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
JPH0564422B2 - - Google Patents
[go: Go Back, main page]

JPH0564422B2 - - Google Patents

Info

Publication number
JPH0564422B2
JPH0564422B2 JP60170460A JP17046085A JPH0564422B2 JP H0564422 B2 JPH0564422 B2 JP H0564422B2 JP 60170460 A JP60170460 A JP 60170460A JP 17046085 A JP17046085 A JP 17046085A JP H0564422 B2 JPH0564422 B2 JP H0564422B2
Authority
JP
Japan
Prior art keywords
active material
sintered substrate
material filling
manufacturing
sintered
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
JP60170460A
Other languages
Japanese (ja)
Other versions
JPS6231949A (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 JP60170460A priority Critical patent/JPS6231949A/en
Publication of JPS6231949A publication Critical patent/JPS6231949A/en
Publication of JPH0564422B2 publication Critical patent/JPH0564422B2/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, an electrolytic treatment is performed in an electrolytic step 2. The sintered substrate that has been electrolytically treated 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, 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.

[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 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 sequentially installed. Therefore, the conditions such as the temperature and concentration of the salt solution of the active material, 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 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を渦巻状にして
該渦巻状の製造ライン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、
渦巻状の製造ライン6の重なり合うライン部分に
跨つて配置された共用の装置によつてそれぞれの
前記活物質充填単位工程のそれぞれの処理を行
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 formed into a spiral shape, and the active material filling operation by each active material filling unit process 5 is repeated along the spiral production line 6.
Each of the active material filling unit steps is performed by a shared device disposed across the overlapping line portions of the spiral production line 6, and the sintered substrate 8 is erected with its plate surface 8a. and sent to each active material filling unit process 5.

[作用] 上記のようにすると、渦巻状の製造ライン6に
沿つて活物質充填単位工程5による活物質充填作
業を焼結基板8に繰り返し行い、渦巻状の製造ラ
イン6の重なり合うライン部分に跨つて配置され
た共用の装置によつてそれぞれの処理を行うの
で、作業条件が同じになり、品質管理を効果的に
行うことができ、また、制御装置が少なくなつて
製造装置を安価に構成できる。
[Function] With the above method, the active material filling operation in the active material filling unit process 5 is repeatedly performed on the sintered substrate 8 along the spiral production line 6, and the active material filling operation is repeatedly performed on the sintered substrate 8 along the spiral production line 6, and the overlapping line portions of the spiral production line 6 are straddled. Since each process is carried out using shared equipment located in the same location, the working conditions are the same, quality control can be carried out effectively, and the manufacturing equipment can be configured at low cost since there are fewer control devices. .

[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が渦巻状に配置されている。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を浸漬し、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 spiral shape. This production line 6 includes an impregnation process 1, an electrolytic process 2,
The active material filling operation in the active material filling unit process 5 consisting of the water washing process 3 and the drying process 4 is performed several times in succession. Therefore, in such a manufacturing line 6, in order to fill the sintered substrate 8 with the active material, first, in the impregnation step 1, the active material salt solution bath 21 is filled.
A strip-shaped sintered substrate 8 is inserted into the sintered substrate 8. (At this time, when molding an anode plate, the sintered substrate 8 is immersed in a saturated solution of nickel nitrate; when molding a 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 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 to complete the active material filling operation on the sintered substrate 8. .

このような活物質充填作業を渦巻状の製造ライ
ン6上で行う際、重なり合うライン部分に跨るよ
うにして共用の装置としての、活物質の塩の溶液
槽21と電解槽22と水洗槽23と乾燥装置24
とを配置して焼結基板8をこれらの槽21,2
2,23及び装置24に繰返し通して所定回数の
活物質充填単位工程5による活物質充填作業を行
う。
When such active material filling work is performed on the spiral production line 6, the active material salt solution tank 21, electrolytic tank 22, and water washing tank 23 are used as common equipment so as to straddle the overlapping line parts. Drying device 24
and place the sintered substrate 8 in these tanks 21 and 2.
2, 23 and the device 24 to perform the active material filling operation in the active material filling unit process 5 a predetermined number of times.

上記実施例において、各処理液槽には縦スリツ
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 vertical slits 13 are formed in each processing liquid tank, the processing liquid may spill out to the outside. It is preferable that the processing liquid is returned to the processing liquid tank.

