Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0245300B2 - - Google Patents
[go: Go Back, main page]

JPH0245300B2 - - Google Patents

Info

Publication number
JPH0245300B2
JPH0245300B2 JP57222140A JP22214082A JPH0245300B2 JP H0245300 B2 JPH0245300 B2 JP H0245300B2 JP 57222140 A JP57222140 A JP 57222140A JP 22214082 A JP22214082 A JP 22214082A JP H0245300 B2 JPH0245300 B2 JP H0245300B2
Authority
JP
Japan
Prior art keywords
electrolytic
electrolytic solution
electrolyte
regeneration
nickel
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
Application number
JP57222140A
Other languages
Japanese (ja)
Other versions
JPS59112572A (en
Inventor
Toshuki Nakanishi
Shogo Suzuki
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.)
Furukawa Battery Co Ltd
Original Assignee
Furukawa Battery 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 Furukawa Battery Co Ltd filed Critical Furukawa Battery Co Ltd
Priority to JP57222140A priority Critical patent/JPS59112572A/en
Publication of JPS59112572A publication Critical patent/JPS59112572A/en
Publication of JPH0245300B2 publication Critical patent/JPH0245300B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D21/00Processes for servicing or operating cells for electrolytic coating
    • C25D21/16Regeneration of process solutions
    • C25D21/18Regeneration of process solutions of electrolytes

