JP2000282282A - Electrolytic tank - Google Patents

Electrolytic tank

Info

Publication number
JP2000282282A
JP2000282282A JP11093589A JP9358999A JP2000282282A JP 2000282282 A JP2000282282 A JP 2000282282A JP 11093589 A JP11093589 A JP 11093589A JP 9358999 A JP9358999 A JP 9358999A JP 2000282282 A JP2000282282 A JP 2000282282A
Authority
JP
Japan
Prior art keywords
chamber
caustic
cathode
electrolytic cell
diffusion electrode
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
Application number
JP11093589A
Other languages
Japanese (ja)
Other versions
JP3041793B1 (en
Inventor
Akihiro Sakata
昭博 坂田
Koji Saiki
幸治 斉木
Hiroaki Aikawa
洋明 相川
Shinji Katayama
真二 片山
Kenzo Yamaguchi
健三 山口
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 Chemicals Inc
Toagosei Co Ltd
Kanegafuchi Chemical Industry Co Ltd
ThyssenKrupp Uhde Chlorine Engineers Japan Ltd
Original Assignee
Chlorine Engineers Corp Ltd
Mitsui Chemicals Inc
Toagosei Co Ltd
Kanegafuchi Chemical Industry 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 Chlorine Engineers Corp Ltd, Mitsui Chemicals Inc, Toagosei Co Ltd, Kanegafuchi Chemical Industry Co Ltd filed Critical Chlorine Engineers Corp Ltd
Priority to JP11093589A priority Critical patent/JP3041793B1/en
Priority to US09/701,418 priority patent/US6383349B1/en
Priority to CNB008004536A priority patent/CN1163634C/en
Priority to EP00911433A priority patent/EP1092789B1/en
Priority to PCT/JP2000/001921 priority patent/WO2000060140A1/en
Application granted granted Critical
Publication of JP3041793B1 publication Critical patent/JP3041793B1/en
Publication of JP2000282282A publication Critical patent/JP2000282282A/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Electrodes For Compound Or Non-Metal Manufacture (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an electrolytic tank using a gas diffusion electrode, and capable of completely preventing the leakage of a caustic solution using a chamber simple in structure, and easy in corrosion resistant metal plating. SOLUTION: In the electrolytic tank, an upper chamber 17 as a caustic solution outlet, and a lower chamber 16 as a caustic solution inlet are provided through caustic solution passages 12, 13 with a spacer therein on an outer end of an electrolytic tank comprising a gas chamber 8 having oxygen gas inlet and outlets 6, 7 for a gas diffusion electrode 9 in contact with oxygen gas inlet and outlets 4, 5 of upper and lower chambers provided on the center side along a surface of a cathode collector frame 3 adjacent to a cathode element 1, and a cathode chamber 11 filled with the caustic solution between the gas diffusion electrode 9 and an ion-exchange membrane 10.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、イオン交換膜法食
塩電解等に使用される酸素陰極を用いた電解槽に関し、
更に詳しくは、苛性液の供給、排出を有効に行う電解槽
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolytic cell using an oxygen cathode used for ion exchange membrane method salt electrolysis and the like.
More particularly, it relates to an electrolytic cell for effectively supplying and discharging a caustic liquid.

【0002】[0002]

【従来の技術】従来のガス拡散電極を用いる電解槽にお
いては、陰極エレメント、陰極集電枠、苛性室枠などで
構成され、これらはガスケットを間に挟んで組み立てら
れており、苛性液は陰極エレメント内に設けられた苛性
チャンバーの液出入口から供給、排出されている。しか
も、この電解槽はガスケットを必要とするものであっ
た。
2. Description of the Related Art A conventional electrolytic cell using a gas diffusion electrode is composed of a cathode element, a cathode current collecting frame, a caustic chamber frame, and the like, which are assembled with a gasket interposed therebetween. It is supplied and discharged from the liquid inlet and outlet of a caustic chamber provided in the element. Moreover, this electrolytic cell required a gasket.

