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JPH0566715B2 - - Google Patents

Info

Publication number
JPH0566715B2
JPH0566715B2 JP60170459A JP17045985A JPH0566715B2 JP H0566715 B2 JPH0566715 B2 JP H0566715B2 JP 60170459 A JP60170459 A JP 60170459A JP 17045985 A JP17045985 A JP 17045985A JP H0566715 B2 JPH0566715 B2 JP H0566715B2
Authority
JP
Japan
Prior art keywords
active material
sintered substrate
material filling
manufacturing
filling unit
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
JP60170459A
Other languages
Japanese (ja)
Other versions
JPS6231948A (en
Inventor
Narifumi Matsuki
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.)
Resonac Corp
Original Assignee
Shin Kobe Electric Machinery 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 Shin Kobe Electric Machinery Co Ltd filed Critical Shin Kobe Electric Machinery Co Ltd
Priority to JP60170459A priority Critical patent/JPS6231948A/en
Publication of JPS6231948A publication Critical patent/JPS6231948A/en
Publication of JPH0566715B2 publication Critical patent/JPH0566715B2/ja
Granted legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/24Electrodes for alkaline accumulators
    • H01M4/26Processes of manufacture
    • H01M4/28Precipitating active material on the carrier
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、焼結基板へ活物質の充填を行うアル
カリ蓄電池用焼結式極板の製造方法に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for manufacturing a sintered electrode plate for an alkaline storage battery, in which a sintered substrate is filled with an active material.

[従来の技術] 一般に、アルカリ蓄電池用焼結式極板において
は、第3図に示されているように、帯板状焼結基
板に、含浸工程1で活物質の塩の溶液を含浸し、
次いで、電解工程2で電解処理を行う。このよう
に電解処理が行われた焼結基板を次に水洗工程3
で水洗し、その後焼結基板を乾燥工程4で乾燥す
る。これらの含浸工程1、電解工程2、水洗工程
3及び乾燥工程4により焼結基板に対して1回の
活物質充填単位工程5による処理を行う。そこ
で、焼結基板に十分な活物質を充填するためには
数回の活物質充填単位工程5による処理を行わな
ければならない。
[Prior Art] Generally, in a sintered electrode plate for an alkaline storage battery, as shown in FIG. ,
Next, electrolytic treatment is performed in electrolysis step 2. The sintered substrate subjected to electrolytic treatment in this way is then subjected to water washing step 3.
After washing with water, the sintered substrate is dried in a drying step 4. Through these impregnation step 1, electrolysis step 2, water washing step 3, and drying step 4, the sintered substrate is subjected to one active material filling unit step 5. Therefore, in order to fill the sintered substrate with a sufficient amount of active material, the active material filling unit process 5 must be performed several times.

従つて、従来では、活物質充填単位工程5を数
回繰り返し行うために、第4図に示すように直線
状の製造ライン6に沿つて活物質充填単位工程5
を繰り返し行い、順次焼結基板に活物質を充填し
ていた。また、これら各工程5において、活物質
の塩の溶液槽、電解槽及び水洗槽のそれぞれに焼
結基板を浸漬するが、この場合、第5図に示すよ
うに、複数のローラ7を用いて帯板状焼結基板8
を上下方向に折曲げて対応する槽9内に挿入して
いた。
Therefore, conventionally, in order to repeat the active material filling unit process 5 several times, the active material filling unit process 5 is carried out along a linear production line 6 as shown in FIG.
This process was repeated to sequentially fill the sintered substrate with active material. In addition, in each of these steps 5, the sintered substrate is immersed in each of the active material salt solution bath, electrolytic bath, and water washing bath. In this case, as shown in FIG. Band-shaped sintered substrate 8
was bent vertically and inserted into the corresponding tank 9.

[本発明が解決しようとする問題点] しかし、上記従来の製造方法では、活物質充填
単位工程5を繰り返し行う製造ライン6が直線状
なので、各工程5の各処理液槽と乾燥装置とが順
次同一直線状に並んで配置されることになり、こ
のため活物質の塩の溶液の温度及び濃度等の条
件、電解処理の条件、水洗処理における水量等の
条件及び乾燥処理の条件をそれぞれ個々に制御す
る必要があつて制御装置が多くなり、製造装置が
高価になる問題点があつた。しかも、各工程にお
ける作業条件が異り易く品質管理が効果的に行え
ないという問題点があつた。
[Problems to be Solved by the Present Invention] However, in the conventional manufacturing method described above, since the manufacturing line 6 in which the active material filling unit process 5 is repeated is linear, each processing liquid tank and drying device in each process 5 are Therefore, the conditions such as the temperature and concentration of the active material salt solution, the conditions of electrolytic treatment, the conditions such as the amount of water in washing treatment, and the conditions of drying treatment must be adjusted individually. There was a problem that the number of control devices needed to be controlled was increased, and the manufacturing equipment became expensive. Moreover, there was a problem in that the working conditions in each process were likely to differ, making it difficult to effectively control quality.

