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JPS6043630B2 - Manufacturing method for electrode plates for nickel-cadmium storage batteries - Google Patents
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JPS6043630B2 - Manufacturing method for electrode plates for nickel-cadmium storage batteries - Google Patents

Manufacturing method for electrode plates for nickel-cadmium storage batteries

Info

Publication number
JPS6043630B2
JPS6043630B2 JP53134265A JP13426578A JPS6043630B2 JP S6043630 B2 JPS6043630 B2 JP S6043630B2 JP 53134265 A JP53134265 A JP 53134265A JP 13426578 A JP13426578 A JP 13426578A JP S6043630 B2 JPS6043630 B2 JP S6043630B2
Authority
JP
Japan
Prior art keywords
nickel
electrode plates
impregnation
storage batteries
manufacturing
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
Application number
JP53134265A
Other languages
Japanese (ja)
Other versions
JPS5560271A (en
Inventor
利明 島
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 JP53134265A priority Critical patent/JPS6043630B2/en
Publication of JPS5560271A publication Critical patent/JPS5560271A/en
Publication of JPS6043630B2 publication Critical patent/JPS6043630B2/en
Expired 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
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/58Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • 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
    • 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

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

Description

【発明の詳細な説明】 本発明はニッケルカドミウム蓄電池用の陽極板及ひ陰極
板の製造法に係り、特に一連の工程の操作回数少にして
電極基板の多孔部に活物質を多量に含浸せしめ、従つて
製造工程の簡略化および時間の短縮をはかることを目的
とするものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing an anode plate and a cathode plate for a nickel-cadmium storage battery, and in particular, it impregnates a large amount of active material into the pores of an electrode substrate by reducing the number of operations in a series of steps. Therefore, the purpose is to simplify the manufacturing process and shorten the time.

従来、ニッケルカドミウム蓄電池用極板は、ニッケル等
の微粉末を焼結して多孔性基板となし、この多孔部に陽
極は水酸化ニッケル塩、陰極はカドミウム塩をそれぞれ
水溶液の形で含浸させるか又はこれらの塩類の溶融塩の
形で含浸させるかして保持させ、次いで上記の塩類を含
浸させた基板をアルカリ電解液中て電解又は熱分解して
活物質の状態となし、これを水洗乾燥するという様な一
連の操作を数回繰返して所定量の含浸量を得るように製
造していた。然しながら、上記前者の方法は一回の含浸
量が少ないため、6回以上の一の一連の反復操作を要し
て量産上極めて不利であり、又、後者の方法によれば熔
融塩中に長時間浸漬することを要し、1回目の含浸操作
では前者より多く含浸されるが、その以後は含浸効率が
極端に小さくなり、かつ必要な含浸量を得るに非常に長
時間を要していた。
Conventionally, electrode plates for nickel-cadmium storage batteries have been made by sintering fine powder of nickel or other material to form a porous substrate, and these porous parts are impregnated with nickel hydroxide salt for the anode and cadmium salt for the cathode in the form of an aqueous solution. Alternatively, these salts are impregnated in the form of a molten salt and retained, and then the substrate impregnated with the above salts is electrolyzed or thermally decomposed in an alkaline electrolyte to form an active material, which is then washed with water and dried. This series of operations was repeated several times to obtain a predetermined amount of impregnation. However, the former method requires a series of repetitions of 6 or more times as the amount of impregnation at one time is small, which is extremely disadvantageous in terms of mass production. It requires soaking for a long time, and the first impregnation operation results in more impregnation than the former, but after that, the impregnation efficiency becomes extremely low, and it takes a very long time to obtain the required amount of impregnation. .

即ち、第1図に示すように、従来の方法においては、含
浸工程A)電解工程B)水洗工程C)乾燥工程Dからな
る一連の工程を6回も反復するため、含浸工程以外の電
解工程および次の基板に付着した電解液を水洗する水洗
工程の操作工数および操作時間の全体に占める割合が大
きくなつて非能率的であつた。本発明は上記の欠点を除
去するためになされたもので、含浸工程で基板に含浸さ
れた活物質の塩類溶液は、電解工程において沈着固定す
る前でも、一旦乾燥することにより含浸操作の反復に耐
える程度に基板に保持することができることを見い出し
たことに基くものである。
That is, as shown in FIG. 1, in the conventional method, a series of steps consisting of the impregnation step A) electrolysis step B) washing step C) drying step D is repeated six times, so that the electrolysis step other than the impregnation step is In addition, the next step of washing the electrolytic solution adhering to the substrate with water takes up a large proportion of the operating man-hours and operating time, resulting in inefficiency. The present invention has been made to eliminate the above-mentioned drawbacks, and the salt solution of the active material impregnated into the substrate in the impregnation process can be dried even before it is deposited and fixed in the electrolytic process, thereby making it easier to repeat the impregnation operation. This is based on the discovery that it can be held to a substrate to a durable extent.

