JPS6120489B2 - - Google Patents
Info
- Publication number
- JPS6120489B2 JPS6120489B2 JP53056295A JP5629578A JPS6120489B2 JP S6120489 B2 JPS6120489 B2 JP S6120489B2 JP 53056295 A JP53056295 A JP 53056295A JP 5629578 A JP5629578 A JP 5629578A JP S6120489 B2 JPS6120489 B2 JP S6120489B2
- Authority
- JP
- Japan
- Prior art keywords
- manganese dioxide
- acid
- battery
- heat treatment
- treatment temperature
- 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
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
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/50—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese
- H01M4/502—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of manganese for non-aqueous cells
-
- 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
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Description
【発明の詳細な説明】
本発明は、リチウムなどの軽金属を負極活物質
とし、非水電解質を用いる電池の正極活物質に用
いられる二酸化マンガンの製造法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing manganese dioxide, which is used as a positive electrode active material in a battery that uses a light metal such as lithium as a negative electrode active material and uses a non-aqueous electrolyte.
一般に、非水電池用正極活物質として用いられ
る二酸化マンガンとしては、電解で得られたもの
を微分末状とし、さらに含有水分除去のために、
適度な熱処理を施したものを用いている。この熱
処理温度と二酸化マンガンの電気化学的活性、電
池保存性能の間には密接な関係があり、処理温度
が高いほど電池の保存に伴う放電性能劣化が少な
く、この傾向は高温保存の場合において特に顕著
である。しかし、処理温度が高くなると、電池の
高率放電特性が低下し、また保存に伴う電池内部
抵抗の増加も著しくなるなどの挙動が認められ
る。 In general, manganese dioxide used as a positive electrode active material for non-aqueous batteries is obtained by electrolysis and made into a differentiated powder, and further, in order to remove the water content,
We use materials that have undergone appropriate heat treatment. There is a close relationship between this heat treatment temperature, the electrochemical activity of manganese dioxide, and battery storage performance, and the higher the treatment temperature, the less deterioration in discharge performance associated with battery storage. Remarkable. However, as the treatment temperature increases, the high rate discharge characteristics of the battery deteriorates, and the internal resistance of the battery increases significantly during storage.
これらの原因として以下の理由が考えられる。
すなわち、二酸化マンガンに熱処理を施すと、結
晶中に含有される水分量は減少するが、同時に二
酸化マンガン粒子の表面積も大幅に減少するた
め、高温保存性能の向上に反して高率放電特性の
低下を伴うものと考えられる。さらにまた二酸化
マンガンは加熱によつて、2MnO2→Mn2O3+1/2O2
の反応により分解し、この反応は300〜400℃の温
度においても一部起こつているものと考えられ、
二酸化マンガン粒子表面では、電気化学的に不活
性な三二酸化マンガンMn2O3が生成しているもの
と考えられる。特に400〜450℃の温度で処理した
二酸化マンガンを用いた電池における、高率放電
特性の低下、及び保存に伴う電池内部インピーダ
ンスの増大は、上記Mn2O3の生成に起因するとこ
ろが大きいものと考えられる。 The following reasons can be considered as these causes.
In other words, when manganese dioxide is heat-treated, the amount of water contained in the crystals decreases, but at the same time, the surface area of the manganese dioxide particles also decreases significantly, resulting in a decrease in high-rate discharge characteristics while improving high-temperature storage performance. It is thought that this is accompanied by Furthermore, manganese dioxide is decomposed by the reaction of 2MnO 2 →Mn 2 O 3 + 1/2O 2 when heated, and this reaction is thought to partially occur at temperatures of 300 to 400°C.
It is considered that electrochemically inactive manganese sesquioxide Mn 2 O 3 is generated on the surface of the manganese dioxide particles. In particular, in batteries using manganese dioxide treated at temperatures of 400 to 450°C, the decrease in high-rate discharge characteristics and the increase in battery internal impedance with storage are largely due to the formation of Mn 2 O 3 mentioned above. Conceivable.
本発明は、電解二酸化マンガンに熱処理を施し
た後、Mn2O3を溶解し不均化反応を起こさない酸
で酸処理を施すことにより、二酸化マンガン粒子
表面に生成したMn2O3を溶解除去し、高率放電特
性、正極利用率、保存性能に優えた性質を有する
二酸化マンガンを提供するものである。 The present invention dissolves Mn 2 O 3 generated on the surface of manganese dioxide particles by heat treating electrolytic manganese dioxide and then performing acid treatment with an acid that dissolves Mn 2 O 3 and does not cause a disproportionation reaction. The object of the present invention is to provide manganese dioxide having excellent properties such as high rate discharge characteristics, positive electrode utilization rate, and storage performance.
