JPS60221595A - Method for operating alkali chloride electrolytic cell provided with air electrode as cathode - Google Patents

Method for operating alkali chloride electrolytic cell provided with air electrode as cathode

Info

Publication number
JPS60221595A
JPS60221595A JP7889684A JP7889684A JPS60221595A JP S60221595 A JPS60221595 A JP S60221595A JP 7889684 A JP7889684 A JP 7889684A JP 7889684 A JP7889684 A JP 7889684A JP S60221595 A JPS60221595 A JP S60221595A
Authority
JP
Japan
Prior art keywords
air electrode
water
electrolytic cell
cathode
catholyte
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.)
Pending
Application number
JP7889684A
Other languages
Japanese (ja)
Inventor
Yuko Fujita
藤田 雄耕
Hitoshi Nakamura
仁志 中村
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.)
Japan Storage Battery Co Ltd
Nihon Denchi KK
Original Assignee
Japan Storage Battery Co Ltd
Nihon Denchi KK
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 Japan Storage Battery Co Ltd, Nihon Denchi KK filed Critical Japan Storage Battery Co Ltd
Priority to JP7889684A priority Critical patent/JPS60221595A/en
Publication of JPS60221595A publication Critical patent/JPS60221595A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/34Simultaneous production of alkali metal hydroxides and chlorine, oxyacids or salts of chlorine, e.g. by chlor-alkali electrolysis
    • C25B1/46Simultaneous production of alkali metal hydroxides and chlorine, oxyacids or salts of chlorine, e.g. by chlor-alkali electrolysis in diaphragm cells

Landscapes

  • Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

PURPOSE:To prevent the deterioration of an air electrode in an alkali chloride electrolytic cell by reducing the concn. of an aqueous alkali hydroxide soln. as a catholyte or replacing the soln. with water when the operation of the electrolytic cell is suspended. CONSTITUTION:When the operation of the alkali chloride electrolytic cell provided with the air electrode as a cathode 1 is suspended, the catholyte 8 is replaced with water by drawing out the catholyte 8 from an outlet 9 for descharging a produced aqueous sodium hydroxide soln. and by feeding water from an inlet 7 for feeding water. Part of the catholyte 8 may be replaced with water. By this method the deterioration of the air electrode 1 is prevented.

Description

【発明の詳細な説明】 本発明は空気極を1差極とする塩化アルカリ電解、曹の
運転方法に関するものであり、その目的とするところは
、空気極の劣化を防止せんとするにある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for operating alkaline chloride electrolysis and carbon dioxide using an air electrode as one differential electrode, and its purpose is to prevent deterioration of the air electrode.

塩化アルカリ電解1曹は、通常は連続的に運転さJ’L
るが、停電その他の事由により運転が止められることが
ある。この運転休止時に113極としての空気極の性能
が劣化するという現家が認めらnろ。
Alkaline chloride electrolysis 1st soda is usually operated continuously J'L
However, operation may be stopped due to power outages or other reasons. The current government cannot accept that the performance of the air electrode as the 113th electrode will deteriorate during this suspension of operation.

一方、空気極の触媒J所にはカーボンが用いらnでいる
が、空気極の性能劣化は、このカーボンの願発明者らの
研究にぼれば、カーボンの酸素の吸着サイトの酸素の吸
着されていないサイトとの間で起る局S電池現象に由来
し、陰極電解散としての水酸化ナトリウム水浴液の温度
が高ければ篩いほど、ま1こ水酸化ナトリウムのTM度
か置け1tば毘いほどより進む。まfこ空気極に畦ml
が流れているときより1′醒流が茄れていないときの方
がカーホンはよりJ腐食を受けやすい。
On the other hand, although carbon is not used as a catalyst in the air electrode, the deterioration in the performance of the air electrode is due to the adsorption of oxygen at the oxygen adsorption sites of carbon, according to research by the inventors of this carbon technology. The higher the temperature of the sodium hydroxide water bath solution as the cathode electrolyte is, the more the TM degree of sodium hydroxide is removed. It progresses in moderation. ML on the air pole
Carphones are more susceptible to J corrosion when the 1' stream is not full than when it is flowing.

本発明はこのような知見にもとつ\゛いてなされfコも
のである。すなわち本発明は、垣化アルカリ゛醒解漕の
運転休止時には陰樺電解欣としての水酸化アルカリ水溶
液を水で稀釈するか、水ですりかり置換してしまうこと
により、空気極に用いられているカーボンの腐食を防止
し、空気極の性能劣化を防止するものである。
The present invention has been made based on such knowledge. That is, in the present invention, the alkaline hydroxide aqueous solution used as the shade birch electrolyte is diluted with water or completely replaced with water when the operation of the alkali clarification tank is stopped, so that it can be used in the air electrode. This prevents corrosion of carbon in the air and prevents deterioration of air electrode performance.

以下本発明の一実施例について詳述する。An embodiment of the present invention will be described in detail below.

実施例: 第1図は本発明の一実施例を説明するγこめ
の空%極を陰極とする食塩電解博の断11iI構造を示
す。
Embodiment: FIG. 1 shows a cross section 11iI structure of a salt electrolyte using a γ-cell empty electrode as a cathode to explain an embodiment of the present invention.

