JPS60110890A - Finger anode in bipolar alkaline chloride electrolyzer assembly unit - Google Patents
Finger anode in bipolar alkaline chloride electrolyzer assembly unitInfo
- Publication number
- JPS60110890A JPS60110890A JP58216613A JP21661383A JPS60110890A JP S60110890 A JPS60110890 A JP S60110890A JP 58216613 A JP58216613 A JP 58216613A JP 21661383 A JP21661383 A JP 21661383A JP S60110890 A JPS60110890 A JP S60110890A
- Authority
- JP
- Japan
- Prior art keywords
- anode
- finger
- cathode
- power supply
- attached
- 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.)
- Granted
Links
Landscapes
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
Description
【発明の詳細な説明】
不発[Jjは、既存の複極式隔膜電解槽において、アス
ベスト隔膜に代えて陽イオン交換膜を用いるに際し、低
い電槽電圧で操業するのに好適な電解槽組立ユニットに
おけるフィンガー陽極に関する。[Detailed Description of the Invention] Unexploded [Jj is an electrolytic cell assembly unit suitable for operating at a low cell voltage when using a cation exchange membrane in place of an asbestos diaphragm in an existing bipolar diaphragm electrolytic cell. Regarding finger anodes in.
塩化アルカリを′11を解して苛性アルカリを得る方法
it公害防止の見地から、水銀法から代ってアスベスト
隔膜を用いる隔膜法に転換され現在この隔膜法が塩化ア
ルカ・り水溶液の電解法の主流となっている。A method for obtaining caustic alkali by dissolving alkali chloride in '11 From the viewpoint of pollution prevention, the mercury method was replaced by the diaphragm method using an asbestos diaphragm.Currently, this diaphragm method is used as the electrolytic method for aqueous alkali chloride solutions. It has become mainstream.
この隔膜法電解槽としては、多数の電解槽ユニットが互
いに接合組付伏されたものが用いられ、各電解槽ユニッ
トは隔壁に接合された給電棒の一端には陰極パックスク
リーンを介して水平断面がU字形をなす多数のフィンガ
ー陰極の脚部が溶接取付けされ、前記電極棒の他端には
給電体を介して同じく水平断面が、U字形をなす多数の
フィンガー陽極の脚部が溶接取付されている。電解槽ユ
ニットを互いに接合組付けるとき、隣接ユニットのフィ
ンガー陰極とフィンガー陽極とは食違い状に入シ込んで
複極式の電解槽(以下フィンガ一槽という)を構成する
。またフィンガー陰極にはアスベスト隔膜が層状に付着
形成される。なお電解槽の最端部ユニットは、フィンガ
ー陽極もしくはフィンガー陰極のいずれか一方のみを備
えていて隣接する中間ユニットのフィンガー陰極もしく
はフィンガー陽極と互いに組伺けられる。This diaphragm method electrolytic cell uses a large number of electrolytic cell units that are assembled and assembled together, and each electrolytic cell unit is connected to one end of the power supply rod that is connected to the partition wall through a cathode pack screen. The legs of a number of finger cathodes having a U-shape are welded to the other end of the electrode rod, and the legs of a number of finger anodes having a U-shape in horizontal cross section are welded to the other end of the electrode rod via a power supply body. ing. When the electrolytic cell units are joined and assembled together, the finger cathodes and finger anodes of adjacent units are inserted in a staggered manner to form a bipolar electrolytic cell (hereinafter referred to as one finger cell). Further, an asbestos diaphragm is attached and formed in a layer on the finger cathode. Note that the end unit of the electrolytic cell is provided with only either a finger anode or a finger cathode, and is assembled with the finger cathode or finger anode of the adjacent intermediate unit.
フィンガー11[はエキスパンドメツシーに形成された
チタン板を水平断面がU字状をなすようにnl(曲しそ
の両脚部は一つの給電体に溶接されている。またフィン
ガー陰極は軟鋼製のワイヤーを織上り゛た網状物を水号
′萌面がU字状をなすように屈曲しその両IJI’11
部は1興イ帆バツクスクリーンおよび給?l’i’、
4’j″・の−*i、’+ VCC接接れている。NM
して前記給電棒i11.11.、角γb”/ユニット
の貼IF、(を通して陽極ボックス側へ9J1ひ、前1
.[シフィンガー円イ至が接続されている給電体に済)
λ、されている。The finger 11 is made by bending a titanium plate formed into an expanded metal sheet so that its horizontal section forms a U-shape, and its both legs are welded to one power supply.The finger cathode is made of a mild steel wire. IJI'11
Is the department 1 entertainment back screen and salary? l'i',
-*i, '+ of 4'j'' is connected to VCC. NM
and said power supply rod i11.11. , Angle γb''/unit pasting IF, (through 9J1 to the anode box side, front 1
.. [Selected to be the power supply to which Schiffer is connected.]
λ, has been.
