JPS6231948A - Manufacture of sintered plate for alkaline storage battery - Google Patents

Manufacture of sintered plate for alkaline storage battery

Info

Publication number
JPS6231948A
JPS6231948A JP60170459A JP17045985A JPS6231948A JP S6231948 A JPS6231948 A JP S6231948A JP 60170459 A JP60170459 A JP 60170459A JP 17045985 A JP17045985 A JP 17045985A JP S6231948 A JPS6231948 A JP S6231948A
Authority
JP
Japan
Prior art keywords
active material
sintered substrate
material filling
line
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.)
Granted
Application number
JP60170459A
Other languages
Japanese (ja)
Other versions
JPH0566715B2 (en
Inventor
Narifumi Matsuki
松木 成文
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)

Abstract

PURPOSE:To reduce the investment in production facilities and effectively perform quality control by repeating filling an active material in a sintered plate with a zigzagged production line, and conducting a treatment in the process which are arranged so as to intersect perpendicularly to the parallel parts of the zigzagged production line by common equipment. CONSTITUTION:After completion of the first active material filling unit process, the following filling unit processes are repeated several times to finish active material filling job. A supply direction of a substrate 8 in a proceeding line 6A is opposite to that in a returning line 6B, and an electrolytic process 2 is arranged in a straight line perpendicularly intersecting to the lines 6A and 6B. The electrolytic process 2 in each active material filling unit process is conducted in an electrolytic bath 22 serving as common equipment. Therefore, the investment in production facilities are reduced, and quality control is effectively performed because the same treatment is conducted with common equipment.

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vJ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 VJ manufacturing method for 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1 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
填中位工程5による処理を行わ<Tければならない。
[Prior art 1] Generally, in sintered electrode plates for alkaline storage batteries, the third
As shown in the figure, a strip-shaped sintered substrate is impregnated with a solution of a salt of an active material in an impregnation step 1, and then electrolytically treated in an electrolysis step 2. The sintered substrate subjected to the electrolytic treatment as described above is then washed with water in a washing step 3, and then 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 intermediate step 5 must be performed several times.

従って、従来では、活物質充填単位■f!115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に沿って活物質充l11tI11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Jように、複数のローラ7を用いて
帯板状焼結基板8を1下方向tこ折曲げて対応する槽9
内に挿入していた。
Therefore, conventionally, the active material filling unit ■f! In order to repeat step 115 several times, as shown in FIG. 4, step 5 of filling the active material was repeated along the linear production line 6 to sequentially fill the sintered substrates with the active material. In addition, in each step 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. 5, a plurality of rollers 7 are used. Bend the strip-shaped sintered substrate 8 downward one time to form a corresponding tank 9.
It was inserted inside.

[本発明が解決しようとする問題点1 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T稈
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hす、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
るホロ等の条件及び乾燥処理の条件をそれぞれ個々に制
御する必要があって制御ll装置が多くなり、製造装置
が高価になる問題点があった。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
問題点があった。
[Problem to be Solved by the Present Invention 1] However, in the above-mentioned conventional manufacturing method, since the manufacturing line 6 that repeatedly performs the active material filling unit process 5 is linear, the processing liquid tank and drying device of each T culm 5 are Therefore, the conditions such as the temperature and concentration of the active material salt solution, the electrolytic treatment conditions, the conditions such as hollowness in the water washing treatment, and the drying treatment conditions must be adjusted. Each of these needs to be controlled individually, resulting in a large number of control devices, which poses a problem in that the manufacturing equipment becomes expensive. Moreover, there is a problem in that the working conditions in each process tend to vary, making it difficult to effectively control quality.

本発明の目的(,1、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。
The purpose of the present invention is to propose a method for manufacturing sintered electrode plates for alkaline storage batteries, which allows a manufacturing apparatus to be constructed at low cost and allows for effective quality control.

E問題点を解決り゛るための手段1 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、水洗を行った後乾燥
を施す活物質充填単位工程5を製造ライン6に沿って活
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って活物質を焼結基板8に充填す
るアルカ  iり蓄電池用焼結式基板の製造方法であっ
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に沿っ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
じ工程による処理を共用の装置によってそれぞれ行い、
■つ、焼結基板Bはその板面8aを起立させて各活物質
充填単位コ]稈5に送り込む。
Means for Solving Problem E 1 The present invention will be explained with reference to FIGS. 1 and 2 showing one embodiment thereof. The active material filling operation is repeated by repeating the active material filling unit step 5 multiple times along the production line 6, in which the active material filling unit step 5 is impregnated with a solution, sequentially subjected to electrolytic treatment, washed with water, and then dried. This is a method for manufacturing a sintered substrate for an alkaline storage battery, in which a sintered substrate 8 is filled with an active material using a sintered substrate. The active material filling operation in the active material filling unit process 5 is repeated, and the same process is performed in a direction perpendicular to the parallel line portion of the meandering production line 6 using a shared device.
(2) The sintered substrate B is fed into each active material filling unit culm 5 with its plate surface 8a erected.