即ち、第2図示すように、本発明は、多孔性基・板を活
物質の塩類溶液に浸漬する含浸工程Aの後に、例えば1
00±2lCの温度の乾燥雰囲気中で乾燥する乾燥工程
D’を組み合せた操作を必要回数例えば2または3回繰
り返し、その後、電解工程B、水洗工程Cおよび乾燥工
程Dを経る一連の工ー程を3または4回程度繰返すこと
により極板を製造することができるものである。
That is, as shown in FIG. 2, in the present invention, for example, 1
A series of steps in which the combined operation of drying step D' of drying in a dry atmosphere at a temperature of 00±2 lC is repeated a necessary number of times, for example, 2 or 3 times, followed by electrolysis step B, water washing step C, and drying step D. An electrode plate can be manufactured by repeating this process about 3 or 4 times.

但し、含浸工程Aと乾燥工程D’の組み合せの反復につ
いては、それにおける反復最後の乾燥工程D″を省略す
ることもできることを含んでいる。
However, the repetition of the combination of impregnation step A and drying step D' includes the possibility of omitting the final drying step D'' of the repetition.

本発明の一実施例を陽極板について説明する。An embodiment of the present invention will be described with respect to an anode plate.

硝酸ニッケルN1(NO3)2・6H20を約70℃の
温度で熔融し、少量の水を添加して比重を約1.7に調
整しておく。先ずこの水溶液中カーボニルニツケル粉末
を焼結して成る多孔性基板を約1分間程度浸漬し、硝酸
ニッケル水溶液を含浸させる。次いでこの基板を約10
0±20′Cの温度の乾燥炉中で約3〜4分間乾燥し、
再び前記水溶液中に基板を浸漬する。浸漬後前記同様乾
燥炉に入れて乾燥し、次いでこの基板を陰極として、8
0℃濃度25%の苛性ソーダ水溶液中て2紛垣の電解行
い、水酸化ニッケル活物質を基板多孔部に沈着させ、こ
れを水洗乾燥する。上記一連の工程を3回繰返して陽極
板を得る。陰極板の場合も同様に硝酸カドミウムを用い
て含浸せしめれば良い。本発明による方法と従来法につ
いて基板の一連の工程の反復回数に対する活物質含浸量
の変化を二第3図に示す。
Nickel nitrate N1(NO3)2.6H20 is melted at a temperature of about 70°C, and a small amount of water is added to adjust the specific gravity to about 1.7. First, a porous substrate made by sintering carbonyl nickel powder in this aqueous solution is immersed for about 1 minute to impregnate it with the nickel nitrate aqueous solution. Next, this board was coated with about 10
Dry for about 3 to 4 minutes in a drying oven at a temperature of 0 ± 20'C,
The substrate is immersed in the aqueous solution again. After dipping, the substrate was placed in a drying oven to dry as described above, and then this substrate was used as a cathode for 8 hours.
Two batches of electrolysis are performed in a caustic soda aqueous solution having a concentration of 25% at 0° C. to deposit a nickel hydroxide active material in the porous portions of the substrate, which is washed with water and dried. The above series of steps is repeated three times to obtain an anode plate. In the case of the cathode plate, it may be similarly impregnated with cadmium nitrate. FIG. 3 shows changes in the amount of active material impregnated with respect to the number of repetitions of a series of substrate steps for the method according to the present invention and the conventional method.