アスベスト1′1°1〜膜を隔てて形成されるフィンガ
ー1i″54’piの中空内部および隔壁と陰極パック
スクリーン間の壁間γ−1−8・J:陰4i; %jを
構成し、アスベスト隔膜の外部ジなわちフィンガー陽極
の存する側は陽極室を構成すZ)。The hollow interior of the fingers 1i''54'pi formed across the asbestos 1'1°1~membrane and the wall gap between the partition wall and the cathode pack screen γ-1-8 J: Yin 4i; constitutes %j, The external side of the asbestos diaphragm, ie the side on which the finger anodes are located, constitutes the anode chamber Z).
以上のように構成された既存のアスベストを隔膜として
用いる隔膜法1→、解槽よシ得られる苛性アルカリは濃
度が低く、且つ多溺の塩化アルカリが不純物として含ま
れ、レーヨン工業などへ直接利用することがケ11かし
い。これに対し、塩化アルカリを含1ず、しかもK l
’A1度の苛性アルカリが直接得られる電解法として陽
イオン交換膜を使用するイオン交換膜法が開発されてい
る。Diaphragm method 1 using the existing asbestos constructed as above as a diaphragm → The caustic alkali obtained from tank decomposition has a low concentration and contains a large amount of alkali chloride as an impurity, so it is directly used for the rayon industry etc. It's hard to do that. On the other hand, it does not contain alkali chloride and K l
An ion exchange membrane method using a cation exchange membrane has been developed as an electrolytic method that can directly obtain a caustic alkali having an A1 degree.
したがって、既存のアスベスト隔膜法電解槽を利用しア
スベスト隔膜に代えて陽イオン交換膜をフィンガー陰極
に装着することにょシ、塩化アルカリを電解して高純度
、高濃度苛性アルカリがイ(Jられれば、電解槽関係の
多大な設備投資をせずにイオン交換法電解に変換可能と
なシ、工業的メリットは非常に大きいものになる。Therefore, it is necessary to use the existing asbestos diaphragm method electrolytic cell and attach a cation exchange membrane to the finger cathode in place of the asbestos diaphragm. , it is possible to convert to ion exchange electrolysis without a large investment in equipment related to electrolyzers, and the industrial advantage is very large.
しかしながら、本発明者らの検討によれば、前記したフ
ィンガ一槽におけるフィンが一陰極にアスベスト隔膜に
代えて陽イオン交換膜を装着して塩化アルカリの電解を
行なったところ、以下に述べる如きいくつかの問題点に
遭遇した。However, according to the studies conducted by the present inventors, when electrolyzing alkali chloride was carried out by attaching a cation exchange membrane to the cathode in place of the asbestos diaphragm to one of the fins in the single finger tank described above, the following results were obtained. I encountered a problem.
即ち、賜イオン交換膜の使用にもかかわらず、電槽電圧
が非常に高く、シたがって陰極室より得られる苛性アル
カリの電流効率が極めて低い。That is, despite the use of an ion exchange membrane, the cell voltage is very high, and therefore the current efficiency of the caustic alkali obtained from the cathode chamber is extremely low.
本発明者らは、この問題点を解決すべく、鋭意検討した
結果、この問題の原因が陽極構造にあることが判明した
。っまシ、電解条件下において中空のフィンガー陽極は
液比重錘にょシ陽イオン交換膜を介して陰極室側よシ圧
力を受け、この圧力によシフィンガー陽給がへこみ、陽
蓚−陰極間距離が液を満たしていないときに比べ2〜3
倍に拡がシ、同時に狭くなった個々゛のフィンガー陽極
により形成される陽極室内への塩化アルカリの供給が不
充分になり、電解槽の陽極室内における塩化アルカリ濃
度の不均一を招き、この結果電槽電圧の上昇、および電
流効率の低下を引きおこしたことが判明した。The inventors of the present invention conducted extensive studies to solve this problem, and as a result, it became clear that the cause of this problem lies in the anode structure. Under electrolytic conditions, the hollow finger anode receives pressure from the cathode chamber side through the liquid specific gravity cation exchange membrane. The distance is 2-3 compared to when the liquid is not filled.
The supply of alkali chloride into the anode chamber formed by the individual finger anodes, which are doubled in size and narrowed at the same time, becomes insufficient, leading to uneven alkali chloride concentration in the anode chamber of the electrolytic cell. It was found that this caused an increase in battery voltage and a decrease in current efficiency.
本発明の目的は上記の問題点を解決し、電解時において
安定した狭い陽極−陰極間距離を維持し、1−1つ陽極
室内を均一な塩化アルカリ濃度に保つことができるフィ
ンガー陽極を提供することにあシ、L2かも該フィンガ
ー陽極は、既存のものに簡単な〔¥、 ;i’iを施し
て利用できるものである。An object of the present invention is to solve the above problems and provide a finger anode that can maintain a stable and narrow anode-cathode distance during electrolysis and maintain a uniform alkali chloride concentration in the anode chamber. In particular, the finger anode L2 can be used by adding a simple modification to an existing one.
