JPS6241973Y2 - - Google Patents
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- Publication number
- JPS6241973Y2 JPS6241973Y2 JP1980175575U JP17557580U JPS6241973Y2 JP S6241973 Y2 JPS6241973 Y2 JP S6241973Y2 JP 1980175575 U JP1980175575 U JP 1980175575U JP 17557580 U JP17557580 U JP 17557580U JP S6241973 Y2 JPS6241973 Y2 JP S6241973Y2
- Authority
- JP
- Japan
- Prior art keywords
- anode
- plate
- cathode
- exchange membrane
- vertical
- 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
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- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
【考案の詳細な説明】
本考案はイオン交換膜をとりつけた竪型水溶液
電解槽に関する。[Detailed Description of the Invention] The present invention relates to a vertical aqueous electrolytic cell equipped with an ion exchange membrane.
従来アルカリ金属塩化物(例えば食塩)の水溶
液を電解する方法として、水銀法、隔膜法および
イオン交換膜法がある。水銀法では製品カセイア
ルカリの濃度が高く、且つ高純度のものがえられ
るが、水銀が漏洩して環境汚染の問題を起こす可
能性があるため、近年、隔膜法に転換されつゝあ
る。然し隔膜法は生成するカセイアルカリの濃度
が約9〜12%と低く、且つ不純物としてかなりの
アルカリ金属塩化物を含んでいる。このため製品
の用途によつては精製や濃縮を更に行う必要があ
る。これら隔膜法の欠点を考慮し、陽イオン交換
膜を用いる方法が開発されつゝあり、そのための
電解槽としては例えばフイルタープレス型のもの
が一般に採用されている。 Conventional methods for electrolyzing aqueous solutions of alkali metal chlorides (eg, common salt) include a mercury method, a diaphragm method, and an ion exchange membrane method. The mercury method produces a product with a high concentration of caustic alkali and high purity, but in recent years it has been replaced by the diaphragm method because of the possibility of mercury leaking and causing environmental pollution problems. However, in the diaphragm method, the concentration of the caustic alkali produced is as low as about 9 to 12%, and it also contains a considerable amount of alkali metal chloride as an impurity. Therefore, depending on the intended use of the product, further purification or concentration may be required. In consideration of the drawbacks of these diaphragm methods, methods using cation exchange membranes are being developed, and as the electrolytic cell for this purpose, for example, a filter press type is generally employed.
然し、従来使用してきた隔膜法に代りイオン交
換膜法を採用する場合、新に電解槽を製作するこ
とは不経済であり、隔膜法用の電解槽の転用が強
く要望されてきた。 However, when adopting the ion exchange membrane method instead of the conventionally used diaphragm method, it is uneconomical to manufacture a new electrolytic cell, and there has been a strong demand for repurposing the electrolytic cell for the diaphragm method.
隔膜法用の電解槽としては竪型と水平型とがあ
るが、本考案は竪型の電解槽の改良に関するもの
である。隔膜法用の電解槽のアスベスト隔膜はア
スベストスラリーからアスベストを陰極金網に沈
着させて作るがこのアスベスト隔膜の代りに陽イ
オン交換膜を直ちにとりつけることは不可能であ
り、陽イオン交換膜の取りつけ装置が問題にな
る。 There are vertical and horizontal types of electrolytic cells for the diaphragm method, and the present invention relates to improvements to vertical electrolytic cells. The asbestos diaphragm of an electrolytic cell for the diaphragm method is made by depositing asbestos from an asbestos slurry onto a cathode wire mesh, but it is impossible to immediately install a cation exchange membrane in place of this asbestos diaphragm, and a cation exchange membrane installation device is required. becomes a problem.
従つて本考案は従来の隔膜法用の竪型水溶液電
解槽をイオン交換膜法用に転用することを目的と
するものであり、鋭意研究の結果完成されたもの
である。 Therefore, the present invention aims to convert the conventional vertical aqueous electrolyzer for the diaphragm method to the ion exchange membrane method, and was completed as a result of intensive research.