Mn2O3は熱処理二酸化マンガンを、塩酸、弗
酸、臭酸等で処理することにより簡単に除去する
ことができる。硫酸によつても除去することがで
きるが、この場合には不均化反応によつてMnO2
が生成し、このMnO2は熱処理二酸化マンガンと
は結晶構造が異なり、非水電池用活物質として不
適当な性質を有するものであつた。塩酸、弗酸、
臭酸を用いると、Mn2O3とともにMnO2も溶解す
るが、粒子表面層が溶解するにとどめるので、特
に問題とならない。 Mn 2 O 3 can be easily removed by treating heat-treated manganese dioxide with hydrochloric acid, hydrofluoric acid, hydrochloric acid, etc. It can also be removed with sulfuric acid, but in this case MnO 2 is removed by a disproportionation reaction.
was produced, and this MnO 2 had a crystal structure different from that of heat-treated manganese dioxide and had properties unsuitable as an active material for non-aqueous batteries. Hydrochloric acid, hydrofluoric acid,
When hydrochloric acid is used, MnO 2 is dissolved together with Mn 2 O 3 , but this does not pose a particular problem since only the particle surface layer is dissolved.
以下本発明をその実施例により説明する。 The present invention will be explained below with reference to Examples.
電解二酸化マンガンを、200℃,250℃,300
℃,350℃,400℃,450℃の各温度にてガラスボ
ード中でそれぞれ8時間熱処理し、これら熱処理
二酸化マンガンを、1規定塩酸中に浸漬し、20℃
にて1〜2時間処理する。ろ過の後、十分水洗し
て塩酸分を除去した後、80℃にて乾燥した。 Electrolytic manganese dioxide at 200℃, 250℃, 300℃
℃, 350℃, 400℃, and 450℃ for 8 hours each in a glass board.The heat-treated manganese dioxide was immersed in 1N hydrochloric acid and heated at 20℃.
Treat for 1 to 2 hours. After filtration, it was thoroughly washed with water to remove hydrochloric acid, and then dried at 80°C.
前記二酸化マンガンを用いて以下の様に電池を
製造した。二酸化マンガン100重量部に対し、導
電材としてアセチレンブラツク8重量部、フツ素
樹脂6重量部を混合したものを加圧成型し、容量
150mAhの正極とした。負極には、圧延リチウム
板を所定の寸法に切断したものを使用した。また
電解液としては、プロピレンカーボネートとジメ
トキシエタンの体積比1:1の混合液に過塩素酸
リチウムを1.0モル/溶解したものを用いた。
この本発明による二酸化マンガンを用いた電池を
Aとする。比較のため、前記と同様の熱処理を施
し酸処理を施さない従来法による二酸化マンガン
を用いて同様に製造した電池をBとする。 A battery was manufactured using the manganese dioxide as described below. A mixture of 100 parts by weight of manganese dioxide, 8 parts by weight of acetylene black as a conductive material, and 6 parts by weight of fluororesin is pressure molded, and the volume
The positive electrode was 150mAh. For the negative electrode, a rolled lithium plate cut into predetermined dimensions was used. The electrolytic solution used was a mixture of propylene carbonate and dimethoxyethane in a volume ratio of 1:1 in which 1.0 mole of lithium perchlorate was dissolved.
A battery using manganese dioxide according to the present invention is designated as A. For comparison, a battery B was manufactured in the same manner using manganese dioxide by the conventional method, which was subjected to the same heat treatment as described above but without acid treatment.
第1図は、二酸化マンガンの熱処理温度と電池
を60℃で1ヵ月保存した場合の電池内部抵抗の変
化を示す。電池製造直後においてはA,Bいずれ
の電池においてもほとんど差が認められないが、
保存後においては、電池Aの内部抵抗の増加は小
さく、特に300℃以上の熱処理温度の場合に顕著
な差異が認められる。300℃以下の熱処理温度の
場合の内部抵抗増加は、主として、二酸化マンガ
ン中の残存水分によるものであり、300℃以上の
場合には二酸化マンガン分解生成物に起因するも
のと考えられ、熱処理温度が高くなるほど、酸処
理の効果が大きいことが説明できる。 Figure 1 shows the change in battery internal resistance when the manganese dioxide heat treatment temperature and the battery were stored at 60°C for one month. Immediately after battery manufacture, there is almost no difference between batteries A and B, but
After storage, the increase in internal resistance of battery A is small, and a significant difference is observed especially when the heat treatment temperature is 300° C. or higher. The increase in internal resistance at a heat treatment temperature of 300℃ or lower is mainly due to residual moisture in manganese dioxide, and at a heat treatment temperature of 300℃ or higher, it is thought to be due to manganese dioxide decomposition products. It can be explained that the higher the value, the greater the effect of acid treatment.