即ち、第1市目の発明は前記目的を達成するフィンガー
陽枚の構成として、隔壁に接合された給tilt枠の一
端には陰極バンクスクリーンを介して水子1tllr面
がU字形をなす多数のフィンガー陰極の脚部を増刊け、
前記給電棒の他端には、給電体を介して同じく水平断面
がU字形をなす多数のフィンガー陽極の脚部を取付は−
、前記フィンガー陰極には陽イオン交換膜を装着してな
る複極式塩化アルカリ電解槽組立用ユニットにおいて、
前記フィンが一陽極はそのU字形のフィンガー内側に柱
状の陽極サポートを縦方向に取付は外圧に対して補強し
たことを特徴とするものである。That is, the first invention has a structure of a finger positive plate that achieves the above-mentioned object, and has a large number of U-shaped water droplets at one end of the feed tilt frame connected to the partition wall through a cathode bank screen. Add the foot part of the finger cathode,
At the other end of the power supply rod, legs of a number of finger anodes having a U-shaped horizontal section are attached via a power supply body.
, in a unit for assembling a bipolar alkali chloride electrolytic cell, in which the finger cathode is equipped with a cation exchange membrane,
The anode having one fin is characterized in that a columnar anode support is vertically attached inside the U-shaped finger to reinforce against external pressure.
また、第2番目の発明は、第1番目の発明に対しさらに
効果の著しいフィンガー陽極の構成として、隔壁に接合
された給電棒の一端には陰極パックスクリーンを介して
水平断面がU字形をなす多数のフィンガー陰極の脚部を
増刊け、前記給電体の他端には、給電体を介して同じく
水平断面がU字形をなす多数のフィンガー陽極の脚部を
増刊け、前記フィンガー陰極には陽イオン交換膜を装着
してなる複極式塩化アルカリ電解槽組立用ユニットにお
いて、前記フィンガーl5III$p、は、その先端部
を縦方向に切断して二枚の陽極板となしそれぞれの陽極
板を給電体に対する取付脚部から10〜5Qmmの位置
において外側方向に屈曲加工して拡III′iシ、次い
でフィンが一陽極の先端部と脚部との間の1個所又はv
J数個所においてピンチが200 mm以内となるよう
にフィンガー内側縦方向に中空状陽極ザ、I? )を増
刊け、前記二枚の一極板の先端同志を架橋板を介して固
定したことを特徴とするものである。In addition, the second invention has a finger anode structure that is even more effective than the first invention, and has a U-shaped horizontal section at one end of the power supply rod connected to the partition wall through a cathode pack screen. The legs of a large number of finger cathodes are added to the other end of the power supply body, and the leg parts of a large number of finger anodes whose horizontal cross section is U-shaped are added to the other end of the power supply body. In a bipolar alkaline chloride electrolyzer assembly unit equipped with an ion exchange membrane, the tip of the finger 15III$p is cut in the longitudinal direction to form two anode plates, each of which is made up of two anode plates. The fin is bent outward at a position 10 to 5 Qmm from the mounting leg to the power supply body to enlarge it, and then the fin is attached at one place between the tip of the anode and the leg or v
Hollow anodes are placed vertically inside the finger so that the pinch is within 200 mm at several points. ), and is characterized in that the tips of the two monopolar plates are fixed together via a bridging plate.
本発明の実施態様について説明すると、フィンガー陽極
は、エキスバンドメツシュに形成されたチタン板を水平
1す1面が【1字形をなすように屈曲形成され、その脚
部が給電体に溶接されている。この中空フィンガー閾極
の内1111に柱状の陽極サポーi・を縦方向に増刊け
るが、該陽極サポートはフィンガー1場給の先端部と給
電体に対する取付部とのいずノ1からも20 Q mr
B以内となるようにフィンガーの内側にr(y、伺けら
れる。捷た二つ以上の陽伊サポートを取りイー]ける場
合は、隣シ合う陽極サポート間が2(JOmm以内とな
るようにフィンガー陽極内に取シ伺ける。To explain the embodiment of the present invention, the finger anode is formed by bending a titanium plate formed on an expanded mesh so that each horizontal side forms a ``1'' shape, and the legs of the finger anode are welded to the power supply body. ing. A column-shaped anode support i is added vertically to 1111 of this hollow finger threshold electrode, and the anode support is attached to both the tip of the finger 1 and the attachment part to the power supply body. mr
When inserting r (y, can be removed. Take two or more separated anode supports) on the inside of the finger so that the distance between adjacent anode supports is within 2 (JOmm), It can be seen inside the finger anode.
木兄町名らの検討によれば、フィンガー陽極の/l−A
l11 +’llr JT−+−2+’仏曙t/J−+
−x4qc八立:++ ハr−I−1t”、y 酬 し
m烙すポートとの距離が200咽以内であれば、陰極
室側からの圧力に対しても陽極板のへこみは1.0調以
内に押える゛ことが可能となる。According to the study by Kinoe Machina et al., the /l-A of the finger anode
l11 +'llr JT-+-2+'Buddha Dawn t/J-+
-x4qc eight points: ++ Har-I-1t", y return If the distance to the m heating port is within 200mm, the dent in the anode plate will be 1.0 even against the pressure from the cathode chamber side. It becomes possible to press within the key.
この陽極すp )によって、陽イオン交換膜を介して陰
極室側からの圧力によってフィンガー陽極が内側にへこ
み、電槽電圧が上昇したり、塩化アルカリの供給量不足
という問題が回避され、低い電槽電圧、且つ高い電流効
率で運転すること〃二可能となる。This anode (sp) avoids problems such as the finger anode being dented inward by the pressure from the cathode chamber side through the cation exchange membrane, increasing the battery cell voltage, and insufficient supply of alkali chloride, and causing a low battery voltage. It becomes possible to operate at high cell voltage and high current efficiency.