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、電解析出法に使用した電解液の再生
法に関する。 従来、多孔性ニツケル焼結体等の多孔性電極基
板にニツケル活物質を充填する方法として、硝酸
ニツケル、硫酸ニツケル等のニツケル塩水溶液を
電解液とし、ニツケル板を対極板として陰電解を
行ないその多孔性基板内に水酸化ニツケル活物質
を析出せしめるいわゆる電解析出法によるニツケ
ル電極板の製造は公知であるが、その電解析出工
程に於て、時間が経つにつれ、アンモニウムイオ
ンNH4 +が多量に生成し、これが、基板中での水
酸化ニツケルの析出含浸が低下し、能率のよい連
続作業を困難にしている。含浸性良く連続的に電
解析出させるためには、このアンモニウムイオン
を或る一定以下に制御する必要がある。このた
め、新電解液との交換や電解液にアルカリ水溶液
を添加しアンモニウムイオンをアンモニアガスの
形として除去し、その後アルカリ性を酸で中和
し、アンモニウムイオンの除去された電解液に再
生して再び利用する等の手段が行なわれていた
が、製造コストの増大をもたらし、又その再生に
薬液を使用したり、中和により、極板に残存して
自己放電特性を悪くするNaNO3が生成し好まし
くない等の不利益を伴なう。 本発明は、かかる欠点を除去し、薬品を使用す
ることなく、アンモニウムイオンを能率良く除去
し得られ、連続製造を可能にした電解析出法に使
用した電解液の再生法を提供するもので、アルカ
リ蓄電池用電極基板に活物質を電解析出せしめる
工程に於て生成するアンモニウムイオンを含む電
解液を再生する方法に於て、その電解液を電解槽
から取り出し、その電解液を加熱濃縮後冷却して
有効成分を結晶として析出せしめ、次で液と分離
して得た結晶を水に溶解し、所定の濃度の電解液
とすることを特徴とする。 本発明実施の1例を添付図面につき説明する。 第1図は、本法を実施する電解液再生装置を付
設したアルカリ蓄電池用ニツケル電極の製造に於
ける水酸化ニツケル活物質の電解析出装置Aを示
し、1は電解槽、2は直流電源、3は直流電源2
に接続するニツケル対極板、4は直流電源2に接
続する帯状ニツケル焼結基板、5は、電槽1内に
収容した電解液を示す。該帯状ニツケル焼結基板
4は、1側の巻き解しロール6より電槽1内の電
解液5を通過し他側の巻き取りロール7に巻き取
られるようにし、連続電解析出作業ができるよう
にしたもので、8はその基板を導く複数個のガイ
ドローラーを示し、そのガイドローラーの1つ
は、電源2に接続されている。基板4は、例えば
多孔度80%、厚さ0.68mmのものとする。この電解
析出装置Aにより、基板の連続電解析出法により
行なう。この場合の条件は、例えば、電解液5
は、4モル硝酸ニツケル水溶液とし、120mA/
cm2の一定の電解条件として、一定速度で該基板4
を電解液5内に浸漬し対極板3との陰電解を行な
うもので、本発明によれば、該装置Aに本法を実
施する電解液装置Bを次のように付設し、前記電
解液5の1部をとり出し、再生し、再びこれを電
解槽1にもどして常に電解液1内の電解液5中の
アンモニウムイオン濃度を一定以下に保ち、連続
して活物質の電解析出が行なえるようにした。 即ち、9は、再生槽を示し、これに、ジヤケツ
ト9aを有し、該ジヤケツト9a内には水等の冷
媒と加熱水蒸気等の熱媒を交換流通するようにし
た。該再生槽9は、前記電解槽1よりの排液管1
0を受けるべく上面開口している。該再生槽9の
下部1側面には、分離液取り出し用開閉弁口11
とその下部他側面には、先端口を電槽1上面に位
置せしめた調製液供給パイプ12を有し、該パイ
プ12には弁閉弁13とポンプ14とを介在され
ている。該分離液取り出し用弁口11の内側に網
状等のフイルターを設けることも出来る。本装置
を使用し、電解液を再生するには、電解槽1内の
電解液5が電解析出過程で生成するアンモニウム
イオンが、活物質の析出生成効率が低下するほど
に過剰になつたとき、その1部を該排液管10よ
り再生槽9内に取り出しその再生槽9のジヤケツ
ト9aに加熱水蒸気等の熱媒を通して電解液を
100℃以上に加熱し水分を蒸発させ初期体積の70
〜80%程度に濃縮し、次でジヤケツト9a内に冷
媒を通して20℃まで冷却し放置する。かくして容
積の80%程度が結晶化したところで、取り出し用
弁口11を開き、液分を分離除去する。この液分
には、アンモニウムイオンが濃厚に含有されて居
り、結晶として残溜する側には殆んどアンモニウ
ムイオンは残らない。かくして、結晶の残溜した
再生槽9内に、所定量の水を加え加熱し、又は直
接温水を加えて溶解し、所定濃度の電解液に調製
した後、これを弁13に開き、ポンプ14により
パイプ12により電槽1内へもどす、このように
して電解液5の再生を繰り返し電槽1へもどすこ
とにより、常に所定の良好な電解液の状態で電解
析出法ができ、高能率な作業ができる。 次に本法により再生した電解液を使用した電解
液のアンモニウムイオン濃度の変化、活物質含浸
量の変化、その製造極板の残存容量比(ケース
)を、電解液を再生しない場合のもの(ケース
)及び電解液をアルカリでアンモニアガスを除
去後硝酸で再溶解した再生した場合(ケース)
とを夫々比較試験、測定し下記表1に示す結果を
得た。
The present invention relates to a method for regenerating an electrolyte used in electrolytic deposition. Conventionally, as a method for filling a porous electrode substrate such as a porous nickel sintered body with a nickel active material, a nickel salt aqueous solution such as nickel nitrate or nickel sulfate is used as an electrolyte, and a nickel plate is used as a counter electrode to perform negative electrolysis. The production of nickel electrode plates by the so-called electrolytic deposition method in which a nickel hydroxide active material is deposited within a porous substrate is known, but as time passes during the electrolytic deposition process, ammonium ions NH 4 + It forms in large quantities, which reduces the precipitate impregnation of nickel hydroxide in the substrate and makes efficient continuous operation difficult. In order to achieve continuous electrolytic deposition with good impregnating properties, it is necessary to control the ammonium ions below a certain level. For this reason, ammonium ions are removed in the form of ammonia gas by replacing the electrolyte with a new electrolyte or adding an alkaline aqueous solution to the electrolyte, and then neutralizing the alkalinity with acid to regenerate the electrolyte from which ammonium ions have been removed. Measures such as reusing the electrodes have been used, but this increases manufacturing costs and requires the use of chemicals for regeneration, and due to neutralization, NaNO 3 remains on the electrode plates and deteriorates their self-discharge characteristics. It is accompanied by disadvantages such as being undesirable. The present invention eliminates these drawbacks and provides a method for regenerating the electrolytic solution used in electrolytic deposition, which can efficiently remove ammonium ions without using chemicals, and which enables continuous production. In a method for regenerating an electrolytic solution containing ammonium ions generated in the process of electrolytically depositing an active material onto an electrode substrate for an alkaline storage battery, the electrolytic solution is removed from an electrolytic tank, and the electrolytic solution is heated and concentrated. It is characterized in that it is cooled to precipitate the active ingredient as crystals, and then separated from the liquid and the resulting crystals are dissolved in water to form an electrolytic solution with a predetermined concentration. An example of implementing the present invention will be described with reference to the accompanying drawings. Figure 1 shows an electrolytic deposition apparatus A for nickel hydroxide active material used in the production of nickel electrodes for alkaline storage batteries, which is equipped with an electrolyte regeneration apparatus that implements this method, in which 1 is an electrolytic tank and 2 is a DC power source. , 3 is DC power supply 2
4 is a strip-shaped sintered nickel substrate connected to the DC power supply 2, and 5 is an electrolytic solution contained in the battery case 1. The strip-shaped nickel sintered substrate 4 passes through the electrolytic solution 5 in the battery container 1 through an unwinding roll 6 on one side and is wound up onto a winding roll 7 on the other side, thereby enabling continuous electrolytic deposition work. 8 indicates a plurality of guide rollers that guide the substrate, and one of the guide rollers is connected to the power source 2. The substrate 4 has, for example, a porosity of 80% and a thickness of 0.68 mm. Using this electrolytic deposition apparatus A, continuous electrolytic deposition of a substrate is performed. The conditions in this case are, for example, electrolyte 5
is a 4M nickel nitrate aqueous solution, 120mA/
The substrate 4 at a constant speed as a constant electrolytic condition of cm 2
is immersed in an electrolytic solution 5 to perform negative electrolysis with a counter electrode plate 3.According to the present invention, an electrolytic solution device B for carrying out the present method is attached to the device A as follows, and the electrolytic solution is A part of the electrolyte 5 is taken out, regenerated, and returned to the electrolytic bath 1 to keep the ammonium ion concentration in the electrolytic solution 5 below a certain level at all times, and the active material is continuously electrolytically deposited. I made it possible to do it. That is, the regeneration tank 9 has a jacket 9a in which a refrigerant such as water and a heat medium such as heated steam are exchanged and circulated. The regeneration tank 9 includes a drain pipe 1 from the electrolytic tank 1.
The top surface is open to receive 0. On the side of the lower part of the regeneration tank 9, there is an on-off valve port 11 for taking out the separated liquid.
A prepared liquid supply pipe 12 whose tip end is located on the upper surface of the battery container 1 is provided at the lower part and other side surfaces thereof, and a valve closing valve 13 and a pump 14 are interposed in the pipe 12. A net-like filter or the like can also be provided inside the separated liquid extraction valve port 11. In order to regenerate the electrolytic solution using this device, when the ammonium ions generated in the electrolytic solution 5 in the electrolytic cell 1 during the electrolytic deposition process become excessive to the extent that the active material precipitation generation efficiency decreases. , a part of the electrolyte is taken out from the drain pipe 10 into the regeneration tank 9 and the electrolyte is passed through the jacket 9a of the regeneration tank 9 through a heating medium such as heated steam.
Heat to over 100℃ to evaporate water and reduce the initial volume to 70
Concentrate it to about 80%, then cool it to 20°C by passing a refrigerant into the jacket 9a and leave it. When about 80% of the volume has been crystallized, the take-out valve 11 is opened to separate and remove the liquid. This liquid fraction contains ammonium ions in a high concentration, and almost no ammonium ions remain on the side where they remain as crystals. In this way, a predetermined amount of water is added and heated in the regeneration tank 9 in which the crystals remain, or hot water is directly added to dissolve the crystals to prepare an electrolytic solution of a predetermined concentration. By repeating the regeneration of the electrolytic solution 5 and returning it to the container 1 in this way, the electrolytic deposition method can always be carried out with a predetermined good electrolyte state, resulting in highly efficient electrolytic deposition. I can work. Next, we compared the changes in the ammonium ion concentration, the changes in the amount of active material impregnated, and the residual capacity ratio (case) of the electrolyte produced using the electrolyte regenerated by this method to those obtained without regenerating the electrolyte (case). case) and regenerated case where ammonia gas is removed from the electrolyte with alkali and then redissolved with nitric acid (case)
Comparative tests and measurements were conducted on each of these, and the results shown in Table 1 below were obtained.