本発明によるものXは従来法によるものYに比して一連
の工程の反復回数が半分にして、所定の含浸量が得られ
ることがわかる。また得られた極板について、活物質利
用率を測定したところ、本発明により得られた極板は8
4%〜992%となり、従来の極板の78〜90%に比
して約10%の特性向上をもたらした。なお本実施例に
おいて、乾燥工程の温度を約100±20℃とし、時間
を約3〜4分間としたのは、温度が120℃を越え且つ
長時間では含浸物質が不活性化して活物質の利用率が低
下する上に、基板の焼結体の一部が腐食し、極板の強度
劣化が発生する場合があるためであり、また温度が80
℃以下では含浸量を増加させるという効果があまり得ら
れないためである。
It can be seen that in the product X according to the present invention, the number of repetitions of the series of steps is halved compared to the product Y according to the conventional method, and a predetermined amount of impregnation can be obtained. Furthermore, when the active material utilization rate of the obtained electrode plate was measured, it was found that the electrode plate obtained according to the present invention was 8.
4% to 992%, resulting in an approximately 10% improvement in characteristics compared to 78 to 90% for conventional electrode plates. In this example, the temperature of the drying process was set to about 100±20°C and the time was set to about 3 to 4 minutes, because if the temperature exceeds 120°C and for a long time, the impregnated material becomes inactive and the active material deteriorates. This is because not only the utilization rate decreases but also a part of the sintered body of the board may corrode and the strength of the electrode plate may deteriorate.
This is because the effect of increasing the amount of impregnation cannot be obtained much below the temperature.

上述したように、電解は製造工程数および時間を簡略化
および短縮化して製造効率を向上させることができ、而
も特性を向上した極板を得ることができる点工業的価値
甚だ大なるものである。
As mentioned above, electrolysis can improve manufacturing efficiency by simplifying and shortening the number of manufacturing steps and time, and has great industrial value in that it can obtain electrode plates with improved characteristics. be.

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

第1図は従来のニッケルカドミウム蓄電池用極板の製造
法における工程を示す工程図、第2図は本発明における
工程を示す工程図、第3図は第1図および第2図におけ
る一連の工程の反復回数に対する活物質含浸量の変化を
示す比較曲線図てある。 Aは含浸工程、Bは電解工程、Cは水洗工程、D,D″
は乾燥工程、Xは本発明法によるもの、Yは従来法によ
るもの。
FIG. 1 is a process diagram showing the steps in the conventional manufacturing method of electrode plates for nickel-cadmium storage batteries, FIG. 2 is a process diagram showing the steps in the present invention, and FIG. 3 is a series of steps in FIGS. 1 and 2. 3 is a comparison curve showing the change in the amount of active material impregnated with respect to the number of repetitions. A is the impregnation process, B is the electrolysis process, C is the water washing process, D, D″
is the drying process, X is by the method of the present invention, and Y is by the conventional method.

Claims (1)

【特許請求の範囲】[Claims] 1 含浸工程、電解工程、水洗工程、乾燥工程の一連の
工程の反復からなるニッケルカドミウム蓄電池用極板の
製造法において、含浸工程と電解工程との間に含浸物質
が熱分解しない程度の温度および時間の乾燥工程を設け
、含浸工程と乾燥工程の組み合せを反復した後電解工程
に移行することを特徴とするニッケルカドミウム蓄電池
用極板の製造法。
1. In a method for manufacturing electrode plates for nickel cadmium storage batteries, which consists of repeating a series of steps of impregnation, electrolysis, washing, and drying, the impregnation step and electrolysis step are conducted at a temperature that does not cause thermal decomposition of the impregnated material. 1. A method for producing electrode plates for nickel-cadmium storage batteries, characterized by providing a drying step for a certain amount of time, repeating a combination of an impregnating step and a drying step, and then proceeding to an electrolytic step.
JP53134265A 1978-10-31 1978-10-31 Manufacturing method for electrode plates for nickel-cadmium storage batteries Expired JPS6043630B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP53134265A JPS6043630B2 (en) 1978-10-31 1978-10-31 Manufacturing method for electrode plates for nickel-cadmium storage batteries

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP53134265A JPS6043630B2 (en) 1978-10-31 1978-10-31 Manufacturing method for electrode plates for nickel-cadmium storage batteries

Publications (2)

Publication Number Publication Date
JPS5560271A JPS5560271A (en) 1980-05-07
JPS6043630B2 true JPS6043630B2 (en) 1985-09-28

Family

ID=15124248

Family Applications (1)

Application Number Title Priority Date Filing Date
JP53134265A Expired JPS6043630B2 (en) 1978-10-31 1978-10-31 Manufacturing method for electrode plates for nickel-cadmium storage batteries

Country Status (1)

Country Link
JP (1) JPS6043630B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS603861A (en) * 1983-06-22 1985-01-10 Shin Kobe Electric Mach Co Ltd Manufacture of positive plate for alkaline storage battery

Also Published As

Publication number Publication date
JPS5560271A (en) 1980-05-07

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