【0003】[0003]

【発明が解決しようとする課題】このため、この電解槽
は構造が複雑で、各部材の接合部、例えば、ガスケット
のシール性の低下により苛性液の液漏れが生じる可能性
が大きいという問題があった。また、陰極エレメントの
苛性チャンバーが電食を生じる可能性があるが、この場
合、前記苛性チャンバーの防食のために、銀などのNa
OHに対し防食性を有する金属によるメッキ施工も構造
上困難であるという問題点もあった。
For this reason, this electrolytic cell has a complicated structure, and there is a problem that leakage of caustic liquid is likely to occur due to a decrease in the sealability of a joint portion of each member, for example, a gasket. there were. Also, the caustic chamber of the cathode element may cause electrolytic corrosion. In this case, in order to prevent corrosion of the caustic chamber, Na such as silver is used.
There is also a problem that plating with a metal having corrosion resistance to OH is structurally difficult.

【0004】本発明は、このような従来の課題に鑑みて
なされたものであり、構造が簡単で、従来の電解槽をそ
のまま用いることができ、防食金属メッキ施工が容易に
行えるチャンバーを使用して、苛性液の漏れ防止を完全
に行える、ガス拡散電極を用いる電解槽を提供すること
を目的とする。
The present invention has been made in view of such conventional problems, and uses a chamber which has a simple structure, can use a conventional electrolytic cell as it is, and can easily perform anticorrosion metal plating. It is another object of the present invention to provide an electrolytic cell using a gas diffusion electrode that can completely prevent leakage of caustic liquid.

【0005】[0005]

【課題を解決するための手段】本発明によれば、下記の
電解槽が提供されて、本発明の上記目的が達成される。 (1)陽極、イオン交換膜及びガス拡散電極よりなる酸
素陰極を用いる電解槽において、陰極エレメントに隣接
して陰極集電枠の面に沿って中央側に設けた上下部チャ
ンバーの酸素ガス出入口に接してガス拡散電極の酸素ガ
ス出入口を有するガス室、ガス拡散電極とイオン交換膜
の間に苛性液が入る陰極室から構成される電解槽の外側
端部に、苛性液排出口として上部チャンバーを、苛性液
導入口として下部チャンバーを、苛性液通路を介して接
続する苛性室枠を設けたことを特徴とする電解槽。 (2)各チャンバーからの苛性液通路は、狭い間隔を有
する平行な板材の間に形成され、苛性液の分散の均一化
及び強度の確保のために間隔10〜100mmにスペー
サーが設けられていることを特徴とする前記(1)記載
の電解槽。
According to the present invention, the following electrolytic cell is provided to achieve the above object of the present invention. (1) In an electrolytic cell using an oxygen cathode composed of an anode, an ion exchange membrane, and a gas diffusion electrode, an oxygen gas inlet / outlet of an upper / lower chamber provided at the center side along the surface of the cathode current collecting frame adjacent to the cathode element. An upper chamber as a caustic liquid outlet is provided at the outer end of an electrolytic cell comprising a gas chamber having an oxygen gas inlet / outlet of a gas diffusion electrode and a cathode chamber in which a caustic liquid enters between the gas diffusion electrode and the ion exchange membrane. An electrolytic cell provided with a caustic chamber frame connecting a lower chamber as a caustic liquid inlet through a caustic liquid passage. (2) The caustic liquid passage from each chamber is formed between parallel plate members having a narrow space, and spacers are provided at a distance of 10 to 100 mm for uniform distribution of the caustic liquid and for securing strength. The electrolytic cell according to (1), wherein:

【0006】[0006]

【発明の実施の形態】以下、本発明について単極式電解
槽に実施した形態を図面に基づいて説明するが、本発明
はこれに限定されず、複極式電解槽にも応用できる。図
1は、本発明の一実施態様を示す断面図である。電解槽
の陰極エレメント1に隣接して陰極集電枠3の面に沿っ
て中央部側に上部ガスチャンバーの酸素ガス入口4と下
部チャンバーの酸素ガス出口5が設けられている。この
酸素入口及び出口に接して酸素ガス入口4及び出口5を
有する陰極集電枠3とガス拡散電極9の間にコルゲート
メッシュを充填したガス室8と、ガス拡散電極9とイオ
ン交換膜10とで苛性液が入る陰極室11を構成する。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described with reference to the drawings in which a preferred embodiment of the present invention is applied to a monopolar electrolytic cell. However, the present invention is not limited to this and can be applied to a bipolar electrolytic cell. FIG. 1 is a sectional view showing an embodiment of the present invention. An oxygen gas inlet 4 for the upper gas chamber and an oxygen gas outlet 5 for the lower chamber are provided at the center along the surface of the cathode current collecting frame 3 adjacent to the cathode element 1 of the electrolytic cell. A gas chamber 8 filled with a corrugated mesh between a cathode current collector frame 3 having an oxygen gas inlet 4 and an outlet 5 in contact with the oxygen inlet and outlet and a gas diffusion electrode 9; a gas diffusion electrode 9 and an ion exchange membrane 10; Constitutes the cathode chamber 11 into which the caustic liquid enters.