すなわち本考案は、陽極板とそれを囲む箱形陰
極金網とが配置されている竪型水溶液電解槽にお
いて、陰極金網の上方に空間部分を保持して該陰
極金網上部を囲覆する側板付陰極カバーと、陽極
ロツドが貫通している穴を底部に有し周囲には陽
極板下方を包囲する鉛直側板を有し、陽極ロツド
に設けられた鍔と陽極取付板面とにより水密に挾
持固定された取付用部材と、陽極の各鉛直面に平
行で陽極を覆つて設けられ、且つ陽極に対する面
は有孔であり、上辺は陰極カバーの側板に、下辺
は取付用部材の鉛直側板に夫々気密、水密に取り
つけられた管状フレームと該フレームの陽極側に
フレーム有孔部分を完全に覆つて気密、水密に固
定されている陽イオン交換膜とが設けられている
竪型水溶液電解槽に関する。 That is, the present invention provides a cathode with a side plate that maintains a space above the cathode wire mesh and surrounds the upper part of the cathode wire mesh in a vertical aqueous electrolytic cell in which an anode plate and a box-shaped cathode wire mesh surrounding the anode plate are arranged. It has a cover and a hole at the bottom through which the anode rod passes, and a vertical side plate surrounding the lower part of the anode plate, and is watertightly clamped and fixed by a flange provided on the anode rod and an anode mounting plate surface. The mounting member is provided parallel to each vertical plane of the anode and covers the anode, and the surface facing the anode is perforated, the upper side is airtightly attached to the side plate of the cathode cover, and the lower side is attached to the vertical side plate of the mounting member This invention relates to a vertical aqueous electrolytic cell that is provided with a tubular frame that is watertightly attached and a cation exchange membrane that is fixed to the anode side of the frame in an airtight and watertight manner so as to completely cover the perforated part of the frame.
本明細書において、気密、水密とは陰極区域
(陰極室)及び陽極区域(陽極室)間の気体及び
液体の流通が事実上遮断されている状態をいう。 In this specification, airtightness and watertightness refer to a state in which the flow of gas and liquid between the cathode area (cathode chamber) and the anode area (anode chamber) is virtually blocked.
次に、本考案の代表的な例を示す第1図イ,
ロ、第2図及び第3図にもとづいて本考案を説明
する。 Next, Figure 1A shows a typical example of the present invention.
B. The present invention will be explained based on FIGS. 2 and 3.
第1図イ,ロは本考案の電解槽の構成を示すも
のでイは一部平面図(ロのb−b′横断面)、ロは
一部縦断面斜視図、(イのa−a′縦断面)であ
る。図において、1は箱型陰極金網、2は陽極
板、3は陰極カバーであつて、陰極カバー3は箱
型陰極金網1の上方に空間部分4を保持してもう
けられ、該空間部分4は発生する水素ガス捕集用
の大きな容積をもつ。箱型陰極金網は第1図a,
bに示す如く箱型で陽極板を包囲してもうけられ
ている。5は陽極取付板、6はその上にもうけら
れたシートパツキングであつて、陽極板2には陽
極ロツド7が貫入、埋設してとりつけられてい
る。8は底部中心線上に穿孔を設けた取付用部材
で、陽極ロツド7に設けられた鍔16と陽極取付
板5との間にパツキング6を介して固定されてい
る。又9は陰極カバー3の側板であり、該側板9
と、前記取付用部材8の周囲にある鉛直側板9′
との間には陽極の鉛直面に平行で、且つ陽極を覆
うようにもうけられており、且つ該陽極に相対す
る部分のみは格子状等の有孔構造となつている管
状フレームAが側板9と鉛直側板9′に気密、水
密に取りつけられている。10は管状の陽イオン
交換膜であつて、フレームAを陽極側より完全に
覆い、且つ管状フレームAの上下部分において気
密、水密に固定されている。イオン交換膜はこの
場合陰極周囲を囲める寸法の管状体を使用すると
膜の接合部がなくなり便利である。またイオン交
換膜は管状フレームの有孔部分の陽極側を覆うの
で水位の高い陽極側より水圧により押されて管状
フレームAの面に固定される効果がある。 Figures 1A and 1B show the configuration of the electrolytic cell of the present invention. 'longitudinal section). In the figure, 1 is a box-shaped cathode wire mesh, 2 is an anode plate, and 3 is a cathode cover. The cathode cover 3 is provided with a space 4 held above the box-shaped cathode wire mesh 1. It has a large volume for collecting generated hydrogen gas. The box-shaped cathode wire mesh is shown in Figure 1a,
As shown in b, it is box-shaped and surrounds the anode plate. 5 is an anode mounting plate, 6 is a sheet packing provided thereon, and an anode rod 7 penetrates and is embedded in the anode plate 2 and is attached thereto. Reference numeral 8 denotes a mounting member having a hole provided on the center line of the bottom, and is fixed via a packing 6 between a collar 16 provided on the anode rod 7 and the anode mounting plate 5. Further, 9 is a side plate of the cathode cover 3;
and a vertical side plate 9' around the mounting member 8.