1111−)四脩版梢1瓜trス1漁mで 名A通二I
ケIし層(2+、10%の白金触媒を担持せるカーボン
粉床とポリ4フワ化エチレン結看剤との混合物からなる
触媒111(81および多孔性ポリ4フフ化エチレンm
lt’J(4)から構成されている。(5)は窄気供帖
口、(6)は余剰空気排出口、(7)は水供給口、(8
)は水酸化ナトリウム水性液からなる鴎(返奄解欣、(
9)は性成水酸化ナトリウム水溶液導出口、(IOJは
イオン交a暎。
1111-) 4 Shu version 1 gourd 1 fishing meter name A 2 I
Catalyst 111 (81 and porous polytetrafluoroethylene m
It is composed of lt'J(4). (5) is the narrow air supply port, (6) is the excess air outlet, (7) is the water supply port, (8
) is an aqueous solution made of sodium hydroxide.
9) is a synthetic sodium hydroxide aqueous solution outlet (IOJ is an ion exchanger).

(11)は陽極、(12月よ食塩水供給口、(L8)は
塩素導出口、(14)は1硝極電解欣、(15)は僧枠
体である。
(11) is the anode, (December 2015) is the saline water supply port, (L8) is the chlorine outlet, (14) is the 1-nitrode electrolyte, and (15) is the frame body.

この食4北解瘤の正常運転時には、空気供給口(5)か
ら空気を供給しつつ、i(m愼甲と、@+韮(11)と
の間vc30〜40 A/dm2 の面m 電111’
E カ1lll ’j”J、 サn ルト、陰極(!2
で水酸化ナトリウムが生成し、陰極電解液(8)として
の水酸化ナトリウム水浴液の1文は80〜40のに保1
これ、陽極(11)で塩素が生1戎する。
During normal operation of this eclipse 4 north aneurysm, while supplying air from the air supply port (5), a surface m electric current of VC30 to 40 A/dm2 is applied between the 111'
E Ka1llll 'j"J, Sun Ruto, Cathode (!2
Sodium hydroxide is generated, and the sodium hydroxide water bath solution as the catholyte (8) is kept at 80 to 40.
Chlorine is generated at the anode (11).

濃厚な水酸化ナトリウムは生成水内!化ナトリウム水溶
欣導出口(9)から槽外に取り出され、塩素は塩素導出
口(L3)から取り出されろ。陰極電解液(8)の温1
f:は80〜95°Cの範囲に設定される。
Concentrated sodium hydroxide is in the produced water! The sodium chloride solution is taken out of the tank from the aqueous outlet (9), and the chlorine is taken out from the chlorine outlet (L3). Cathode electrolyte (8) temperature 1
f: is set in the range of 80 to 95°C.

この食塩電解槽の運転休止時には、陰極電解液(8)を
生成水酸イじナトリウム水1容M4出口(9)からすべ
て抜き出すとともに、水供給口(7)から水を供給し、
陰極電解液(8)を水に置換する。なお運転イ木止時に
は温度は室温に下がる。
When the operation of this salt electrolyzer is stopped, the cathode electrolyte (8) is completely extracted from the M4 outlet (9) of 1 volume of produced sodium hydroxide water, and water is supplied from the water supply port (7).
The catholyte (8) is replaced with water. The temperature drops to room temperature when the machine stops operating.

効果の比咬例: 上述の実施例のように運転休止時に陰
極電解液を水に置換する本発明の方法をへ方法とし、従
来のように陰極電解液の水酸化ナト運転休止を1サイク
ルとする量大運転をお乙なり1こ際の空気極の運転時に
おけろ電位(対酸化水銀電層)がサイクルと共にどのよ
うな変化するかを調べfごところ第2図に示すような結
果が得ら几1こ。
Example of ratio of effectiveness: The method of the present invention in which the catholyte is replaced with water at the time of suspension of operation as in the above-mentioned embodiment is used as a method, and the suspension of operation of the catholyte with sodium hydroxide as in the conventional method is replaced with one cycle. During the current operation of the air electrode, we investigated how the potential (electrolayer against mercury oxide) changes with the cycle and obtained the results shown in Figure 2. I got one.

第2図から、本究明のA方法の場合にはIIJ)欠運転
サイ・タルの進行とともに空気極の性能劣化は何ら認め
られないのに対し、従来のB方法の場合には、間欠運転
サイクルの進行とともに徐々に空気極が劣化し、30サ
イクル目に急激に劣化しfこ。
From Fig. 2, in the case of method A of this investigation, no deterioration in the performance of the air electrode was observed as the intermittent operation cycle progressed, whereas in the case of the conventional method B, the intermittent operation cycle As time progresses, the air electrode gradually deteriorates, and suddenly deteriorates at the 30th cycle.

この結果から本究明の運転方法が空気極の性能劣化を防
止する上で極めて葡効であることがわか
These results show that the operating method investigated in this study is extremely effective in preventing deterioration of air electrode performance.