取付けられる陽極す7+?−トは角柱、多孔板、および
・ぞイブなどの中空体のものでも本発明の目的は達成さ
れるが、−中でも第3〜5図に示す断面形状が円形、髪
型、および変形四角形を例とした中空の柱状物がlhに
好ましい。Anode installed 7+? -The object of the present invention can be achieved even if the object is a hollow body such as a prism, a perforated plate, or an eclipse. A hollow columnar object with a diameter of 100 mm is preferable for lh.
このパイプの場合、フィンガー陽極への取付けにあたっ
ては面接合よりも点接合になるように、例えばスポット
溶接やTIG溶接によ多接合することが望ましい。In the case of this pipe, when attaching it to the finger anode, it is preferable to perform multiple joints by, for example, spot welding or TIG welding so that it is a point joint rather than a surface joint.
陽極サポートを中空体にすることによシ、フィンガー陽
極内の電解液の循環を促すダウンカマーとしての働きを
もたすことができ、電解槽内の塩化アルカ961隻度の
均一化に役立ち、高い電流効率での運転が容易となる。By making the anode support hollow, it can function as a downcomer that promotes the circulation of the electrolyte within the finger anode, helping to equalize the alkali chloride concentration within the electrolytic cell. Operation with high current efficiency becomes easy.
このとき、電解液の下向流を促し、ダウンカマーとして
の働きを一層発揮さ−FLるプこめに、190イ令ザポ
ート中空簡の内面は陽極7占1(1物り勺がイ1υ4′
4色されていないことが好ましい。At this time, it promotes the downward flow of the electrolyte and further exerts its function as a downcomer.
It is preferable that there are no four colors.
又、It?94に+iとの距rp;Iaを狭くする目的
でフィンガート(1枦lの先3″りhlを切断し、該1
電極フインガーの付は根部のD Vli:体との接合部
から10〜5otmnの位置までのフィンガー194極
を外側方向、即ち陰極側へ拡巾1“14シ、そして賜椅
サポートを切断した2枚の陽極板間に数個ける場合、極
めて精度よく陰極との距ばも保つことがI」能となシ、
更に電槽電圧の低下が達成出来るので好ましい。Also, It? In order to narrow the distance rp;
The electrode finger is attached to the root D Vli: The finger 194 pole from the junction with the body to the position 10 to 5 otmn is expanded outward, that is, toward the cathode side, and the width is 1"14, and the support is cut into two pieces. When several anodes are placed between the anode plates, it is impossible to maintain the distance to the cathode with extreme precision.
Furthermore, it is preferable because the battery voltage can be reduced.
次に、既イrのフィンガー陽極を改造して得た本発明に
よるフィンガー陽極について図面をもとに説明する。Next, a finger anode according to the present invention obtained by modifying an existing finger anode will be described with reference to the drawings.
第1図は、既看の複極式隔膜法電解槽を水平に切断し上
部よシ眺めた一部断面図である。第2図は、多数数句け
られているフィンガー陽極の1つを示す斜視図である。FIG. 1 is a partial sectional view of a conventional bipolar diaphragm electrolytic cell taken horizontally and viewed from above. FIG. 2 is a perspective view of one of the many finger anodes.
陽極室側内面にチタンでライニングされた軟鋼からなる
隔壁1に接合−された給電棒2に給電体3が溶接され、
該給電体3に陽極活性物質を被鞄したチタン製のエキス
バンドメタルをU字型に加工したフィンガー状の陽極4
の脚部が溶接されている。一方陰極側においては隔壁1
とは間隔をおいて陰極バックスクリーン5そして該バッ
クスクリーン5を通した給電棒2に、軟鋼製のワイヤー
を織った網を袋状に加工したフィンガー陰極6が溶接さ
れている。A power supply body 3 is welded to a power supply rod 2 which is joined to a partition wall 1 made of mild steel whose inner surface on the side of the anode chamber is lined with titanium.
The power supply body 3 is provided with a finger-shaped anode 4 made of titanium expanded metal coated with an anode active material and processed into a U-shape.
The legs are welded. On the other hand, on the cathode side, the partition wall 1
A finger cathode 6 made of a net made of woven mild steel wire is welded to the cathode back screen 5 and the power supply rod 2 passing through the back screen 5 at a distance from the finger cathode 6 .
通常、アスベストを隔膜として用いる隔膜法においては
該袋状のフィンガー陰極6の上にアスベストスラリーを
デデジットさせ形成させたアスベスト隔膜が被覆されて
いる。Usually, in the diaphragm method using asbestos as a diaphragm, the bag-shaped finger cathode 6 is covered with an asbestos diaphragm formed by digitizing asbestos slurry.
第3図は、第1図、第2図に示すU字型のフィンガー陽
極を本発明によシ改造した陽極の例を示す断面図であシ
、第4図はその斜視図である。FIG. 3 is a sectional view showing an example of an anode obtained by modifying the U-shaped finger anode shown in FIGS. 1 and 2 according to the present invention, and FIG. 4 is a perspective view thereof.