A tubular frame A is provided between the side plate 9 and the side plate 9 so as to be parallel to the vertical plane of the anode and cover the anode, and only the portion facing the anode has a perforated structure such as a grid. and is attached airtightly and watertightly to the vertical side plate 9'. Reference numeral 10 denotes a tubular cation exchange membrane, which completely covers the frame A from the anode side and is fixed airtightly and watertightly at the upper and lower portions of the tubular frame A. In this case, it is convenient for the ion exchange membrane to use a tubular body with a size that can surround the cathode, since there are no membrane joints. Furthermore, since the ion exchange membrane covers the anode side of the perforated portion of the tubular frame, it has the effect of being pushed by water pressure from the anode side where the water level is higher and being fixed to the surface of the tubular frame A.
このような構造とすることにより、陽極室と陰
極室とはイオン交換膜により完全に水密、気密に
分離している。陽イオン交換膜10と管状フレー
ムAとは陽イオン交換膜10の固定のために密に
接触していればよくその構造は限定されないが、
その代表的な例の詳細を第2図に示す。第2図に
おいて側板9、鉛直側板9′の端縁部にフレーム
Aが設けられ、該フレームAの陽極側には陽イオ
ン交換膜10が配され11で示されるパツキング
を介して押え板12,12′、13,13′、ボル
ト14,14′およびナツト15,15′により締
めつけられ気密、水密に固定されている。又第2
図において陽極ロツド7には鍔16がもうけら
れ、鍔16と陽極取付板5との間にはパツキング
6,17を介して取付部材8が固定されている。 With this structure, the anode chamber and the cathode chamber are completely watertightly and airtightly separated by the ion exchange membrane. The structure of the cation exchange membrane 10 and the tubular frame A is not limited as long as they are in close contact to fix the cation exchange membrane 10.
The details of a typical example are shown in FIG. In FIG. 2, a frame A is provided at the edge of the side plate 9 and the vertical side plate 9', and a cation exchange membrane 10 is arranged on the anode side of the frame A, and a holding plate 12, 12', 13, 13', bolts 14, 14', and nuts 15, 15' are tightened and fixed airtightly and watertightly. Also second
In the figure, a collar 16 is provided on the anode rod 7, and a mounting member 8 is fixed between the collar 16 and the anode mounting plate 5 via packings 6 and 17.
第3図は陽極板2と陽極ロツド7及び取付用部
材8の組立構造を示す斜視図である。 FIG. 3 is a perspective view showing the assembly structure of the anode plate 2, anode rod 7, and mounting member 8.
本考案の電解槽は従来のイオン交換膜法用の電
解槽と同じく陽極室と陰極室とが陽イオン交換膜
により完全に分離され、製造されるカセイアルカ
リ溶液中のアルカリ金属塩化物の量は極めて少
い。又陰極室において箱型陰極金網と陰極カバー
との間には水素捕集用の大きな空間があるため、
陽極板2は電解液中に完全に浸せられるので陽極
板2の全電解面を有効に利用することができる。
またイオン交換膜の固定性がよく電解が安定に行
われる。なお陽極室からは塩素が発生するので、
前記押え板等露出部はチタン、チタン合金、フツ
素樹脂等の耐食性の材料を使用する必要がある。 In the electrolytic cell of the present invention, the anode chamber and the cathode chamber are completely separated by a cation exchange membrane, similar to the conventional electrolytic cell for ion exchange membrane method, and the amount of alkali metal chloride in the produced caustic alkaline solution is Very few. In addition, in the cathode chamber, there is a large space for hydrogen collection between the box-shaped cathode wire mesh and the cathode cover.