[作 用1 上記のようにすると、蛇行した製造ライン6に沿って活
物質充填中位T稈5に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
装置によってそれぞれ行うので、従来に比して制御装置
を少む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。
[Function 1] By doing as described above, the active material filling operation by the active material filling medium T culm 5 is carried out along the meandering production line 6 to the sintered substrate 8.
Since the same processes are carried out repeatedly and lined up perpendicularly to the parallel line portions of the meandering production line 6 using shared equipment, fewer control devices are required than in the past, making the manufacturing equipment cheaper. Furthermore, since the same process in each active material filling unit process 5 is performed using a shared device, the working conditions are the same and quality control can be performed 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] Embodiments of the present invention will be described in detail below with reference to the drawings.

先ず、本発明の製造方法を行う各処即工程におt−J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。
First, the state in which a strip-shaped sintered substrate is inserted into a treatment liquid tank in each process of carrying out the manufacturing method of the present invention will be explained.

第2図に承ずように、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個のスリット13
を形成し、各スリット13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1ノでいる。この場合、スリット13
を構成する部材は、側v12に嵌め込まれたゴム等の弾
性体14からなっている。尚処理液槽11に形成するス
リット13の数は送給する焼結基板80枚数等によって
定められ、その数は任意である。
As shown in FIG. 2, two slits 13 each extend vertically in a pair of mutually opposing side walls 12 of the processing liquid tank 11.
is formed, and the sintered substrate is fed in the direction of the arrow through the strip-shaped sintered substrate 8 with the plate surface 8a raised up in each slit 13. In this case, slit 13
The member constituting the is made of an elastic body 14 such as rubber fitted into the side v12. The number of slits 13 formed in the processing liquid tank 11 is determined by the number of 80 sintered substrates to be fed, and the number is arbitrary.

次に、板?fii8a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= 6− 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T
稈2、水洗工程3及び乾燥T稈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J二う
になっている。そこで、このにうな製造ライン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
入覆る。(この際、陽極板を成形する場合には、硝酸ニ
ッケル飽和溶液に焼結基板8を浸漬し、陰極板を成形覆
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を浸漬り゛る。)次いで、電解工程
2の電解槽22に焼11!l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1−稈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]二程4
の乾燥装置24によって乾燥作業を行う。このようにし
て、1回目の活物質充1?Mre位工稈5が終了り′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
けて数回行って焼結基板8に対する活物質充填作業を完
了Jる。
Next, the board? A method of filling the active material into the strip-shaped sintered substrate 8 that is fed by standing up the fii 8a will be described. 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 outgoing line of this meandering manufacturing line 6 = 6- Portion 6A and incoming line The portions 6B are arranged parallel to each other. In this production line 6, impregnation step 1, electrolytic T
The active material filling operation in the active material filling unit step 5 consisting of the culm 2, water washing step 3, and drying T culm 4 is performed several times in succession. Therefore, in order to fill the sintered substrate 8 with the active material in this production line 6, first, in the impregnation step 1, the strip-shaped sintered substrate 8 is inserted into the active material salt solution bath 21 and covered. (At this time, when molding the anode plate, the sintered substrate 8 is immersed in a saturated solution of nickel nitrate, and when molding and covering the cathode plate, the sintered substrate 8 is immersed in a saturated solution of cadmium nitrate or cadmium chloride. ) Next, the electrolytic bath 22 of the electrolysis step 2 is heated with 11! l Insert the board 8. (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 1-culm 3 and washed with water. The sintered substrate 8 that has been washed with water is dried] Step 2
The drying operation is performed by a drying device 24. In this way, the active material is charged for the first time. When the Mre mill 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に対して自交する直線上
に位置することになる。従って、各活物質充vJ4甲位
T稈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
は活物質充用単位−[稈5の数に応じて焼結基板8を通
1スリット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613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1!ながら送給しく′所定
回数の活物質充IIW甲位T稈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,
Of the processing steps performed in sequence, the electrolysis step 2 is located on a straight line that intersects with the outgoing line portion 6A and the returning line portion 6B. Therefore, each electrolytic process 2 in each active material charge VJ4 T culm 5 is performed in the electrolytic cell 22 as one shared device. In this case, in the electrolytic bath 22, the number of slits 13 through which the sintered substrate 8 is passed is set according to the active material filling unit - the number of culms 5. It is shared by the turn portion 6C of each sintered substrate 8 at the boundary from the outbound line portion 6A to the return line portion 6B, and the turn portion 6D of each sintered substrate 8 at the boundary from the inbound line portion 613 to the outbound line portion 6A. A drying device 24.24 is arranged to perform the drying process 4. In this way, the sintered substrate 8 is meandered in order from the outgoing line portion 6A to the incoming line portion 6B! While feeding, the active material filling operation using the active material filling IIW upper T culm 5 is carried out a predetermined number of times.