【0007】前記陰極集電枠3と陰極エレメント1との
間には、苛性液や酸素ガス防止用のガスケットを嵌挿し
てシールする構成になっている。このシール用のガスケ
ットとしては、耐アルカリ性のガスケットであれば特に
制限されることなく使用でき、例えば、合成ゴム、プラ
スチック等が好ましく使用できる。
A gasket for preventing caustic liquid or oxygen gas is inserted between the cathode current collecting frame 3 and the cathode element 1 for sealing. The gasket for the seal can be used without any particular limitation as long as it is an alkali-resistant gasket. For example, synthetic rubber, plastic, and the like can be preferably used.

【0008】一方、このように構成された電解槽の陰極
部の外側端部に、苛性液排出口として上部チャンバー1
7を、苛性液導入口として下部チャンバー16を、それ
ぞれ苛性液通路13及び12を経て陰極室11の上下端
部から離して配設する。各苛性液通路12及び13は、
狭い陰極室を構成できるように狭い間隔で平行に配置し
た枠板の上部枠部及び下部枠部で形成するのがよく、苛
性液の分散の均一化及び強度の確保を計る目的で、間隔
10〜100mmにスペーサーが配置されている。更
に、スペーサー型苛性液通路12及び13と陰極集電枠
3との間にはガスケット14を、イオン交換膜10との
間にはガスケット15を嵌挿して、苛性液濡れ防止用に
シールしている。なお、ガスケットの材料は、前記の耐
アルカリ性のガスケットを特に制限されることなく使用
できる。
On the other hand, at the outer end of the cathode portion of the electrolytic cell thus constructed, an upper chamber 1 is provided as a caustic liquid outlet.
The lower chamber 16 is disposed apart from the upper and lower ends of the cathode chamber 11 via the caustic liquid passages 13 and 12, respectively. Each of the caustic liquid passages 12 and 13
It is preferable to form the upper and lower frames of a frame plate arranged in parallel at a narrow interval so as to form a narrow cathode chamber. The interval 10 is used for the purpose of equalizing the dispersion of the caustic liquid and ensuring the strength. Spacers are arranged at 100100 mm. Further, a gasket 14 is inserted between the spacer-type caustic liquid passages 12 and 13 and the cathode current collecting frame 3, and a gasket 15 is inserted between the spacers and the ion exchange membrane 10, and sealed to prevent caustic liquid wetting. I have. In addition, as the material of the gasket, the above-described alkali-resistant gasket can be used without particular limitation.

【0009】陰極室11の上部チャンバー16、下部チ
ャンバー17は、あらかじめ苛性ソーダに対し防食性の
ある銀などの金属でメッキした金属板を、内面側になる
ように板金加工で形成しているので、容易に製作するこ
とができると共に、苛性液に対する耐食性が優れてお
り、上部、下部チャンバー16及び17は電食を起こす
可能性もなくなる。さらに、板金加工では、陰極室枠2
と一体として形成してもよい。
The upper chamber 16 and the lower chamber 17 of the cathode chamber 11 are made of a metal plate previously plated with a metal such as silver having corrosion resistance against caustic soda by sheet metal processing so as to face the inner side. It can be easily manufactured and has excellent corrosion resistance to caustic liquid, so that the upper and lower chambers 16 and 17 are not likely to cause electrolytic corrosion. Further, in sheet metal processing, the cathode chamber frame 2
And it may be formed integrally.

