JPH0429751B2 - - Google Patents
Info
- Publication number
- JPH0429751B2 JPH0429751B2 JP59171435A JP17143584A JPH0429751B2 JP H0429751 B2 JPH0429751 B2 JP H0429751B2 JP 59171435 A JP59171435 A JP 59171435A JP 17143584 A JP17143584 A JP 17143584A JP H0429751 B2 JPH0429751 B2 JP H0429751B2
- Authority
- JP
- Japan
- Prior art keywords
- caustic soda
- aqueous solution
- hydrogen
- soda aqueous
- hydrogen separator
- 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 - Lifetime
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- 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
離器の腐蝕防止法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for preventing 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及び濃度が高
くできることから行われていた。しかし、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。 BACKGROUND ART Conventionally, as a common salt electrolysis method, a mercury electrolysis method has been used because the purity and concentration of the resulting caustic soda aqueous solution can be increased. However, due to mercury pollution problems, the method has been changed to a diaphragm type or ion exchange membrane type electrolysis method.
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
ン交換膜式電解法に転換されている。 Among these, 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 replaced by the ion-exchange membrane electrolysis method.
ところで、イオン交換膜式電解法では、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。 By the way, in the ion exchange membrane electrolysis method, hydrogen and caustic soda are generated on the cathode side, and the caustic soda aqueous solution and hydrogen are separated by a hydrogen separator following the electrolytic cell, and the caustic soda aqueous solution is sent to a concentration step.
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ボル
ト止めがされている。 The hydrogen separator used here is usually made of metal and is connected to the electrolytic cell through packing with flange bolts.
この様に構成され、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、水素分離器にも腐食が生じることが見出され
た。 Since the electrolytic cell and the hydrogen separator are constructed in this way and are connected by bolts, they should normally be at equal potential, but unexpectedly, the problem is that the bolts generate heat and burn out the bolts. 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
け及び腐食の原因は、カセイソーダ水溶液が導電
体になつていることによるものであることを見出
し、遂に、本発明を完成するに到つた。 The present inventors discovered that the cause of the burning and corrosion of the bolt portion of the hydrogen separator is that the caustic soda aqueous solution is a conductor, and finally 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水素分離器
で分離したのち、カセイソーダ水溶液を電気絶縁
性物質でできた滴下装置の内部に設けた、カセイ
ソーダ水溶液を点滴状にする分散板上に導入し、
該カセイソーダ水溶液を該滴下装置内で点滴状に
滴下することを特徴とする食塩電解槽の水素分離
器の腐蝕防止法である。 That is, the present invention separates hydrogen from a mixture of hydrogen and caustic soda in an ion-exchange membrane salt electrolyzer using a hydrogen separator, and then the caustic soda aqueous solution is placed inside a dropping device made of an electrically insulating material. Introduced onto a dispersion plate to form a drop,
This is a method for preventing corrosion of a hydrogen separator of a salt electrolytic cell, characterized in that the caustic soda aqueous solution is dripped in the dripping device.
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
膜4があり、この陽極側に精製食塩水(通常、濃
度は25〜26wt%)が導入され、陽極側から塩素
と濃度が低くなつた食塩水が排出される。 There is an ion exchange membrane 4 between the anode 2 and the cathode 3 of the electrolytic cell 1, and purified saline (usually at a concentration of 25 to 26 wt%) is introduced to the anode side, and the concentration is lowered to chlorine from the anode side. The saline solution is drained out.
一方、陰極側には、通常低濃度のカセイソーダ
水溶液(水のみの場合もある)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。 On the other hand, a low-concentration caustic soda aqueous solution (sometimes only water) is introduced to the cathode side, and sodium ions are taken in through the ion exchange membrane 4, and the concentration of the introduced caustic soda aqueous solution increases. Hydrogen is generated. This highly concentrated caustic soda is discharged together with hydrogen and introduced into a hydrogen separator 5 following the electrolytic cell.
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。 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.
一方、水素を分離されたカセイソーダ水溶液
は、水素分離器5から配管7を経て滴下装置11
に至る。 On the other hand, the caustic soda aqueous solution from which hydrogen has been separated is passed from the hydrogen separator 5 through the pipe 7 to the dropping device 11.
leading to.
滴下装置内には、電気絶縁性物質でできた適当
な孔径を適当個数有するカセイソーダ水溶液の分
散板12が設けられている。 A dispersion plate 12 for an aqueous caustic soda solution made of an electrically insulating material and having a suitable number of holes of a suitable size is provided in the dropping device.
