JPS603861A - Manufacture of positive plate for alkaline storage battery - Google Patents
Manufacture of positive plate for alkaline storage batteryInfo
- Publication number
- JPS603861A JPS603861A JP58112249A JP11224983A JPS603861A JP S603861 A JPS603861 A JP S603861A JP 58112249 A JP58112249 A JP 58112249A JP 11224983 A JP11224983 A JP 11224983A JP S603861 A JPS603861 A JP S603861A
- Authority
- JP
- Japan
- Prior art keywords
- base plate
- active material
- thermal decomposition
- temperature
- positive
- 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.)
- Pending
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/24—Electrodes for alkaline accumulators
- H01M4/26—Processes of manufacture
- H01M4/28—Precipitating active material on the carrier
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy 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
Description
【発明の詳細な説明】
本発明は、アルカリ蓄電池の陽極板の含浸工程に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an impregnation process for anode plates of alkaline storage batteries.
従来、アルカリ蓄電池陽極板の陽極活物質の含浸法とし
ては、溶融含浸法が行なわれている。Conventionally, a melt impregnation method has been used as a method for impregnating an anode active material of an anode plate of an alkaline storage battery.
溶融含浸法は、溶融塩を含浸し、これを熱分解する方法
で、含浸工程が簡単であるという特徴をもっている。す
なわち、多孔性焼結基板を硝酸コバルトを含む80〜1
00℃の溶融硝酸ニッケル中に約5分間浸漬し、基板の
気孔中に硝酸ニッケルを含浸する。続いて、この基板を
空気中で180〜250Cに加熱して熱分解する。熱分
解終了後、60〜70℃のアルカリ水溶液中に浸漬して
、活物質である水酸化ニッケルを基板の気孔中に含浸析
出し、流水中で気孔中のアルカリ成分がなくなるまで水
洗し、乾燥を行なう。この操作を3〜5回経返し、所定
の活物質を含浸するものである。The melt impregnation method is a method in which a molten salt is impregnated and then thermally decomposed, and the impregnation process is simple. That is, the porous sintered substrate was heated to 80-1 containing cobalt nitrate.
The substrate is immersed in molten nickel nitrate at 00° C. for about 5 minutes to impregnate nickel nitrate into the pores of the substrate. Subsequently, this substrate is heated to 180 to 250 C in air to thermally decompose it. After thermal decomposition, the substrate is immersed in an alkaline aqueous solution at 60 to 70°C to impregnate and precipitate the active material nickel hydroxide into the pores of the substrate, washed under running water until the alkaline component in the pores disappears, and dried. Do the following. This operation is repeated 3 to 5 times to impregnate the desired active material.
しかし、この方法によると、熱分解の際に。However, according to this method, during pyrolysis.
硝酸根の分解によって、基板を損なうので、活物質利用
率が低く、また窒素酸化物を除去するための公害防止装
置が必要になるなどの極板の特性上および製造費用上の
欠点がある。Decomposition of nitrate radicals damages the substrate, resulting in a low active material utilization rate and the need for a pollution prevention device to remove nitrogen oxides, which has drawbacks in terms of electrode plate characteristics and manufacturing costs.
本発明は、上記の欠点を除去するもので、中間乾燥温度
を下げることによって、活物質利用率の向上、製造費用
の低減をするものである。The present invention eliminates the above drawbacks and improves the active material utilization rate and reduces manufacturing costs by lowering the intermediate drying temperature.
第1図は多孔性焼結基板に含浸される溶融硝酸ニッケル
の示差熱分析と熱重量分析の結果を示した曲線図である
。1は熱重量分析による熱分解曲線、2に示差熱分折曲
iを示している。FIG. 1 is a curve diagram showing the results of differential thermal analysis and thermogravimetric analysis of molten nickel nitrate impregnated into a porous sintered substrate. 1 shows the thermal decomposition curve obtained by thermogravimetric analysis, and 2 shows the differential thermal refraction curve i.