【0010】図1に示すように、本発明の実施態様で
は、電解液が下部から供給されて上部へ上昇する形式で
ある。すなわち、苛性液は、陰極室11の下部チャンバ
ー16から供給されて苛性液通路12から苛性室11に
入り、苛性室11中を上昇し、苛性液通路13を経て上
部チャンバー17より排出される。
As shown in FIG. 1, in the embodiment of the present invention, an electrolytic solution is supplied from a lower part and rises to an upper part. That is, the caustic liquid is supplied from the lower chamber 16 of the cathode chamber 11, enters the caustic chamber 11 from the caustic liquid passage 12, rises in the caustic chamber 11, and is discharged from the upper chamber 17 via the caustic liquid passage 13.

【0011】[0011]

【発明の効果】本発明の電解槽によれば、苛性液の漏れ
が防止できるばかりでなく、上部チャンバー、下部チャ
ンバーの防食メッキ施工が容易にできるため、苛性チャ
ンバーが電食を生じることもない。更に、陰極室と上部
チャンバー、下部チャンバーを連通する苛性液通路にス
ペーサーを配置することにより、苛性液の均一の配分及
び円滑な流通も可能になる。さらに、上部チャンバー、
下部チャンバーは電解槽の外側に設けるようにしたの
で、従来の電解槽の内部構造を変えることなく改造する
ことができる。
According to the electrolytic cell of the present invention, not only leakage of the caustic solution can be prevented, but also the anticorrosion plating of the upper chamber and the lower chamber can be easily performed, so that the electrolytic corrosion does not occur in the caustic chamber. . Further, by disposing the spacer in the caustic liquid passage communicating the cathode chamber with the upper chamber and the lower chamber, uniform distribution and smooth distribution of the caustic liquid can be achieved. In addition, the upper chamber,
Since the lower chamber is provided outside the electrolytic cell, it can be modified without changing the internal structure of the conventional electrolytic cell.

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

【図1】本発明のガス拡散電極を使用する電解槽の一例
を示す断面図である。
FIG. 1 is a sectional view showing an example of an electrolytic cell using a gas diffusion electrode of the present invention.

【符号の説明】[Explanation of symbols]

1 陰極エレメント 2 苛性室枠 3 陰極集電枠 4,6 酸素ガス入口 5,7 酸素ガス出口 8 ガス室 9 ガス拡散電極 10 イオン交換膜 11 陰極室 12,13 苛性液通路 14,15 ガスケット 16 下部チャンバー 17 上部チャンバー DESCRIPTION OF SYMBOLS 1 Cathode element 2 Caustic chamber frame 3 Cathode current collecting frame 4,6 Oxygen gas inlet 5,7 Oxygen gas outlet 8 Gas chamber 9 Gas diffusion electrode 10 Ion exchange membrane 11 Cathode chamber 12,13 Caustic liquid passage 14,15 Gasket 16 Lower part Chamber 17 Upper chamber

───────────────────────────────────────────────────── フロントページの続き (71)出願人 000105040 クロリンエンジニアズ株式会社 東京都江東区深川2丁目6番11号 富岡橋 ビル (72)発明者 坂田 昭博 東京都港区西新橋一丁目14番1号 東亞合 成株式会社内 (72)発明者 斉木 幸治 大阪府大阪市北区中之島三丁目2番4号 鐘淵化学工業株式会社内 (72)発明者 相川 洋明 東京都千代田区霞が関三丁目2番5号 三 井化学株式会社内 (72)発明者 片山 真二 岡山県玉野市東高崎24丁目6号 クロリン エンジニアズ株式会社内 (72)発明者 山口 健三 東京都中央区築地5丁目6番4号 コンセ プト エンジニアズ株式会社内 Fターム(参考) 4K011 AA12 DA03 4K021 BA03 CA08 CA09 DB16 DB31 DB46  ──────────────────────────────────────────────────続 き Continuation of the front page (71) Applicant 000105040 Chlorine Engineers Co., Ltd. 2-6-111 Fukagawa, Koto-ku, Tokyo Tomiokabashi Building (72) Inventor Akihiro Sakata 1-14-1 Nishishinbashi, Minato-ku, Tokyo (72) Koji Saiki, Inventor 3-4-2 Nakanoshima, Kita-ku, Osaka-shi, Osaka Prefecture Kanebuchi Chemical Industry Co., Ltd. (72) Hiroaki Aikawa 3-2-2 Kasumigaseki, Chiyoda-ku, Tokyo, Japan No. 5 Inside Mitsui Chemicals, Inc. (72) Inventor Shinji Katayama 24-6 Higashi-Takasaki, Tamano-shi, Okayama Prefecture Inside Chlorine Engineers Co., Ltd. (72) Kenzo Yamaguchi 5-6-1, Tsukiji, Chuo-ku, Tokyo Consulate F-term in PT Engineers Co., Ltd. (reference) 4K011 AA12 DA03 4K021 BA03 CA08 CA09 DB16 DB31 DB46