ここに到来したカセイソーダ水溶液は、この分
散板12を通過することにより点滴状に滴下し、
もはや、液としての連続性は断ち切られることに
より水素分離器5に関する電気回路は形成される
ことはなく、従つて、腐食の原因となる電流はな
くなり、ここに水素分離器5の電流による腐食は
防止される。 The caustic soda aqueous solution that has arrived here passes through this dispersion plate 12 and is dripped in the form of a drip.
Since the continuity as a liquid is broken, an electric circuit related to the hydrogen separator 5 is no longer formed, and therefore, there is no current that causes corrosion, and corrosion due to the current in the hydrogen separator 5 is no longer formed. Prevented.
本発明の水素分離器の腐蝕防止法は生成したカ
セイソーダ水溶液を簡単な滴下装置を用いて滴下
させることにより腐蝕防止法が達せられ、また、
水素分離器が腐蝕により破壊することもなく安全
性も良好となり工業的に寄与するところ大であ
る。 The corrosion prevention method of the hydrogen separator of the present invention is achieved by dropping the generated caustic soda aqueous solution using a simple dripping device, and also,
The hydrogen separator will not be destroyed due to corrosion and will be safe, which will greatly contribute to the industrial field.
第1図は、本発明の方法を実施する電解槽、水
素分離器及びカセイソーダ滴下装置を示す概略図
である。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…水素排出配管、7
…水素分離器のカセイソーダ水溶液排出配管、8
…カセイソーダ水溶液、9…水素分離器のカセイ
ソーダ水溶液導入配管、10…均圧配管、11…
カセイソーダ水溶液の滴下装置、12…カセイソ
ーダ水溶液の分散板、13…滴状カセイソーダ水
溶液、14…カセイソーダ水溶液。
FIG. 1 is a schematic diagram showing an electrolytic cell, a hydrogen separator, and a caustic soda dropping device for carrying out the method of the present invention. Each symbol has the following meaning. 1... Electrolytic cell, 2... Anode, 3... Cathode, 4... Ion exchange membrane, 5... Hydrogen separator, 6... Hydrogen discharge piping, 7
...Hydrogen separator caustic soda aqueous solution discharge piping, 8
... Caustic soda aqueous solution, 9... Caustic soda aqueous solution introduction pipe of hydrogen separator, 10... Pressure equalization pipe, 11...
A dropping device for a caustic soda aqueous solution, 12... A dispersion plate for a caustic soda aqueous solution, 13... A droplet-like caustic soda aqueous solution, 14... A caustic soda aqueous solution.
Claims (1)
素とカセイソーダ水溶液の混合物を水素分離器で
分離したのち、カセイソーダ水溶液を電気絶縁性
物質でできた滴下装置の内部に設けた、カセイソ
ーダ水溶液を点滴状にする分散板上に導入し、該
カセイソーダ水溶液を該滴下装置内で点滴状に滴
下することを特徴とする食塩電解槽の水素分離器
の腐蝕防止法。1. After separating the mixture of hydrogen and caustic soda aqueous solution discharged from the ion-exchange membrane type salt electrolyzer using a hydrogen separator, the caustic soda aqueous solution is placed inside a dripping device made of an electrically insulating material. A method for preventing corrosion of a hydrogen separator of a salt electrolytic cell, characterized in that the caustic soda aqueous solution is introduced onto a dispersion plate in which the caustic soda is dissolved, and the caustic soda aqueous solution is dripped in the dripping device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59171435A JPS6152377A (en) | 1984-08-20 | 1984-08-20 | Method for preventing corrosion of hydrogen separator for sodium chroride electrolytic cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59171435A JPS6152377A (en) | 1984-08-20 | 1984-08-20 | Method for preventing corrosion of hydrogen separator for sodium chroride electrolytic cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6152377A JPS6152377A (en) | 1986-03-15 |
| JPH0429751B2 true JPH0429751B2 (en) | 1992-05-19 |
Family
ID=15923066
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59171435A Granted JPS6152377A (en) | 1984-08-20 | 1984-08-20 | Method for preventing corrosion of hydrogen separator for sodium chroride electrolytic cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6152377A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0554416U (en) * | 1991-10-16 | 1993-07-20 | 高浜工業株式会社 | Hanger for transporting tile base material |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5535337U (en) * | 1978-08-25 | 1980-03-06 |
-
1984
- 1984-08-20 JP JP59171435A patent/JPS6152377A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6152377A (en) | 1986-03-15 |
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