本発明において先ず、フィンガー陽極の先端部7を機械
的切断法、又はガス溶断法等の公知の手法にて切断する
。次に第3図に示す如き切断したフィンガー陽極の同極
板4を、給電体3との接合部8よシ10〜50叫の位動
゛9で外側方向に屈曲加工して向い合っている二枚の同
極板を対座するフィンガー陰伜との間隔が隔膜として陽
イオン交換膜を用いる場合の適切な所定帥囲内になるよ
うに拡幅する。次いで、先端部で切11yiされ拡幅加
工された二枚の陽極板4,4の内側に陽極サポート10
を数個ける。該陽極サポート10は、陽極板4の縦方向
の全長とほぼ同じ長さを有し、陽極板と点又は線接触す
るように、例えばスポット溶接やTIG活接取伺数個れ
る。In the present invention, first, the tip portion 7 of the finger anode is cut by a known method such as a mechanical cutting method or a gas cutting method. Next, the homopolar plate 4 of the cut finger anode as shown in FIG. The width of the two homopolar plates is widened so that the distance between the opposing finger holes falls within an appropriate predetermined range when a cation exchange membrane is used as a diaphragm. Next, an anode support 10 is placed inside the two anode plates 4, which have been cut 11yi at the tip and widened.
Take a few. The anode support 10 has approximately the same length as the entire length of the anode plate 4 in the vertical direction, and has several points or lines of contact with the anode plate, for example, by spot welding or TIG welding.
11’、3極ザポート10は液の循環を促すために、第
3〜6図に例を示すような中空の筒状体のものを取イ・
目することが効−ましく、又材質としては陽極室生成物
′JI[に1lul性を有するものであれば何れのもの
も(+lj用できる。加工性、数個は易さから陽極基材
と同じチタンが中でも好ましい。11', The three-pole Zaport 10 is a hollow cylindrical body as shown in Figs. 3 to 6 in order to promote the circulation of the liquid.
In addition, any material can be used as long as it has a 1 lul property for the anode chamber product. Among these, titanium, which is the same as , is preferred.
このj)4合、中竪のが)の内面は陽極活性物質が被覆
されていないことが望ましい。筒内側に泡の発生がなく
ダウンカマーの働きが一層発揮されるからである。It is desirable that the inner surface of this j) 4-way, middle vertical part) is not coated with an anode active material. This is because no bubbles are generated on the inside of the cylinder, and the downcomer functions more effectively.
陽極板4の内側に取付けられる陽極サポート10は、陰
極室側からの圧力によるへこみを防ぐために、フィンガ
ー陽極の先端部7及び給電体との接合部8のいづれから
も200咽以内となるように陽極板の内側に少くとも1
つ以上取付けられる。The anode support 10 attached to the inside of the anode plate 4 is placed within 200 mm from both the tip 7 of the finger anode and the joint 8 with the power supply body in order to prevent denting due to pressure from the cathode chamber side. At least 1 on the inside of the anode plate
More than one can be installed.
フィンガー陽極の先端部7と給電体との接合部8との距
離が400調以内であればフィンガー陽極の長さの半分
にあたる個所に陽極サポート10を取シ付けることが好
ましい。又2つ以上取付ける場合はフィンガー陽極の長
さを等分するような位置にそれぞれ取付けることが好ま
しい。If the distance between the tip 7 of the finger anode and the joint 8 with the power supply body is within 400 degrees, it is preferable to attach the anode support 10 at a location corresponding to half the length of the finger anode. When two or more finger anodes are attached, it is preferable to attach them at positions that equally divide the length of the finger anodes.
そして最后に、先端部7を切断した対向する陽極板4.
4の先端部同志を架橋板11を介して所定の間隔を保っ
て固定して陰極室側からの圧力に而4えるようにする。Finally, the opposing anode plate 4 with the tip 7 cut off.
The tips of the cathode chambers 4 are fixed at a predetermined distance through a bridging plate 11 so that pressure from the cathode chamber side can be applied.
該架橋板11は、多孔板でも平板でも特に限定されず、
又陽極と同一仕様の陽極活性被覆されたチタンエキツノ
9ンドメタルを加工したものでもよい。又この部分は電
流?し【度が小さいので金属でなく、耐塩素性を有した
樹脂を成型した枠秋物でもよい。賜イメン交換lx t
2を前もってフィンガーIQ 4/li 6に4追い
、該フィンガー状陽極と電解槽を組み立てる場合に幀:
、架橋板として、あらかじめ平m面仕土けした金の五プ
レートや、テフロンなどのプラスチック製の枠秋物を用
いると、賜イオン交拉!1j・:へを全く傷つけること
なく化1’l’r漕を組み立てることが出来るので好ま
しい。The bridge plate 11 is not particularly limited to a perforated plate or a flat plate,
Alternatively, it may be made of titanium exotic metal coated with anode active coating and having the same specifications as the anode. Also, is this part a current? [Because of its low strength, a frame made of chlorine-resistant resin may be used instead of metal. Gift exchange lxt
2 to the finger IQ 4/li 6 in advance and when assembling the finger-shaped anode and the electrolytic cell:
If you use a pre-plated gold plate or a frame made of Teflon or other plastic as a bridging board, you will be able to exchange ions! This is preferable because the chemical 1'l'r column can be assembled without damaging the 1j.:.