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 陽極、イオン交換膜及びガス拡散電極よ
りなる酸素陰極を用いる電解槽において、陰極エレメン
トに隣接して陰極集電枠の面に沿って中央側に設けた上
下部チャンバーの酸素ガス出入口に接してガス拡散電極
の酸素ガス出入口を有するガス室、ガス拡散電極とイオ
ン交換膜の間に苛性液が入る陰極室から構成される電解
槽の外側端部に、苛性液排出口として上部チャンバー
を、苛性液導入口として下部チャンバーを、苛性液通路
を介して接続する苛性室枠を設けたことを特徴とする電
解槽。
1. An electrolytic cell using an oxygen cathode comprising an anode, an ion exchange membrane and a gas diffusion electrode, wherein oxygen gas in upper and lower chambers provided at the center side along the surface of the cathode current collecting frame adjacent to the cathode element. A gas chamber having an oxygen gas inlet / outlet of the gas diffusion electrode in contact with the inlet / outlet, a cathode chamber into which the caustic liquid enters between the gas diffusion electrode and the ion exchange membrane, and an upper end serving as a caustic liquid outlet at the outer end of the electrolytic cell. An electrolytic cell having a caustic chamber frame, wherein the chamber is a caustic liquid inlet and the lower chamber is connected via a caustic liquid passage.
【請求項2】 各チャンバーからの苛性液通路は、狭い
間隔を有する平行な板材の間に形成され、苛性液の分散
の均一化及び強度の確保のために間隔10〜100mm
にスペーサーが設けられていることを特徴とする請求項
1記載の電解槽。
2. A caustic solution passage from each chamber is formed between parallel plate members having a narrow space, and a space of 10 to 100 mm is provided for uniformity of dispersion of the caustic solution and securing of strength.
The electrolytic cell according to claim 1, wherein a spacer is provided on the cell.
JP11093589A 1999-03-31 1999-03-31 Electrolytic cell Expired - Fee Related JP3041793B1 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP11093589A JP3041793B1 (en) 1999-03-31 1999-03-31 Electrolytic cell
US09/701,418 US6383349B1 (en) 1999-03-31 2000-03-28 Electrolytic cell using gas diffusion electrode and power distribution method for the electrolytic cell
CNB008004536A CN1163634C (en) 1999-03-31 2000-03-28 Electrolytic cell using gas diffusion electrode and power distribution method for electrolytic cell
EP00911433A EP1092789B1 (en) 1999-03-31 2000-03-28 Electrolytic cell using gas diffusion electrode and power distribution method for the electrolytic cell
PCT/JP2000/001921 WO2000060140A1 (en) 1999-03-31 2000-03-28 Electrolytic cell using gas diffusion electrode and power distribution method for the electrolytic cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11093589A JP3041793B1 (en) 1999-03-31 1999-03-31 Electrolytic cell

Publications (2)

Publication Number Publication Date
JP3041793B1 JP3041793B1 (en) 2000-05-15
JP2000282282A true JP2000282282A (en) 2000-10-10

Family

ID=14086493

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11093589A Expired - Fee Related JP3041793B1 (en) 1999-03-31 1999-03-31 Electrolytic cell

Country Status (1)

Country Link
JP (1) JP3041793B1 (en)

Also Published As

Publication number Publication date
JP3041793B1 (en) 2000-05-15

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