[発明の効果] 以上のように本発明によれば、渦巻状の製造ラ
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、渦巻状の製造
ラインの重なり合うライン部分に跨つて配置され
た共用の装置によつてそれぞれの処理を行うの
で、作業条件が同じになり、品質管理を効果的に
行うことができ、また、制御装置が少なくなつて
製造装置を安価に構成できる。
[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 repeated on the sintered substrate along the spiral production line, and the overlapping line portions of the spiral production line are Since each process is carried out using shared equipment located across multiple locations, the working conditions are the same and quality control can be carried out effectively.In addition, the number of control devices is reduced, making manufacturing equipment cheaper. Can be configured.

【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、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... Manufacturing line, 8... Band-shaped sintered substrate,
8a...Plate surface of a 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、 前記製造ラインを渦巻状にして該渦巻状の製造
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、 渦巻状の前記製造ラインの重なり合うライン部
分に跨つて配置された共用の装置によつてそれぞ
れの前記活物質充填単位工程のそれぞれの処理を
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. In 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 by repeating a unit process multiple times, the manufacturing line is formed into a spiral shape and the spiral shape is The active material filling operation in each of the active material filling unit steps is repeated along the production line, and each of the active material filling units is filled by a shared device disposed astride the overlapping line portions of the spiral production line. A method for manufacturing a sintered electrode plate for an alkaline storage battery, characterized in that each of the steps is performed, and the sintered substrate is sent to each of the active material filling unit steps with its plate surface erected.
JP60170460A 1985-08-01 1985-08-01 Manufacture of sintered plate for alkaline storage battery Granted JPS6231949A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60170460A JPS6231949A (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
JP60170460A JPS6231949A (en) 1985-08-01 1985-08-01 Manufacture of sintered plate for alkaline storage battery

Publications (2)

Publication Number Publication Date
JPS6231949A JPS6231949A (en) 1987-02-10
JPH0564422B2 true JPH0564422B2 (en) 1993-09-14

Family

ID=15905346

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60170460A Granted JPS6231949A (en) 1985-08-01 1985-08-01 Manufacture of sintered plate for alkaline storage battery

Country Status (1)

Country Link
JP (1) JPS6231949A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9823418D0 (en) * 1998-10-26 1998-12-23 Notetry Ltd Cyclonic seperating apparatus

Also Published As

Publication number Publication date
JPS6231949A (en) 1987-02-10

Similar Documents

Publication Publication Date Title
JPH0566715B2 (en)
KR890005305A (en) Process of electroplating metal
DE2862463D1 (en) Electrode for electrolytic processes, electrolysis cell and method for electrolysis
KR880013009A (en) Method and apparatus for measuring electrochemically active ingredient in process flow
DE19856840A1 (en) Wastewater treatment process and treatment apparatus therefor
JPH0564422B2 (en)
Vuković Rotating ring–disc electrode study of the enhanced oxygen evolution on an activated ruthenium electrode
GB1572756A (en) Electrolytic method and device for the treatment of effluent
US3671321A (en) Process for production and treatment of battery plates
US2760923A (en) Process and apparatus for reverse current protection of anodes in electropickling
US2559926A (en) Anode basket
US7341655B2 (en) Process for improving an electrode
US3979223A (en) Electrochemical impregnation of electrode for rechargeable cell
DE59107541D1 (en) Method and device for the electrolytic discharge of metals from a solution containing metal ions and electrode for carrying out the method
EP0445516B1 (en) Process and apparatus for the production of silver nitrate
US4172909A (en) Application of active mass to porous electrode support structures
DE1299739B (en) Process for impregnating porous nickel electrodes with active material
US5213666A (en) Method of preparing support for printing plate
DE1071840B (en) Process for the production of electrodes on semiconductor bodies of semiconductor arrangements
SU548294A1 (en) The method of electrochemical regeneration of ion exchanger
JPS61277160A (en) Manufacture of plate for alkaline storage battery
US3320139A (en) Method for preparing negative electrodes
DE2238236C3 (en) Process for electrophoretic coating of iron or steel workpieces with enamel
JPS5925172A (en) Manufacture of cadmium electrode for alkaline battery
DE4218916A1 (en) Process for electrolytic detoxification or regeneration of an aqueous solution containing cyanide and device for carrying out the process