このようにして改造された陽′4f、構造をもつ複極式
隔膜法′眠#(tt’Vを用いて陽イオン交換膜を用い
て塩化アルカリをtt解するとき、19歩イオン交換を
介した陽極と陰極との距離をこれまでのアスベスト■、
つ膜を用いたときに比べても一段と狭く又、フィンが−
の付は根部間における極間距離も均一にすることが出来
、低い’tB 4Vi電圧が達成される。又、更にフィ
ンガー陽極内に数句けられた陽極サポートし11、陽イ
オン交換膜を介した陰極室側からの圧力によるフィンガ
ー陽極のへこみを防ぎ、所定の41シ(間距離を保つ役
目を果すと共に、陽極サポートを中空体とすることによ
ってフィンガー陽極内の電解液の循環を促すダウンカマ
ーの働きをするのて電解槽陽極室内の塩化アルカリ濃度
の均一化に役立ち、高い電流効率での運転が可能となる
。When alkali chloride is decomposed using a cation exchange membrane using a bipolar diaphragm method (tt'V) having the structure modified in this way, 19 steps are carried out through ion exchange. The distance between the anode and cathode was
It is much narrower than when using a membrane, and the fins are
The distance between the poles between the roots can also be made uniform, and a low 'tB 4Vi voltage can be achieved. In addition, several anode supports 11 are placed inside the finger anodes to prevent the finger anodes from being dented due to pressure from the cathode chamber side through the cation exchange membrane, and to maintain a predetermined distance of 41 cm. At the same time, by making the anode support hollow, it acts as a downcomer that promotes the circulation of the electrolyte in the finger anode, which helps to equalize the alkali chloride concentration in the anode chamber of the electrolytic cell, and allows operation with high current efficiency. It becomes possible.
実施例
フィンガー状陽極の側面の大きさが高さ1220鯛、長
さ335關、断面がU字型の酸化ルテニウムを被覆した
1/2インチメツシュのチタンエキス・ぐンドメタルか
らなるフィンガー状陽極の先端部をガス溶断機で切断し
、給電体に溶接している陽極板の接合部から25咽の位
置を外側方向にhJi曲加工した。そして断面の大きさ
が長さ335 mm 。Example Finger-shaped anode The tip of a finger-shaped anode made of 1/2-inch mesh titanium extract gundo metal coated with ruthenium oxide and has a U-shaped cross section with a side surface size of 1220 mm in height and 335 mm in length. was cut using a gas cutting machine, and a hJi curve was formed outward at a position 25 mm away from the joint of the anode plate welded to the power supply body. The cross-sectional size is 335 mm long.
先端部の幅が16咽、付は根部が25咽のU字型の袋状
のフィンガー陰極との距離が2.5Mになる様に、陽極
板間隔を拡幅した。そしてこの陽極板の中央部内側の所
に長さ1220 mm l内径28 mm 。The distance between the anode plates was widened so that the distance to the U-shaped bag-shaped finger cathode, which had a width of 16 mm at the tip and a width of 25 mm at the base, was 2.5 M. The inside of the central part of this anode plate has a length of 1220 mm and an inner diameter of 28 mm.
外径31簡のチタン製の〕ぐイブをTIG溶接によシ点
付けし、次に切断した2枚の陽極板の先端部同志を、厚
み1.5mの表面をあらかじめ平滑仕上けしだチタンプ
レートを曲げ加工して製作した長さ1220 mmの架
橋板を介してTIG溶接にて固定した。A titanium tube with an outer diameter of 31 mm was attached by TIG welding, and then the tips of the two cut anode plates were attached to a titanium plate with a thickness of 1.5 m and the surface smoothed in advance. They were fixed by TIG welding via a bridge plate with a length of 1220 mm that was manufactured by bending.
このように改造された陽極を有する、44のフィンガー
陰′柾を備えた複極式隔膜法電解槽にカル21−ン酸基
を有する陽イオン交換膜を装着して食塩水の箱5角′r
を行なった。A bipolar diaphragm electrolytic cell with 44 finger cathodes and a modified anode as described above was equipped with a cation exchange membrane having a carboxyl acid group, and a 5-square box of saline solution was added. r
I did this.
世;イオン交倹trqは前もって袋状に成形加工し、袋
状フィンガー陰極にかぶせ、陰極室を一5011111
+1120減圧[7た状態で、賜榛ネ枠に陰極室枠を組
み入第1た。そして次の条件にて食塩水の電解を行なつ
プこ。World: The ion exchanger trq is formed into a bag shape in advance, and is placed over the bag-shaped finger cathode to form a cathode chamber.
At a vacuum of +1,120°C, the cathode chamber frame was assembled into the frame. Then, electrolysis of saline water is carried out under the following conditions.