本発明の目的は、製造装置を安価に構成でき、
しかも、品質管理を効果的に行えるアルカリ蓄電
池用焼結式極板の製造方法を提案することにあ
る。
An object of the present invention is to be able to construct a manufacturing device at low cost;
Moreover, it is an object of the present invention to propose a method for manufacturing sintered electrode plates for alkaline storage batteries that allows for effective quality control.

[問題点を解決するための手段] 本発明を、その一実施例を示す第1図及び第2
図を参照して説明すると、帯板状焼結基板8に、
活物質の塩の溶液を含浸し、順次電解処理を行
い、水洗を行つた後乾燥を施す活物質充填単位工
程5を製造ライン6に沿つて活物質充填単位工程
5を複数回繰り返すことにより活物質充填作業を
繰り返し行つて活物質を焼結基板8に充填するア
ルカリ蓄電池用焼結式基板の製造方法であつて、
本発明においては、製造ライン6を蛇行させて該
蛇行した製造ライン6に沿つて各活物質充填単位
工程5による活物質充填作業を繰り返し行い、蛇
行した製造ライン6の平行なライン部分に対して
直交する方向に並ぶ同じ工程による処理の共用の
装置によつてそれぞれ行い、且つ、焼結基板8は
その板面8aを起立させて各活物質充填単位工程
5に送り込む。
[Means for solving the problems] The present invention is illustrated in FIGS. 1 and 2 showing one embodiment thereof.
To explain with reference to the figure, on the strip-shaped sintered substrate 8,
The active material filling unit step 5 is repeated several times along the production line 6, in which the active material is impregnated with a salt solution, sequentially electrolyzed, washed with water, and then dried. A method for manufacturing a sintered substrate for an alkaline storage battery, in which a sintered substrate 8 is filled with an active material by repeatedly carrying out material filling operations,
In the present invention, the production line 6 is made to meander, and the active material filling operation by each active material filling unit process 5 is repeated along the meandering production line 6, and the parallel line portions of the meandering production line 6 are The same processes arranged in orthogonal directions are carried out using a shared device, and the sintered substrate 8 is sent to each active material filling unit process 5 with its plate surface 8a erected.

[作用] 上記のようにすると、蛇行した製造ライン6に
沿つて活物質充填単位工程5いよる活物質充填作
業を焼結基板8に繰り返し行い、蛇行した製造ラ
イン6の平行なライン部分に直交する向きに並ぶ
同じ工程による処理を共用の装置によつてそれぞ
れ行うので、従来に比して制御装置を少なくして
製造装置を安価に構成でき、しかも、各活物質充
填単位工程5における同じ工程による処理を共用
の装置で行うので、作業条件が同じになり、品質
管理を効果的に行える。
[Operation] By doing as described above, the active material filling operation according to the active material filling unit process 5 is repeatedly performed on the sintered substrate 8 along the meandering production line 6, and the active material filling operation is repeated at right angles to the parallel line portion of the meandering production line 6. Since the same processes are performed in the same direction, each process is performed by a shared device, the manufacturing device can be constructed at low cost with fewer control devices than in the past. Since the processing is carried out using shared equipment, the working conditions are the same and quality control can be carried out effectively.

[実施例] 以下本発明の実施例を図面を参照して詳細に説
明する。
[Example] Hereinafter, an example of the present invention will be described in detail with reference to the drawings.