Since the anode plate 2 is completely immersed in the electrolyte, the entire electrolytic surface of the anode plate 2 can be effectively utilized.
In addition, the ion exchange membrane has good fixation and electrolysis can be carried out stably. Note that chlorine is generated from the anode chamber, so
It is necessary to use a corrosion-resistant material such as titanium, titanium alloy, or fluororesin for the exposed parts such as the presser plate.
本装置の組立は容易である。次にその一例を示
す。 Assembly of this device is easy. An example is shown below.
まず電解槽体に箱型陰極金網をとりつけてお
く。 First, a box-shaped cathode wire mesh is attached to the electrolytic cell body.
次に陰極カバー3の側板9の下端に第2図に示
すように、押え板13、ナツト15を例えば溶接
により固着する。そして側板9、押え板13にナ
ツト15の孔にあわせて共通の貫通孔をもうけて
おく。 Next, as shown in FIG. 2, a presser plate 13 and a nut 15 are fixed to the lower end of the side plate 9 of the cathode cover 3 by, for example, welding. A common through hole is provided in the side plate 9 and the holding plate 13 to match the hole in the nut 15.
別に取付用部材8の鉛直側板9′に、第2図に
示すように管状フレームAの下端、陽イオン交換
膜の下端を押え板12′,13′、ナツト15′、
ボルト14′により固定する。これにより取付用
部材8に管状フレームAおよび陽イオン交換膜1
0がとりつけられて一体化された構造体を得る。
この一体化された構造体の取付用部材8を、その
穿孔が陽極取付板5の孔に一致するようシートパ
ツキングを介して該取付板5の上に載置する。 Separately, as shown in FIG. 2, attach the lower end of the tubular frame A and the lower end of the cation exchange membrane to the vertical side plate 9' of the mounting member 8 with holding plates 12', 13', nuts 15',
It is fixed with bolts 14'. As a result, the tubular frame A and the cation exchange membrane 1 are attached to the mounting member 8.
0 is attached to obtain an integrated structure.
The mounting member 8 of this integrated structure is placed on the mounting plate 5 via sheet packing so that its perforation matches the hole in the anode mounting plate 5.
つぎに陽極板2の陽極ロツド7を前記の取付用
部材8、陽極取付板5の穿孔に挿入した後、ロツ
ドの鍔16を第2図に示すようにパツキング17
を介して陽極取付板5に公知の手段により固定す
る。 Next, after inserting the anode rod 7 of the anode plate 2 into the mounting member 8 and the hole in the anode mounting plate 5, the flange 16 of the rod is inserted into the packing 17 as shown in FIG.
It is fixed to the anode mounting plate 5 via known means.
最後に前記一体化された構造体の上端部に第2
図に示すようにイオン交換膜10側にパツキング
を介して押え板12を、又、環状フレームA側に
押え板13、ナツト15を固着した陰極カバー9
を、それらのすべての穴が連通するように保持し
た後、押え板12側より即ち陽極室側よりボルト
14を前記連通孔に挿入して、ナツト15に螺入
させる。これにより陰極カバー3はその側板9に
おいて管状フレームA、イオン交換膜と水密、気
密に固定される。 Finally, a second
As shown in the figure, a cathode cover 9 has a holding plate 12 fixed to the ion exchange membrane 10 side through packing, and a holding plate 13 and a nut 15 fixed to the annular frame A side.
is held so that all the holes communicate with each other, and then the bolt 14 is inserted into the communication hole from the holding plate 12 side, that is, from the anode chamber side, and screwed into the nut 15. Thereby, the cathode cover 3 is fixed to the tubular frame A and the ion exchange membrane at the side plate 9 in a watertight and airtight manner.