上記実施例において、名処理液槽には縦にスリット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、散出する処理液を器状部材で受けてポ
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, the processing liquid tank has a vertical slit 13.
is formed, the processing liquid may spill out to the outside. In this case, it is recommended to catch the spilled processing liquid with a container-like member and return the processing liquid to the processing liquid tank using a pump, etc. .

尚、上記実施例においては、蛇行りる製造ライン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T稈4による
処理を2個の共用装置どしての乾燥装置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6十のそれぞれの含浸工程1にJ、
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ってそれ
ぞれ行うようにすればよい。
In the above embodiment, the treatment by each electrolytic process 2 on the meandering production line 6 is performed in one electrolytic bath 22 as a shared device, and the treatment by each dry T culm 4 is performed by two Although the drying device 24.24 is used as a shared device, the present invention is not limited thereto, and J,
It is also possible to carry out the treatment in the active material salt solution tank as one shared device, and to perform the treatment in each washing step 3 in two washing tanks as shared devices, resulting in a meandering manufacturing process. The same processes arranged in a direction orthogonal to the parallel line portions of the line 6 may be performed using a shared device.

「発明の効宋] 以上のように本発明によれば、蛇行した製造ラインに沿
っ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
装置によってそれぞれ行うので、従来に化して制御装置
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 the parallel line portions of the meandering production line are Since the same processes arranged perpendicular to each other are carried out by shared equipment, the manufacturing equipment can be constructed at low cost by reducing the number of control devices compared to the conventional method. Since both processes are 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 the drawing]

第1図は本発明の製造方法を実施づ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檜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・・・vJ造プライン6A、6B・・・平行なライン
部分く往路ライン部分、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。 一’)Rn− 軸
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 processing liquid tank in the manufacturing method of the present invention, and FIG. 3 and FIG. 4 are explanatory views showing the conventional manufacturing method, respectively, and FIG. 5 is an explanatory view showing a state in which a sintered substrate is inserted into each processing liquid cylinder 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... vJ manufacturing lines 6A, 6B... parallel line portions, outward line portions, return line portions), 8... strip-shaped sintered substrate, 8a... plate of strip-shaped sintered substrate surface. 1') Rn- axis

Claims (1)

【特許請求の範囲】 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った焼結
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
ってそれぞれ行い、 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] An impregnation process in which a strip-shaped sintered substrate is impregnated with a solution of a salt of an active material, and an electrolysis process in which the sintered substrate impregnated with a solution of a salt of an active material in the impregnation process is electrolytically treated. The sintered substrate that has been electrolytically treated is washed with water, and the sintered substrate that has undergone the water washing step is dried. 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, the method comprising: making the manufacturing line meander; repeating the active material filling operation in each of the active material filling unit steps along the line, and performing the processing in the same step in a direction perpendicular to the parallel line portion of the meandering manufacturing line using a shared device, and A method for producing 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 true JPS6231948A (en) 1987-02-10
JPH0566715B2 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)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03151980A (en) * 1989-11-08 1991-06-28 Hiroshima Univ Magnetic force-driven artificial heart
JPH03165776A (en) * 1989-11-24 1991-07-17 Hiroshima Univ Motor-driven type artificial heart
JPH03176069A (en) * 1989-12-05 1991-07-31 Yoshiro Nakamatsu Artificial heart

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03151980A (en) * 1989-11-08 1991-06-28 Hiroshima Univ Magnetic force-driven artificial heart
JPH03165776A (en) * 1989-11-24 1991-07-17 Hiroshima Univ Motor-driven type artificial heart
JPH0460671B2 (en) * 1989-11-24 1992-09-28 Univ Hiroshima
JPH03176069A (en) * 1989-12-05 1991-07-31 Yoshiro Nakamatsu Artificial heart

Also Published As

Publication number Publication date
JPH0566715B2 (en) 1993-09-22

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