先ず、本発明の製造方法を行う各処理工程にお
ける処理液槽に帯板状焼結基板を挿入する状態を
説明する。第2図に示すように、処理液槽11の
相互に対向する一組の側壁12にそれぞれ縦に延
びる2個のスリツト13を形成し、各スリツト1
3に板面8aを起立させた帯板状焼結基板8を通
して該焼結基板を矢印の何れかの方向に送給する
ようにしている。この場合、スリツト13を構成
する部材は、側壁12に嵌め込まれたゴム等の弾
性体14からなつている。尚処理液槽11に形成
するスリツト13の数は送給する焼結基板8の枚
数等によつて定められ、その数は任意である。
First, the state in which the strip-shaped sintered substrate is inserted into the processing liquid tank in each processing step of the manufacturing method of the present invention will be explained. As shown in FIG. 2, two vertically extending slits 13 are formed in a pair of mutually opposing side walls 12 of the processing liquid tank 11, and each slit 1
The sintered substrate 3 is fed in either direction of the arrow through a band-shaped sintered substrate 8 having a raised plate surface 8a. In this case, the member constituting the slit 13 is an elastic body 14 such as rubber fitted into the side wall 12. The number of slits 13 formed in the processing liquid tank 11 is determined by the number of sintered substrates 8 to be fed, and the number is arbitrary.

次に、板面8aを起立して送給される帯板状焼
結基板8に活物質を充填する方法を説明する。本
発明の製造方法では、第1図に示されているよう
に、製造ライン6が蛇行状に配置されており、こ
の蛇行状の製造ライン6のそれぞれの往路ライン
部分6A及び復路ライン部分6Bが相互に平行に
配置されている。この製造ライン6では、含浸工
程1、電解工程2、水洗工程3及び乾燥工程4か
らなる活物質充填単位工程5による活物質充填作
業を続けて数回行うようになつている。そこで、
このような製造ライン6において、焼結基板8に
活物質を充填するには、先ず、含浸工程1で活物
質の塩の溶液槽21に帯板状焼結基板8を挿入す
る。(この際、陽極板を成形する場合には、硝酸
ニツケル飽和溶液に焼結基板8を浸漬、陰極板を
成形する場合には、硝酸カドミウムまたは塩化カ
ドミウムの飽和溶液に焼結基板8を浸漬する。)
次いで、電解工程2の電解槽22に焼結基板8を
挿入する。(この際、陽極板においては電解酸化
処理を行い、陰極板においては電解還元処理を行
う。)電解処理を施した焼結基板8を次いで水洗
工程3の水洗槽23に挿入して水洗を行い、この
水洗が行われた焼結基板8は乾燥工程4の乾燥装
置24によつて乾燥作業を行う。このようにし
て、1回目の活物質充填単位工程5が終了する
と、後続の活物質充填単位工程5で活物質充填作
業を続けて数回行つて焼結基板8に対する活物質
充填作業を完了する。
Next, a method of filling the active material into the strip-shaped sintered substrate 8, which is fed with the plate surface 8a erected, will be explained. In the manufacturing method of the present invention, as shown in FIG. 1, the manufacturing line 6 is arranged in a meandering manner, and each of the outgoing line portion 6A and the incoming line portion 6B of this meandering manufacturing line 6 is arranged in a meandering manner. are arranged parallel to each other. In this production line 6, the active material filling operation in an active material filling unit process 5 consisting of an impregnation process 1, an electrolysis process 2, a water washing process 3, and a drying process 4 is performed several times in succession. Therefore,
In such a production line 6, in order to fill the sintered substrate 8 with the active material, first, in the impregnation step 1, the strip-shaped sintered substrate 8 is inserted into the active material salt solution bath 21. (At this time, when forming the anode plate, the sintered substrate 8 is immersed in a saturated solution of nickel nitrate; when forming the cathode plate, the sintered substrate 8 is immersed in a saturated solution of cadmium nitrate or cadmium chloride. .)
Next, the sintered substrate 8 is inserted into the electrolytic bath 22 of the electrolytic step 2. (At this time, the anode plate is subjected to electrolytic oxidation treatment, and the cathode plate is subjected to electrolytic reduction treatment.) The electrolytically treated sintered substrate 8 is then inserted into the washing tank 23 of the washing step 3 and washed with water. The sintered substrate 8 that has been washed with water is dried by the drying device 24 in the drying step 4. In this way, when the first active material filling unit step 5 is completed, the active material filling operation is performed several times in succession in the subsequent active material filling unit step 5, and the active material filling operation for the sintered substrate 8 is completed. .