1L37 カ(t; ; 72kA
温度 ; 90 C
出口1”ηf1ソーダi!53度 ; 32W%出[1
地水41度 : 200ft
この結果、電摺電圧は3.37.fルトで長期間安定し
ていた。又、陰極室側から得られる苛性ンーグの電5+
t、効率も95.5%と安定していた。1L37 force (t; ; 72kA Temperature; 90C Outlet 1"ηf1 soda i! 53 degrees; 32W% output [1
Ground water: 41 degrees: 200ft As a result, the electrical voltage is 3.37. It was stable for a long time at f-rut. In addition, the caustic acid 5+ obtained from the cathode chamber side
The efficiency was also stable at 95.5%.
比較例
1県柘/7″1〜婚を行りもhrN版実施例と全く同様
な方法にて食塩水の電解を行なった。Comparative Example 1 Prefecture / 7'' 1 ~ 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 2000 x 100 x 100 x 100 x 100 x 100 x 200 x 100 x 200 for hrN Version
その結果、電摺電圧は運転開始后よシ徐々に上昇がみら
れ安定した電摺電圧は3.63zルトでありた。又陰極
室側からの苛性ソーダの電流効率も92.5%と低く陽
極室から得られる塩素中の酸素の濃度も実施例に比べI
Vol ’%以上高い値を示した。As a result, the electric wire voltage gradually increased after the start of operation, and the electric wire voltage stabilized at 3.63 z. In addition, the current efficiency of caustic soda from the cathode chamber side is as low as 92.5%, and the concentration of oxygen in chlorine obtained from the anode chamber is also lower than in the example.
It showed a value higher than Vol'%.
第1図は、既存の複極式隔膜法電解槽の断面説明図であ
る。第2図は、既存の陽極構造体の斜視説明図である。
第3図は、本発明によるフィンガー陽極の断面説明図で
ある。第4図は、同フィンガー陽極斜視説明図である。
第5図は、本発明における陽極す4?−トの例を示す断
面説明図である。第6図は、本発明の陽イオン交換膜を
セットした複極式隔膜法電解槽の断面説明図である。
1:隔壁 2:給電棒
3:給電体 4:陽極
5:陰極バックスクリーン
6:フインガニ陰極
7:フィンガー陽極先端部
8:陽極の端部であって給電体との接合部9:陽極板拡
幅部 lO:陽極サポート11:架橋板 12:陽イオ
ン交換膜。
I 第1図
イi> 2目
第3図
て1゛j 4 図
−イFIG. 1 is an explanatory cross-sectional view of an existing bipolar diaphragm electrolytic cell. FIG. 2 is a perspective explanatory view of an existing anode structure. FIG. 3 is a cross-sectional explanatory diagram of a finger anode according to the present invention. FIG. 4 is a perspective explanatory view of the finger anode. FIG. 5 shows the anode 4 in the present invention. - FIG. FIG. 6 is an explanatory cross-sectional view of a bipolar diaphragm electrolytic cell in which the cation exchange membrane of the present invention is set. 1: Partition wall 2: Power supply rod 3: Power supply body 4: Anode 5: Cathode back screen 6: Fingani cathode 7: Finger anode tip 8: Anode end and joint with power supply body 9: Anode plate widened part lO: Anode support 11: Crosslinked plate 12: Cation exchange membrane. I Figure 1 Ii> 2nd Figure 3 1゛j 4 Figure-A
Claims (1)
クリーンを介して水平断面がU字形をなす多計のフィン
ガー陰極の脚部を取付け、前記給電棒の他端には、給電
体を介して同じく水平断面がU字形をなす多数のフィン
ガー陽極の脚部を取付け、前記フィンガー陰極には1形
イオン交換膜を装着してなる抜極式監、(化アルカリ電
解槽組立用ユニットにおいて、前記フィンガーIt!
極はそのU字形のフィンガー内側に柱状の陽極す号?−
トを縦方向に数句は外圧に対して補強した仁とを特徴と
するフィンガー陽極。 2 前記1Xり極サポートはフィンガー陽極の先端部と
脚部との間の1個所又は複数個所に取付けられ、ピッチ
が200 m18以内と々るようにしたことを特徴とす
る特許請求の範囲第1項に記載のフィンガー陽極。 4、前記中空体陽極サポートの中空内面が陽極活性を有
しない劇壇素性物質で構成されている特許請求の範囲第
3項に記載のフィンガー陽極。 5、前記フィンガー陽極は、給電体に対する取付脚部か
ら10〜50fiの位置において外側方向に拡幅されて
いることを特徴とする特許請求の範囲第1.2.3また
は4項に記載のフィンガー陽極。 6、 隔壁に接合された給電棒の一端には陰極パックス
クリーンを介して水平断面がU字形をなす多数のフィン
が一陰極の脚部を取付け、前記給電棒の他端には、給電
体を介して同じく水平断面がU字形をなす多数のフィン
ガー陽極の脚部を取イ」け、前記フィンガー陰極には陽
イオン交換膜を装着してなる複極式塩化アルカリ電解槽
組立用ユニットにおいて、前記フィンガー陽極は、その
先端部を縦方向に切断して二枚の陽極板となし、それぞ
れの陽極板を給電体に対する取付脚部から10〜59m
mの位置において外側方向に屈曲加工して拡幅し、次い
でフィンガー陽極の先端部と脚部との間の1個所又は複
数個所においてピッチが200門以内となるようにフィ
ンガー内側縦方向に中空状陽極サポートを取付け、前記
二枚の陽極板の先端同志を架4jj!l板を介して固定
したことを特徴とするフィンガー陽極。 7、 前記中空状陽極サポートの中空内面が陽極活性を
有しない耐塩素性物ηで構成されている特許請求の範囲
第6項記載のフィンガー陽極。[Claims] 1. A multi-finger cathode leg portion having a U-shaped horizontal cross section is attached to one end of the power feeder joined to the partition wall through a cathode pack screen, and the legs of a multi-finger cathode having a U-shaped horizontal section are attached to the other end of the power feed rod. This is a detachable type electrode control system, in which the legs of a number of finger anodes, each of which has a U-shaped horizontal cross section, are attached via a power supply body, and a type 1 ion exchange membrane is attached to the finger cathodes. In the assembly unit, the finger It!
