換されている。
Conventionally, mercury electrolysis has been used as a common salt electrolysis method because the purity and concentration of the resulting caustic soda aqueous solution can be increased, but this has been changed to diaphragm or ion exchange membrane electrolysis due to mercury pollution problems. Among them, the ion-exchange membrane electrolysis method is currently becoming mainstream because a highly purified caustic soda aqueous solution can be obtained, and the diaphragm electrolysis method is also being converted to the ion-exchange membrane method.

ところで、イオン交換膜式電解槽では、陰極側
に水素とカセイソーダが生成し、このカセイソー
ダ水溶液と水素は電解槽に続く水素分離器により
分離され、カセイソーダ水溶液は濃縮工程に送ら
れる。ここに用いられる水素分離器は通常金属製
であり、電解槽とはパツキングを介してフランジ
でボルト止めがされている。
By the way, in an ion-exchange membrane type electrolytic cell, hydrogen and caustic soda are generated on the cathode side, and this aqueous caustic soda solution and hydrogen are separated by a hydrogen separator following the electrolytic cell, and the aqueous caustic soda solution is sent to a concentration step. The hydrogen separator used here is usually made of metal, and is bolted to the electrolytic cell via a flange via packing.

このように構成されており、かつ電解槽と水素
分離器はボルトにより連結しているので、通常は
等電位にあるはずであるが、意外なことにボルト
が発熱し、ボルト部が焼けてしまうという問題が
あり、また水素分離器にも腐蝕が生じることが見
出された。
With this structure, and the electrolytic cell and hydrogen separator are connected by bolts, they should normally be at equal potential, but unexpectedly the bolts generate heat and burn out. It was also found that corrosion occurred in the hydrogen separator.

本発明者らはこの水素分離器のボルト部の焼け
および腐蝕の原因は電解槽と水素分離器の間に電
位差が生じていることであることを見出し、本発
明を完成するに至つた。
The present inventors have discovered that the cause of the burning and corrosion of the bolt portion of the hydrogen separator is the potential difference between the electrolytic cell and the hydrogen separator, and have completed the present invention.

即ち、本発明はイオン交換膜式食塩電解槽の水
素とカセイソーダ混合物から水素を分離する装置
(水素分離器)の金属部を電解槽と金属線で継ぐ
ことを特徴とする水素分離器の電蝕防止法であ
る。
That is, the present invention provides a method for electrolytic corrosion of a hydrogen separator, characterized in that a metal part of a device (hydrogen separator) for separating hydrogen from a mixture of hydrogen and caustic soda in an ion-exchange membrane salt electrolyzer is connected to the electrolytic cell by a metal wire. It is a prevention method.

以下、図面により本発明を説明する。 The present invention will be explained below with reference to the drawings.

電解槽1の陽極2と陰極3との間にイオン交換
4があり、この陽極側に精製食塩水(通常濃度は
26%である)が導入され、陽極側から塩素と濃度
が薄くなつた食塩水が排出される。一方陰極側に
は通常低濃度のカセイソーダ水溶液が導入され、
イオン交換膜4を通してナトリウムイオンが取り
込まれ、この導入されたカセイソーダ水溶液の濃
度が上がると共に陰極では水素が発生する。この
高濃度のカセイソーダは水素と共に排出され、電
解槽に続く水素分離器5に導入される。ここで水
素は分離され、分離した水素は水素分離器5の上
部に設けられた配管6を通して水素貯槽(図示せ
ず)または水素消費工程(図示せず)に送られ
る。一方、水素を分離したカセイソーダは水素分
離器5に設けられた配管7を経て、一部は濃縮工
程へ送られ残部は水を加えられ電解槽1に循環さ
れる。
There is an ion exchanger 4 between the anode 2 and the cathode 3 of the electrolytic cell 1, and purified saline (normal concentration is
26%) is introduced, and chlorine and diluted salt water are discharged from the anode side. On the other hand, a low concentration caustic soda aqueous solution is usually introduced to the cathode side.
Sodium ions are taken in through the ion exchange membrane 4, and as the concentration of the introduced caustic soda aqueous solution increases, hydrogen is generated at the cathode. This highly concentrated caustic soda is discharged together with hydrogen and introduced into a hydrogen separator 5 following the electrolytic cell. Here, hydrogen is separated, and the separated hydrogen is sent to a hydrogen storage tank (not shown) or a hydrogen consumption process (not shown) through a pipe 6 provided at the top of the hydrogen separator 5. On the other hand, the caustic soda from which hydrogen has been separated passes through a pipe 7 provided in the hydrogen separator 5, and a portion is sent to a concentration step, and the remainder is added with water and circulated to the electrolytic cell 1.

ここにおいて水素分離器5からの漏電を防止す
るため、通常配管7の先にはゴム等の絶縁性物質
による配管がされている。
Here, in order to prevent electrical leakage from the hydrogen separator 5, the end of the pipe 7 is usually connected to a pipe made of an insulating material such as rubber.