この際、焼結基板8の送給方向は往路ライン部
分6Aにおける送給方向と復路ライン部分6Bの
それとは逆で、順に行う各処理工程のうちの電解
工程2が往路ライン部分6A及び復路ライン部分
6Bに対して直交する直線上に位置することにな
る。従つて、各活物質充填単位工程5におけるそ
れぞれの電解工程2を1個の共用の装置としての
電解槽22で行う。この場合、電解槽22には活
物質充填単位工程5の数に応じて焼結基板8を通
すスリツト13の数等を設定しておく。往路ライ
ン部分6Aから復路ライン部分6Bへ行く境のそ
れぞれの焼結基板8のターン部分6C及び復路ラ
イン部分6Bから往路ライン部分6Aへ行く境の
それぞれの焼結基板8のターン部分6Dにそれぞ
れ共用の装置としての乾燥装置24,24を配置
して乾燥工程4による処理を行う。このようにし
て、焼結基板8を往路ライン部分6A、復路ライ
ン部分6Bと順に蛇行させながら送給して所定回
数の活物質充填単位工程5による活物質充填作業
を行う。
At this time, the feeding direction of the sintered substrate 8 is opposite to the feeding direction in the outgoing line portion 6A and that in the returning line portion 6B. It will be located on a straight line orthogonal to the portion 6B. Therefore, each electrolytic step 2 in each active material filling unit step 5 is performed in the electrolytic cell 22 as one shared device. In this case, the number of slits 13 through which the sintered substrate 8 is passed is set in the electrolytic cell 22 in accordance with the number of active material filling unit processes 5. Commonly used for turn portions 6C of each sintered substrate 8 at the boundary from the outbound line portion 6A to the return line portion 6B, and turn portions 6D of each sintered substrate 8 at the boundary from the inbound line portion 6B to the outbound line portion 6A. Drying devices 24, 24 are arranged to perform the drying process 4. In this way, the sintered substrate 8 is fed in a meandering manner in order from the forward line portion 6A to the backward line portion 6B, and the active material filling operation in the active material filling unit process 5 is performed a predetermined number of times.

上記実施例において、各処理液槽には縦にスリ
ツト13が形成されているため、外部に処理液が
散出することがあり、この場合、散出する処理液
を皿状部材で受けてポンプ等により該処理液を処
理液槽に戻すようにするとよい。
In the above embodiment, since the slits 13 are formed vertically in each processing liquid tank, the processing liquid may spill out to the outside. It is preferable to return the processing liquid to the processing liquid tank by, for example,

尚、上記実施例においては、蛇行する製造ライ
ン6上のそれぞれの電解工程2による処理を1個
の共用の装置としての電解槽22で行い、それぞ
れの乾燥工程4による処理を2個の共用装置とし
ての乾燥装置24,24で行うようにしている
が、本発明はこれに限定されるものではなく、製
造ライン6上のそれぞれの含浸工程1による処理
を1個の共用の装置としての活物質の塩の溶液槽
で行い、それぞれの水洗工程3による処理を2個
の共用の装置としての水洗槽で行うようにしても
よく、蛇行した製造ライン6の平行なライン部分
に対して直交する方向に並ぶ同じ工程による処理
を共用の装置によつてそれぞれ行うようにすれば
よい。
In the above embodiment, each electrolytic process 2 on the meandering production line 6 is carried out in one shared electrolytic tank 22, and each drying process 4 is carried out in two shared apparatuses. However, the present invention is not limited to this, and the treatment in each impregnation step 1 on the production line 6 is carried out in one shared device. The water washing step 3 may be carried out in a salt solution tank, and the processing in each washing step 3 may be carried out in two washing tanks serving as shared equipment, and the direction perpendicular to the parallel line portion of the meandering production line 6. It is only necessary to use a shared device to carry out the same processes in the same manner.

[発明の効果] 以上のように本発明によれば、蛇行した製造ラ
インに沿つて活物質充填単位工程による活物質充
填作業を焼結基板に繰り返し行い、蛇行した製造
ラインの平行なライン部分に直交する向きに並ぶ
同じ工程による処理を共用の装置によつてそれぞ
れ行うので、従来に比して制御装置を少なくして
製造装置を安価に構成でき、しかも、各活物質充
填単位工程における同じ工程による処理を共用の
装置で行うので、作業条件が同じになり、品質管
理を効果的に行える。
[Effects of the Invention] As described above, according to the present invention, the active material filling operation in the active material filling unit process is repeatedly performed on the sintered substrate along the meandering production line, and Since the same processes arranged in orthogonal directions are performed by shared equipment, the manufacturing equipment can be constructed at low cost with fewer control devices than in the past, and the same process in each active material filling unit process Since the processing is carried out using shared equipment, the working conditions are the same and quality control can be carried out effectively.