The pole is a columnar anode inside the U-shaped finger. −
This finger anode is characterized by several lengthwise edges that are reinforced against external pressure. 2. Claim 1, characterized in that the 1X electrode support is attached at one or more locations between the tip and leg of the finger anode, and the pitch is within 200 m18. Finger anodes as described in Section. 4. The finger anode according to claim 3, wherein the hollow inner surface of the hollow anode support is made of a material having no anode activity. 5. The finger anode according to claim 1.2.3 or 4, wherein the finger anode is widened outward at a position 10 to 50 fi from the mounting leg for the power supply body. . 6. At one end of the power supply rod connected to the bulkhead, a large number of fins with a U-shaped horizontal section are attached to one cathode leg through a cathode pack screen, and at the other end of the power supply rod, a power supply body is attached. In the unit for assembling a bipolar alkali chloride electrolytic cell, the leg portions of a number of finger anodes having a U-shaped horizontal cross section are taken through the same, and a cation exchange membrane is attached to the finger cathodes. The tip of the finger anode is cut vertically to form two anode plates, and each anode plate is separated from the mounting leg to the power supply body by 10 to 59 m.
The width of the anode is expanded by bending it outward at the position m, and then a hollow anode is formed in the longitudinal direction inside the finger so that the pitch is within 200 at one or more places between the tip and the leg of the finger anode. Attach the support and place the tips of the two anode plates together! A finger anode characterized in that it is fixed through an l plate. 7. The finger anode according to claim 6, wherein the hollow inner surface of the hollow anode support is made of a chlorine-resistant material η having no anode activity.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58216613A JPS60110890A (en) | 1983-11-17 | 1983-11-17 | Finger anode in bipolar alkaline chloride electrolyzer assembly unit |
IT23625/84A IT1177236B (en) | 1983-11-17 | 1984-11-16 | PROCEDURE FOR PRODUCING CAUSTIC ALKALINE AGENTS |
US06/673,122 US4622113A (en) | 1983-11-17 | 1984-11-19 | Process for producing caustic alkalis |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58216613A JPS60110890A (en) | 1983-11-17 | 1983-11-17 | Finger anode in bipolar alkaline chloride electrolyzer assembly unit |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60110890A true JPS60110890A (en) | 1985-06-17 |
JPH0335389B2 JPH0335389B2 (en) | 1991-05-28 |
Family
ID=16691167
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58216613A Granted JPS60110890A (en) | 1983-11-17 | 1983-11-17 | Finger anode in bipolar alkaline chloride electrolyzer assembly unit |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60110890A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012241206A (en) * | 2011-05-16 | 2012-12-10 | Kobe Steel Ltd | Ozone generating device |
CN103046071A (en) * | 2012-12-13 | 2013-04-17 | 苏州新区化工节能设备厂 | Ion membrane electrolysis unit tank |
JP2020097770A (en) * | 2018-12-18 | 2020-06-25 | マクセルホールディングス株式会社 | Folded electrode, parallel electrode plate structure using the folded electrode, and stacked electrode pair |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5713186A (en) * | 1980-06-26 | 1982-01-23 | Permelec Electrode Ltd | Method for modification of metallic electrode for electrolysis |
-
1983
- 1983-11-17 JP JP58216613A patent/JPS60110890A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5713186A (en) * | 1980-06-26 | 1982-01-23 | Permelec Electrode Ltd | Method for modification of metallic electrode for electrolysis |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2012241206A (en) * | 2011-05-16 | 2012-12-10 | Kobe Steel Ltd | Ozone generating device |
CN103046071A (en) * | 2012-12-13 | 2013-04-17 | 苏州新区化工节能设备厂 | Ion membrane electrolysis unit tank |
CN103046071B (en) * | 2012-12-13 | 2015-02-18 | 苏州市启扬商贸有限公司 | Ion membrane electrolysis unit tank |
JP2020097770A (en) * | 2018-12-18 | 2020-06-25 | マクセルホールディングス株式会社 | Folded electrode, parallel electrode plate structure using the folded electrode, and stacked electrode pair |
Also Published As
Publication number | Publication date |
---|---|
JPH0335389B2 (en) | 1991-05-28 |
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