含浸された硝酸ニッケルは、熱分解の温度が180〜2
50℃の温度領域3になると、次のような反応式によっ
て、中間化合物になり、窒素酸化物を発生する。Impregnated nickel nitrate has a thermal decomposition temperature of 180-2
In temperature range 3 of 50° C., it becomes an intermediate compound and generates nitrogen oxide according to the following reaction formula.
2 N j (Now) t・6H10→2Ni (O
H)NOs+2NO,+5H,O+7°・
これ以上の温度領域5になると、不活性な酸化ニッケル
となる。2 N j (Now) t・6H10→2Ni (O
H) NOs+2NO,+5H,O+7°・When the temperature reaches 5 or higher, it becomes inactive nickel oxide.
このため、180°〜250℃の温度領域3とこれ以下
の温度領域4の差異による影響を比較検討するために、
100℃と200℃の熱分解温度を選択した。Therefore, in order to compare and study the influence of the difference between the temperature range 3 of 180° to 250°C and the temperature range 4 below this,
Pyrolysis temperatures of 100°C and 200°C were chosen.
第2図は熱分解時間と含浸量の関係を示した曲線図であ
る。なお、電池を組立て、電池の性能を検d−Jするた
めに、電池の型式は、密閉形ニッケルΦカドミウム蓄電
池のNR−8C形として、第2図以下の結果を記載して
いる。従来の熱分解温度200℃の場合、短時間で含浸
されるが、熱分解時間が長くなっても増大しない。FIG. 2 is a curve diagram showing the relationship between the thermal decomposition time and the amount of impregnation. In order to assemble the battery and test the performance of the battery, the battery type is NR-8C, a sealed nickel Φ cadmium storage battery, and the results shown in Figure 2 and below are shown. In the case of the conventional thermal decomposition temperature of 200° C., impregnation occurs in a short time, but the impregnation does not increase even if the thermal decomposition time becomes longer.
しかし、熱分解温度100℃の場合、熱分解時間が長く
なると、含浸量の増加が認められ、従来の時間、1時間
では、熱分解温度100℃の方が、含浸量はやや多くな
っている。However, when the pyrolysis temperature is 100℃, the amount of impregnation increases as the pyrolysis time becomes longer, and at the conventional time of 1 hour, the amount of impregnation is slightly larger when the pyrolysis temperature is 100℃. .
第3図は、熱分解時間と活物質利用率の関係を示玄した
曲線図である。従来の熱分解温度。FIG. 3 is a curve diagram showing the relationship between thermal decomposition time and active material utilization rate. Conventional pyrolysis temperature.
200℃の場合、熱分解時間が長くなると、活物質利用
率が低下していくこと、また、熱分解温度100℃の場
合、逆に、熱分解時間が長(なると、活物質利用率が増
加する。そして、従来の時間、1時間では1両者の差は
、約15%もあることが認められる。In the case of 200°C, as the thermal decomposition time becomes longer, the active material utilization rate decreases, and in the case of a thermal decomposition temperature of 100°C, conversely, the thermal decomposition time becomes longer (and the active material utilization rate increases). In the conventional time, one hour, it is recognized that the difference between the two is about 15%.
第4図は熱分解温度100℃と200℃で製作した陽極
板に、陽極板よりも2倍以上の容量をもつ陰極板と電解
液に水酸化カリウム水溶液を用いて、電池を組立て、電
池の0.2 C放電における放電容量と熱分解時間の関
係を示した曲線図である。Figure 4 shows how a battery is assembled using an anode plate made at pyrolysis temperatures of 100°C and 200°C, a cathode plate with a capacity more than twice that of the anode plate, and an aqueous potassium hydroxide solution as an electrolyte. It is a curve diagram showing the relationship between discharge capacity and thermal decomposition time in 0.2 C discharge.
、、、、□、、1200’C(7)□、2□□、。 1
短時間で放電容量が上昇するが、熱分解時間が長くなる
と、放電容量が減少していくことが認められ、熱分解温
度100℃の場合、熱分解時間が長くなると、放電容量
が増加し、熱分解時間か1時間のとき、200℃の場合
より多いことがわかる。,,,,□,,1200'C(7)□,2□□,. 1
Although the discharge capacity increases in a short period of time, it is observed that the discharge capacity decreases as the thermal decomposition time increases.When the thermal decomposition temperature is 100°C, the discharge capacity increases as the thermal decomposition time increases. It can be seen that when the thermal decomposition time is 1 hour, the amount is greater than when the temperature is 200°C.