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

第1図は本発明の製造方法を実施するための装
置の概略説明図、第2図は本発明の製造方法にお
ける各処理液槽に焼結基板を挿入する状態を示す
説明図、第3図及び第4図はそれぞれ従来の製造
方法を示す説明図、第5図は従来の製造方法にお
ける各処理液槽に焼結基板を挿入する状態を示す
説明図である。 1……含浸工程、2……電解工程、3……水洗
工程、4……乾燥工程、5……活物質充填単位工
程、6……製造ライン、6A,6B……平行なラ
イン部分(往路ライン部分、復路ライン部分)、
8……帯板状焼結基板、8a……帯板状焼結基板
の板面。
FIG. 1 is a schematic explanatory diagram of an apparatus for implementing the manufacturing method of the present invention, FIG. 2 is an explanatory diagram showing a state in which a sintered substrate is inserted into each treatment liquid tank in the manufacturing method of the present invention, and FIG. 3 and FIG. 4 are explanatory diagrams showing the conventional manufacturing method, respectively, and FIG. 5 is an explanatory diagram showing a state in which a sintered substrate is inserted into each treatment liquid tank in the conventional manufacturing method. 1...Impregnation process, 2...Electrolysis process, 3...Water washing process, 4...Drying process, 5...Active material filling unit process, 6...Production line, 6A, 6B...Parallel line portion (outward route) line part, return line part),
8... Strip-shaped sintered substrate, 8a... Plate surface of the strip-shaped sintered substrate.

Claims (1)

【特許請求の範囲】 1 帯板状焼結基板に活物質の塩の溶液を含浸す
る含浸工程と、該含浸工程で活物質の塩の溶液の
含浸を行つた焼結基板に電解処理を行う電解工程
と、電解処理が行なわれた焼結基板を水洗する水
洗工程と、該水洗工程を経た焼結基板を乾燥する
乾燥工程とを活物質充填単位工程として製造ライ
ンに沿つて前記活物質充填単位工程を複数回繰り
返すことにより活物質充填作業を繰り返し行つて
活物質を前記焼結基板に充填するアルカリ蓄電池
用焼結式基板の製造方法において、 前記製造ラインを蛇行させて該蛇行した製造ラ
インに沿つて前記各活物質充填単位工程による活
物質充填作業を繰り返し行い、 蛇行した前記製造ラインの平行なライン部分に
対して直交する方向に並ぶ同じ工程による処理を
共用の装置によつてそれぞれ行い、 且つ、前記焼結基板はその板面を起立させて前
記各活物質充填単位工程に送り込むことを特徴と
するアルカリ蓄電池用焼結式極板の製造方法。
[Claims] 1. An impregnation step in which a strip-shaped sintered substrate is impregnated with a solution of a salt of an active material, and an electrolytic treatment is performed on the sintered substrate impregnated with a solution of a salt of an active material in the impregnation step. The active material filling process is carried out along the manufacturing line as an active material filling unit process including an electrolytic process, a washing process of washing the electrolytically treated sintered substrate with water, and a drying process of drying the sintered substrate after the washing process. A method for manufacturing a sintered substrate for an alkaline storage battery, in which the sintered substrate is filled with the active material by repeating the active material filling operation multiple times by repeating a unit process a plurality of times, the manufacturing line being meandered; The active material filling operation by each active material filling unit process is repeated along the line, and the processing by the same process in the direction orthogonal to the parallel line part of the meandering manufacturing line is performed using a shared device. and a method for manufacturing a sintered electrode plate for an alkaline storage battery, characterized in that the sintered substrate is sent to each of the active material filling unit processes with its plate surface erected.
JP60170459A 1985-08-01 1985-08-01 Manufacture of sintered plate for alkaline storage battery Granted JPS6231948A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60170459A JPS6231948A (en) 1985-08-01 1985-08-01 Manufacture of sintered plate for alkaline storage battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60170459A JPS6231948A (en) 1985-08-01 1985-08-01 Manufacture of sintered plate for alkaline storage battery

Publications (2)

Publication Number Publication Date
JPS6231948A JPS6231948A (en) 1987-02-10
JPH0566715B2 true JPH0566715B2 (en) 1993-09-22

Family

ID=15905325

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60170459A Granted JPS6231948A (en) 1985-08-01 1985-08-01 Manufacture of sintered plate for alkaline storage battery

Country Status (1)

Country Link
JP (1) JPS6231948A (en)

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