第2図は、熱処理温度が450℃の場合のそれぞ
れの電池A,Bについて、製造直後と、60℃で
1ヵ月保存後の500Ω定抵抗放電特性を示す。図
より明らかなごとく、製造直後および保存後のい
ずれにおいても、酸処理二酸化マンガンを用いた
電池Aの方が、平坦電圧で約50mV高く、利用率
で約10%大きいなど酸処理効果の大なることが判
かる。 FIG. 2 shows the 500Ω constant resistance discharge characteristics of batteries A and B immediately after manufacture and after storage at 60°C for one month when the heat treatment temperature was 450°C. As is clear from the figure, both immediately after manufacture and after storage, battery A using acid-treated manganese dioxide has a higher flat voltage of about 50 mV and a utilization rate of about 10% higher, showing that the acid treatment has a greater effect. I understand that.
Mn2O3を除去するために塩酸の他に弗酸、臭酸
を用いても前記と同様の効果を得ることができ
た。酸処理においては、Mn2O3を溶解し、かつ、
不均化反応を起こさない酸であればいずれの酸で
も用いることができる。 The same effect as described above could be obtained by using hydrofluoric acid or hydrochloric acid in addition to hydrochloric acid to remove Mn 2 O 3 . In acid treatment, Mn 2 O 3 is dissolved and
Any acid that does not cause a disproportionation reaction can be used.
熱処理温度を500℃程度にすると、二酸化マン
ガンの分解が顕著となり不適当であり、また250
℃前後では水分の除去が不十分となる。以上より
処理温度としては、300〜450℃が適当であり、こ
の温度範囲では、十分に水分を除去することがで
き、かつ酸処理効果も大きい。 If the heat treatment temperature is about 500℃, the decomposition of manganese dioxide will be significant, which is inappropriate.
Moisture removal becomes insufficient at temperatures around ℃. From the above, a suitable treatment temperature is 300 to 450°C; in this temperature range, moisture can be removed sufficiently and the acid treatment effect is also large.
以上のごとく、本発明は、熱処理によつて二酸
化マンガン粒子表面に生成したMn2O3などの酸素
不足型化合物を、酸処理によつて除去することに
より、正極利用率、高率放電特性、保存性能のい
ずれにも優れた性質を有する非水電池用二酸化マ
ンガンを、容易に提供するものである。 As described above, the present invention improves the positive electrode utilization rate, high rate discharge characteristics, and improves the positive electrode utilization rate and high rate discharge characteristics by removing oxygen-deficient compounds such as Mn 2 O 3 generated on the surface of manganese dioxide particles by heat treatment using acid treatment. The object of the present invention is to easily provide manganese dioxide for non-aqueous batteries that has excellent properties in terms of storage performance.
第1図は二酸化マンガンの熱処理温度を保存に
伴う電池内部抵抗の関係を示す図、第2図は、製
造直後および保存後の電池について500Ω定抵抗
放電特性を示す。
FIG. 1 shows the relationship between the heat treatment temperature of manganese dioxide and the internal resistance of the battery depending on storage, and FIG. 2 shows the 500Ω constant resistance discharge characteristics of the battery immediately after manufacture and after storage.
Claims (1)
Mn2O3を溶解しかつ不均化反応を起こさない酸で
酸処理を施すことを特徴とする非水電池用二酸化
マンガンの製造法。 2 熱処理温度が、300〜450℃である特許請求の
範囲第1項記載の非水電池用二酸化マンガンの製
造法。 3 酸が、塩酸、弗酸および臭酸よりなる群から
選択したものである特許請求の範囲第1項または
第2項記載の非水電池用二酸化マンガンの製造
法。[Claims] 1. After heat-treating electrolytic manganese dioxide,
A method for producing manganese dioxide for non-aqueous batteries, characterized by performing acid treatment with an acid that dissolves Mn 2 O 3 and does not cause a disproportionation reaction. 2. The method for producing manganese dioxide for nonaqueous batteries according to claim 1, wherein the heat treatment temperature is 300 to 450°C. 3. The method for producing manganese dioxide for nonaqueous batteries according to claim 1 or 2, wherein the acid is selected from the group consisting of hydrochloric acid, hydrofluoric acid, and hydrobromic acid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5629578A JPS54147197A (en) | 1978-05-11 | 1978-05-11 | Manufacture of manganese dioxide for nonaqueous cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5629578A JPS54147197A (en) | 1978-05-11 | 1978-05-11 | Manufacture of manganese dioxide for nonaqueous cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54147197A JPS54147197A (en) | 1979-11-17 |
| JPS6120489B2 true JPS6120489B2 (en) | 1986-05-22 |
Family
ID=13023110
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5629578A Granted JPS54147197A (en) | 1978-05-11 | 1978-05-11 | Manufacture of manganese dioxide for nonaqueous cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS54147197A (en) |
-
1978
- 1978-05-11 JP JP5629578A patent/JPS54147197A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54147197A (en) | 1979-11-17 |
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