上述したように、本発明によれば、陽極活物質の利用率
が向上し、従来のものより、電池性能が向上すること、
および従来発生していた窒素酸化物の発生がなくなり公
害防止設備が減少すること等製造費用が低減するなど、
それらの効果は甚だ大なるものである。As described above, according to the present invention, the utilization rate of the anode active material is improved, and the battery performance is improved compared to the conventional one.
In addition, production costs are reduced due to the elimination of the production of nitrogen oxides that were previously generated, and the reduction of pollution prevention equipment.
Their effects are enormous.
第1図は硝酸ニッケルの示差熱分科と熱重量分析の結果
を示す曲線図、1は、熱重量分析による熱分解曲線、2
は、示差熱分析曲線、3は頗
180℃〜250℃の温度職域、4は、3より低温の温
度領域、5は3より高温の温度領域、をそれぞれ示す。
第2図は熱分解時間と含浸量の関係を示す曲線図、第3
図は熱分解時間と活物質利用率との関係を示す曲線図、
第4図は電池の放電容量と熱分解時間の関係を示す曲線
図である。
lは熱重量分析による熱分解曲線、2は示差熱分析曲線
、3は180〜250℃のff!I ’t)解温度領域
、4は温度領域3以下の温度領域、5は温度領域3以上
の温度領域
特許出願人
第2図
時間(猟Tl)
第3図
第4図
時間(甑π)Figure 1 is a curve diagram showing the results of differential thermal analysis and thermogravimetric analysis of nickel nitrate, 1 is the thermal decomposition curve by thermogravimetric analysis, 2
3 shows a differential thermal analysis curve, 3 shows a temperature range of 180°C to 250°C, 4 shows a temperature range lower than 3, and 5 shows a temperature range higher than 3. Figure 2 is a curve diagram showing the relationship between thermal decomposition time and amount of impregnation.
The figure is a curve diagram showing the relationship between thermal decomposition time and active material utilization rate.
FIG. 4 is a curve diagram showing the relationship between battery discharge capacity and thermal decomposition time. 1 is the thermal decomposition curve determined by thermogravimetric analysis, 2 is the differential thermal analysis curve, and 3 is the ff! of 180 to 250°C. I't) Solution temperature range, 4 is the temperature range below temperature range 3, 5 is the temperature range above temperature range 3 Patent applicant Figure 2 Time (Tl) Figure 3 Figure 4 Time (Koshiki π)
Claims (1)
熱分解の温度を下げて窒素酸化物の発生を抑えることを
特徴とするアルカリ蓄電池陽極板の製造法。In the process of impregnating the anode active material of the anode plate of an alkaline storage battery,
A method for producing an anode plate for an alkaline storage battery, which is characterized by lowering the thermal decomposition temperature and suppressing the generation of nitrogen oxides.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58112249A JPS603861A (en) | 1983-06-22 | 1983-06-22 | Manufacture of positive plate for alkaline storage battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58112249A JPS603861A (en) | 1983-06-22 | 1983-06-22 | Manufacture of positive plate for alkaline storage battery |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS603861A true JPS603861A (en) | 1985-01-10 |
Family
ID=14581975
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58112249A Pending JPS603861A (en) | 1983-06-22 | 1983-06-22 | Manufacture of positive plate for alkaline storage battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS603861A (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5560271A (en) * | 1978-10-31 | 1980-05-07 | Shin Kobe Electric Mach Co Ltd | Manufacturing method of plate for nickel cadmium storage battery |
-
1983
- 1983-06-22 JP JP58112249A patent/JPS603861A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5560271A (en) * | 1978-10-31 | 1980-05-07 | Shin Kobe Electric Mach Co Ltd | Manufacturing method of plate for nickel cadmium storage battery |
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