【表】 初期容量
上記表から明らかなように、本法を利用して製
造した電極は、液を全く再生しない場合の電極、
及びアルカリにより除去再生する場合に比し、残
存容量比が高いいわゆる自己放電が少ない電極が
得られることが分る。又その再生法は、アルカリ
による除去再生法に比し、再生コストが著しく低
廉ですむ利点がある。 このように本発明によるときは、単なる加熱、
冷却の物理的手段で簡単にアンモニウムイオンを
除去でき、また分離した有効成分結晶を水に溶解
するだけで電解液を再生でき、アルカリ、酸を使
用し再生する場合に比し不純成分の含まない良好
な電解液に再生する。
[Table] Initial capacity
As is clear from the above table, the electrodes manufactured using this method are the same as those in the case where the liquid is not regenerated at all.
It can be seen that an electrode with a high residual capacity ratio and less so-called self-discharge can be obtained compared to the case where the electrode is removed and regenerated using an alkali. Moreover, this regeneration method has the advantage that the regeneration cost is significantly lower than the removal regeneration method using alkali. In this way, according to the present invention, mere heating,
Ammonium ions can be easily removed by physical means of cooling, and the electrolyte can be regenerated simply by dissolving the separated active ingredient crystals in water, and does not contain impurities compared to regeneration using alkali or acid. Regenerates into a good electrolyte.