なお、本発明では陽極板の取付用部材および陽
極取付板への固定は、陰極カバーと一体化構造体
との固定前に行なつているが、カバーと一体化構
造体との固定後に行なつてもよい。 Note that in the present invention, the anode plate is fixed to the mounting member and the anode mounting plate before the cathode cover and the integrated structure are fixed, but it is fixed after the cover and the integrated structure are fixed. You can.
又陽極カバーの他の端部は第1図ロに示される
ように電解槽の側壁と電解槽蓋との間に挟持さ
れ、気密、水密に固定される。 The other end of the anode cover is sandwiched between the side wall of the electrolytic cell and the electrolytic cell lid, as shown in FIG. 1B, and fixed airtightly and watertightly.
第1図イは本考案の電解槽の構成を示す一部平
面図、第1図はロは一部縦断面斜視図、第2図は
陰極カバー、取付部材、フレーム及び陽イオン交
換膜の接続部分の詳細の一例を示す図、第3図は
陽極板、陽極ロツドと取付用部材の組立構造を示
す斜視図である。
主な符号の説明をする。1……箱型陰極金網、
2……陽極板、3……陰極カバー、4……陰極と
陰極カバーとの間の空間、8……取付部材、9…
…陰極カバーの側板、9′……取付部材8の鉛直
側板、10……陽イオン交換膜、A……管状フレ
ーム。
Figure 1A is a partial plan view showing the structure of the electrolytic cell of the present invention, Figure 1B is a partial vertical cross-sectional perspective view, and Figure 2 is the connection of the cathode cover, mounting members, frame, and cation exchange membrane. FIG. 3 is a perspective view showing an assembly structure of an anode plate, an anode rod, and a mounting member. Explain the main symbols. 1...Box-shaped cathode wire mesh,
2...Anode plate, 3...Cathode cover, 4...Space between the cathode and cathode cover, 8...Mounting member, 9...
...Side plate of cathode cover, 9'...Vertical side plate of mounting member 8, 10...Cation exchange membrane, A...Tubular frame.
Claims (1)
れている竪型水溶液電解槽において、 (ロ) 陰極金網の上方に空間部分を保持して該陰極
金網上部を囲覆する側板付陰極カバーと、 (ハ) 陽極ロツドが貫通している穴を有し周囲には
陽極板下方を包囲する鉛直側板を有し、陽極ロ
ツドに設けられた鍔と陽極取付板面とにより水
密に挟持固定された取付用部材と、 (ニ) 陽極の各鉛直面に平行で陽極を覆つて設けら
れ、且つ陽極に対する面は有孔であり、上辺は
陰極カバーの側板に、下辺は取付用部材の鉛直
側板に夫々気密、水密に取り付けられた管状フ
レームと、 (ホ) 該フレームの陽極側にフレームの有孔部分を
完全に覆つて気密、水密に固定されている陽イ
オン交換膜 とが設けられていることを特徴とする竪型水溶
液電解槽。[Scope of Claim for Utility Model Registration] (a) In a vertical aqueous electrolytic cell in which an anode plate and a box-shaped cathode wire mesh surrounding the anode plate are arranged, (b) a space above the cathode wire mesh is maintained so that the cathode (c) a cathode cover with a side plate that surrounds the upper part of the wire mesh, and (c) a vertical side plate that has a hole through which the anode rod passes and surrounds the lower part of the anode plate, and a collar provided on the anode rod and the anode. (d) a mounting member that is watertightly clamped and fixed by the mounting plate surface; (e) A tubular frame whose lower side is airtightly and watertightly attached to the vertical side plate of the mounting member; A vertical aqueous electrolytic cell characterized by being provided with a cation exchange membrane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1980175575U JPS6241973Y2 (en) | 1980-12-09 | 1980-12-09 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1980175575U JPS6241973Y2 (en) | 1980-12-09 | 1980-12-09 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57102570U JPS57102570U (en) | 1982-06-24 |
| JPS6241973Y2 true JPS6241973Y2 (en) | 1987-10-27 |
Family
ID=29967982
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1980175575U Expired JPS6241973Y2 (en) | 1980-12-09 | 1980-12-09 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6241973Y2 (en) |
-
1980
- 1980-12-09 JP JP1980175575U patent/JPS6241973Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57102570U (en) | 1982-06-24 |
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