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

@1図は本究明の一実施例を説明するfコめの望メを極
を陰極とする食塩電解(台の断面構Cjt示す。 第2図は、本究明の一実施例にかかる空気極をIIJ極
とする食塩′Iと解槽の運転方法(A)と従来の運転方
法(均との歯欠運転サイクルを傾り返しγこ際の空気極
の電位のサイクル変化を示す。 ■・・・・陰極、2・・・・・多孔1生ニツケルj湧。 3・・−・ @煤層、4・・・−・・多孔性ポリ47)
化エチレン模J埒、 5・・・・・・空気供給口、 6
・・・・・・余剰空′A排出口、 7・・・・・・水供
給口、 8・・曲1鱗園電解t(グ、9・・・・ 生成
水酸化ナトリウム水M欣尋出口。 lO・・ イオン交換膜、11・・・・1易庵。 12・・・・・&塩水供給口、1B・・・・・・塩素導
出口。 14・・・・1禍庵、を解液、15・・曲博枠体。 方 T 菌 オ 7 図 内X運軌デイ7ル
@ Figure 1 shows a cross-sectional structure of a table for salt electrolysis with a cathode as the third perspective to explain an embodiment of this research. Figure 2 shows an air electrode according to an embodiment of this research. The operation method (A) of the salt solution tank with the IIJ electrode and the conventional operation method (with a toothless operation cycle with γ) are shown below. ... cathode, 2 ... porous 1 raw nickel j spring. 3 ... - @ soot layer, 4 ... - ... porous poly 47)
Ethylene chloride model, 5...Air supply port, 6
... Surplus air 'A discharge port, 7 ... Water supply port, 8 ... Song 1 Urokoen electrolysis t (g, 9 ... Produced sodium hydroxide water M Kinhiro outlet . 1O... Ion exchange membrane, 11...1 Ian. 12... & salt water supply port, 1B... Chlorine outlet. 14... 1 Kaan, solved. Liquid, 15...Kokuhaku frame body.

Claims (1)

【特許請求の範囲】[Claims] 窒%極を1嵯極とする塩化アルカリ電解槽の運転休止時
には極電解改としての水酸化アルカリ水浴液を水で稀釈
するか置換することを特徴とする空気ffiを陰極とす
る壇1bアルカリ屯解h1檜の運転方法。
A stage 1b alkaline tank with air ffi as the cathode characterized by diluting or replacing the alkaline hydroxide water bath solution with water as a electrode electrolytic reformer when the operation of an alkaline chloride electrolytic cell with a nitrogen % electrode as one electrode is stopped. Solution h1 How to drive Hinoki.
JP7889684A 1984-04-18 1984-04-18 Method for operating alkali chloride electrolytic cell provided with air electrode as cathode Pending JPS60221595A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7889684A JPS60221595A (en) 1984-04-18 1984-04-18 Method for operating alkali chloride electrolytic cell provided with air electrode as cathode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7889684A JPS60221595A (en) 1984-04-18 1984-04-18 Method for operating alkali chloride electrolytic cell provided with air electrode as cathode

Publications (1)

Publication Number Publication Date
JPS60221595A true JPS60221595A (en) 1985-11-06

Family

ID=13674573

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7889684A Pending JPS60221595A (en) 1984-04-18 1984-04-18 Method for operating alkali chloride electrolytic cell provided with air electrode as cathode

Country Status (1)

Country Link
JP (1) JPS60221595A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61166991A (en) * 1985-01-18 1986-07-28 Asahi Glass Co Ltd Method for restoring current efficiency
JPH05271974A (en) * 1992-03-26 1993-10-19 Choichi Furuya Electrolytic cell for ion-exchange membrane process using gas diffusion electrode
JP2014091838A (en) * 2012-10-31 2014-05-19 Chlorine Engineers Corp Ltd Reverse current prevention method for ion exchange membrane electrolytic cell
JP2015120944A (en) * 2013-12-20 2015-07-02 旭化成株式会社 Electrolysis cell and electrolysis tank
US10472723B2 (en) 2015-01-06 2019-11-12 Thyssenkrupp Uhde Chlorine Engineers (Japan) Ltd. Method of preventing reverse current flow through an ion exchange membrane electrolyzer

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61166991A (en) * 1985-01-18 1986-07-28 Asahi Glass Co Ltd Method for restoring current efficiency
JPH0333794B2 (en) * 1985-01-18 1991-05-20 Asahi Glass Co Ltd
JPH05271974A (en) * 1992-03-26 1993-10-19 Choichi Furuya Electrolytic cell for ion-exchange membrane process using gas diffusion electrode
JP2014091838A (en) * 2012-10-31 2014-05-19 Chlorine Engineers Corp Ltd Reverse current prevention method for ion exchange membrane electrolytic cell
JP2015120944A (en) * 2013-12-20 2015-07-02 旭化成株式会社 Electrolysis cell and electrolysis tank
US10472723B2 (en) 2015-01-06 2019-11-12 Thyssenkrupp Uhde Chlorine Engineers (Japan) Ltd. Method of preventing reverse current flow through an ion exchange membrane electrolyzer

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