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

図面は本発明実施の1例の線図を示す。 A……電解析出装置、1……電解槽、4……電
極基板、5……電解液、B……電解液再生装置、
9……加熱冷却再生槽、9a……ジヤケツト、1
0……排液管、11……分離液取り出し開閉弁
口、12……調製液供給パイプ、14……ポン
プ。
The drawing shows a diagram of an example of implementing the invention. A... Electrolytic deposition device, 1... Electrolytic cell, 4... Electrode substrate, 5... Electrolyte, B... Electrolyte regeneration device,
9... Heating/cooling regeneration tank, 9a... Jacket, 1
0...Drain pipe, 11...Separated liquid take-out opening/closing valve port, 12...Prepared liquid supply pipe, 14...Pump.

Claims (1)

【特許請求の範囲】[Claims] 1 アルカリ蓄電池用電極基板に活物質を電解析
出せしめる工程に於て生成するアンモニウムイオ
ンを含む電解液を再生する方法に於て、その電解
液を電解槽から取り出し、その電解液を加熱濃縮
後冷却して有効成分を結晶として析出せしめ、次
で液と分離して得た結晶を水に溶解し、所定の濃
度の電解液とすることを特徴とする電解析出法に
使用した電解液の再生法。
1 In a method for regenerating an electrolytic solution containing ammonium ions generated in the process of electrolytically depositing active materials onto electrode substrates for alkaline storage batteries, the electrolytic solution is removed from the electrolytic tank, heated and concentrated, and then An electrolytic solution used in an electrolytic deposition method characterized by cooling to precipitate the active ingredient as crystals, and then separating it from the liquid and dissolving the obtained crystals in water to obtain an electrolytic solution with a predetermined concentration. Regeneration method.
JP57222140A 1982-12-20 1982-12-20 Reclaiming method of electrolyte used in electrolytic extraction process Granted JPS59112572A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57222140A JPS59112572A (en) 1982-12-20 1982-12-20 Reclaiming method of electrolyte used in electrolytic extraction process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57222140A JPS59112572A (en) 1982-12-20 1982-12-20 Reclaiming method of electrolyte used in electrolytic extraction process

Publications (2)

Publication Number Publication Date
JPS59112572A JPS59112572A (en) 1984-06-29
JPH0245300B2 true JPH0245300B2 (en) 1990-10-09

Family

ID=16777796

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57222140A Granted JPS59112572A (en) 1982-12-20 1982-12-20 Reclaiming method of electrolyte used in electrolytic extraction process

Country Status (1)

Country Link
JP (1) JPS59112572A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103842561B (en) * 2011-09-28 2016-03-30 日立金属株式会社 The removing method of the rare earth impurities in nickel plating solution

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5710547B2 (en) * 1973-07-30 1982-02-26

Also Published As

Publication number Publication date
JPS59112572A (en) 1984-06-29

Similar Documents

Publication Publication Date Title
KR101097555B1 (en) Stripping agent for secondary battery electrode material and method of treating secondary battery using the stripping agent
US3335033A (en) Method of making electric battery electrodes
US3600227A (en) Method of impregnating flexible metallic battery plaques
US4330386A (en) Combined ion-exchange particulate bed electrolytic cell
US4863484A (en) Process for producing battery electrodes by electrochemical reduction
JPS5834566A (en) Method for filling porous and flexible expandable metal battery substrates with active materials
JPH0245300B2 (en)
JPH0324022B2 (en)
CN117410437B (en) Antimony-based electrode and preparation method and application thereof
US3671321A (en) Process for production and treatment of battery plates
US4120757A (en) Method of making sintered plaque cadmium electrodes
US3305398A (en) Method for making nickel electrodes for electrolytic cells
JP2007222779A (en) Recovery method of high purity inorganic acid
KR20180080130A (en) Method and apparatus for manufacturing copper foil coated with graphene
US3436266A (en) Method of treating storage battery plates
JPS6136348B2 (en)
US1570115A (en) Storage battery
JPH0241865B2 (en)
SU380424A1 (en) METHOD OF ELECTROLYTES NEUTRALIZATION 'AT ELECTROCHEMICAL TREATMENT OF METALS
US3884717A (en) Method and device for introducing active mass into porous electrode structures for galvanic cells
DE2032699C3 (en) Process for the continuous introduction of active material into porous electrode frameworks for galvanic elements
JPH01312099A (en) Method for controlling electroplating bath
JPS60115159A (en) Manufacture of positive pole plate for alkaline storage battery
US3567517A (en) Process for preparing cadmium electrodes
CN119092859A (en) A lithium ion battery water discharging method and discharging device