また、水素分離器5からの水素配管6も電解槽
1からの漏電防止策がほどこされているので、漏
電対策はほぼ完全であるはずであるが、水素分離
器5から配管7を経て排出されるカセイソーダ水
溶液が導電性体となり、他の所でアースされてい
ることとなつて水素分離器5やこれを取付けるた
めのボルトが焼けたり電蝕を生ずるものと推定さ
れる。
In addition, the hydrogen piping 6 from the hydrogen separator 5 is also equipped with measures to prevent leakage from the electrolytic cell 1, so the leakage prevention should be almost complete. It is presumed that the caustic soda aqueous solution becomes conductive and is grounded elsewhere, causing burning or electrolytic corrosion of the hydrogen separator 5 and the bolts used to attach it.

本発明においては、水素分離器5と電解槽の陰
極室部分の間に良導体である金属、例えば銅の線
8で継ぎ電解槽の陰極室部分と水素分離器5の間
を等電位にする。上記陰極室部分とは、電解槽の
陰極および陰極と常に安定な同電位を維持してい
る電解槽構造物部分である。
In the present invention, a wire 8 made of a metal that is a good conductor, such as copper, is connected between the hydrogen separator 5 and the cathode chamber portion of the electrolytic cell to equalize the potential between the cathode chamber portion of the electrolytic cell and the hydrogen separator 5. The cathode chamber portion is a cathode of the electrolytic cell and a portion of the electrolytic cell structure that always maintains the same stable potential as the cathode.

なお各フランジ間も電解槽1と水素分離器5と
の結線と同様に金属線で継いでおくとボルト部の
焼け防止効果が向上するので好ましい。
Note that it is preferable to connect each flange with a metal wire in the same manner as the connection between the electrolytic cell 1 and the hydrogen separator 5, since this will improve the effect of preventing burning of the bolt portion.

本発明の水素分離器の電蝕防止法は、単に電解
槽との陰極室部分と水素分離器を金属線で継ぐの
みで達せられるのできわめて効率的である。
The method of preventing electrolytic corrosion of a hydrogen separator according to the present invention is extremely efficient because it can be achieved simply by connecting the cathode chamber with the electrolytic cell and the hydrogen separator with a metal wire.

また水素分離器が電蝕により破壊することがな
くなるのできわめて安全性も良好となる。
Furthermore, since the hydrogen separator will not be destroyed by electrolytic corrosion, safety is also improved.

ところで本発明の方法では、やはり水素分離器
5の配管7の金属部の先端が徐々にではあるが腐
蝕してくるので、この部分をフランジにより接続
しておけば容易に取り換えることができるので好
ましい。
However, in the method of the present invention, the tip of the metal part of the pipe 7 of the hydrogen separator 5 gradually corrodes, so it is preferable to connect this part with a flange so that it can be easily replaced. .

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

第1図はイオン交換膜式食塩電解槽と水素分離
器の要部を示す概念図である。図中各符号は次の
意味である。 1…電解槽、2…陽極、3…陰極、4イオン交
換膜、5…水素分離器、6…水素配管、7…カセ
イソーダ水溶液配管、8…金属線。
FIG. 1 is a conceptual diagram showing the main parts of an ion exchange membrane type salt electrolyzer and a hydrogen separator. Each symbol in the figure has the following meaning. DESCRIPTION OF SYMBOLS 1... Electrolytic cell, 2... Anode, 3... Cathode, 4... Ion exchange membrane, 5... Hydrogen separator, 6... Hydrogen piping, 7... Caustic soda aqueous solution piping, 8... Metal wire.

Claims (1)

【特許請求の範囲】[Claims] 1 イオン交換膜式食塩電解槽の水素とカセイソ
ーダの混合物から水素を分離する装置(水素分離
器)の金属部を電解槽の陰極室部分と金属線で継
ぐことを特徴とする水素分離器の電蝕防止法。
1. An electric hydrogen separator characterized in that the metal part of the device (hydrogen separator) for separating hydrogen from a mixture of hydrogen and caustic soda in an ion-exchange membrane salt electrolyzer is connected to the cathode chamber part of the electrolyzer with a metal wire. Erosion prevention method.
JP59188236A 1984-09-10 1984-09-10 Electrolytic corrosion prevention of hydrogen separator for salt electrolyzing cell Granted JPS6167781A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59188236A JPS6167781A (en) 1984-09-10 1984-09-10 Electrolytic corrosion prevention of hydrogen separator for salt electrolyzing cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59188236A JPS6167781A (en) 1984-09-10 1984-09-10 Electrolytic corrosion prevention of hydrogen separator for salt electrolyzing cell

Publications (2)

Publication Number Publication Date
JPS6167781A JPS6167781A (en) 1986-04-07
JPH0425351B2 true JPH0425351B2 (en) 1992-04-30

Family

ID=16220170

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59188236A Granted JPS6167781A (en) 1984-09-10 1984-09-10 Electrolytic corrosion prevention of hydrogen separator for salt electrolyzing cell

Country Status (1)

Country Link
JP (1) JPS6167781A (en)

Also Published As

Publication number Publication date
JPS6167781A (en) 1986-04-07

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