JPH0555983B2 - - Google Patents
Info
- Publication number
- JPH0555983B2 JPH0555983B2 JP61228195A JP22819586A JPH0555983B2 JP H0555983 B2 JPH0555983 B2 JP H0555983B2 JP 61228195 A JP61228195 A JP 61228195A JP 22819586 A JP22819586 A JP 22819586A JP H0555983 B2 JPH0555983 B2 JP H0555983B2
- Authority
- JP
- Japan
- Prior art keywords
- manganese dioxide
- manganese
- powder
- acm
- natural
- 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
Links
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 claims description 100
- 239000011572 manganese Substances 0.000 claims description 27
- 239000000843 powder Substances 0.000 claims description 23
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 8
- 229910052748 manganese Inorganic materials 0.000 claims description 8
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 claims description 7
- 239000007774 positive electrode material Substances 0.000 claims description 6
- 230000006835 compression Effects 0.000 claims description 5
- 238000007906 compression Methods 0.000 claims description 5
- 150000002696 manganese Chemical class 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 238000010298 pulverizing process Methods 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 8
- 239000000047 product Substances 0.000 description 8
- 239000000203 mixture Substances 0.000 description 7
- 238000002156 mixing Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- GOPYZMJAIPBUGX-UHFFFAOYSA-N [O-2].[O-2].[Mn+4] Chemical group [O-2].[O-2].[Mn+4] GOPYZMJAIPBUGX-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 235000010755 mineral Nutrition 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000003825 pressing Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 101100513612 Microdochium nivale MnCO gene Proteins 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 239000006230 acetylene black Substances 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- GEYXPJBPASPPLI-UHFFFAOYSA-N manganese(III) oxide Inorganic materials O=[Mn]O[Mn]=O GEYXPJBPASPPLI-UHFFFAOYSA-N 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 239000011592 zinc chloride Substances 0.000 description 2
- 235000005074 zinc chloride Nutrition 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 229940099596 manganese sulfate Drugs 0.000 description 1
- 239000011702 manganese sulphate Substances 0.000 description 1
- 235000007079 manganese sulphate Nutrition 0.000 description 1
- KVGMATYUUPJFQL-UHFFFAOYSA-N manganese(2+) oxygen(2-) Chemical compound [O--].[O--].[O--].[O--].[Mn++].[Mn++].[Mn++] KVGMATYUUPJFQL-UHFFFAOYSA-N 0.000 description 1
- TYTHZVVGVFAQHF-UHFFFAOYSA-N manganese(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Mn+3].[Mn+3] TYTHZVVGVFAQHF-UHFFFAOYSA-N 0.000 description 1
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 description 1
- XMWCXZJXESXBBY-UHFFFAOYSA-L manganese(ii) carbonate Chemical compound [Mn+2].[O-]C([O-])=O XMWCXZJXESXBBY-UHFFFAOYSA-L 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
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
-
- 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)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は二酸化マンガンを用いた乾電池の製造
法に関し、特に乾電池に好適な二酸化マンガンを
用いた乾電池の充電特性改善に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for manufacturing a dry cell using manganese dioxide, and particularly to improving the charging characteristics of a dry cell using manganese dioxide, which is suitable for dry cells.
いわゆるマンガン乾電池の正極作用物質には二
酸化マンガンの粉末が使用されている。
Manganese dioxide powder is used as the positive electrode material of so-called manganese dry batteries.
この二酸化マンガンには、大別して電解二酸化
マンガン、化学合成二酸化マンガン天然二酸化マ
ンガンと活性化化学処理二酸化マンガンの4種類
のものが使用されている。これらのうち電解二酸
化マンガンは、例えば菱マンガン鉱を硫酸で浸出
して硫酸マンガン水溶液とし、この中の鉄分など
の不純物を沈澱せしめて除去し、約80℃以上の温
度で硬鉛または金属チタニウムを陽極として直流
電解することにより、陽極上に析出せしめ製造さ
れている。又、天然二酸化マンガンは天然の鉱石
をそのまま粉砕し、乾電池用に用いている。 There are four types of manganese dioxide used: electrolytic manganese dioxide, chemically synthesized manganese dioxide, natural manganese dioxide, and activated chemically treated manganese dioxide. Among these, electrolytic manganese dioxide is produced by, for example, leaching rhodochrosite with sulfuric acid to make a manganese sulfate aqueous solution, removing impurities such as iron by precipitation, and then converting it to hard lead or metallic titanium at a temperature of about 80°C or higher. It is produced by depositing it on the anode by direct current electrolysis. In addition, natural manganese dioxide is used for dry batteries by pulverizing natural ores as they are.
一方、活性化化学処理二酸化マンガンは上記方
法とは全く異なり、各種のマンガン酸化物鉱石
を、例えば自成雰囲気中で焙焼して熱分解せし
め、三二酸化マンガン、四三酸化マンガンにし、
これを硫酸、塩酸、硝酸のような鉱酸で処理して
得た活性化された二酸化マンガンである。例え
ば、その製造方法を開示する分献としては、特開
昭53−88696号公報、特開昭60−221324号公報を
あげることができる。 On the other hand, activated chemically treated manganese dioxide is completely different from the above method, in which various manganese oxide ores are roasted and thermally decomposed in an autogenous atmosphere to produce manganese sesquioxide and trimanganese tetraoxide.
It is activated manganese dioxide obtained by treating this with mineral acids such as sulfuric acid, hydrochloric acid, and nitric acid. For example, publications disclosing the manufacturing method include JP-A-53-88696 and JP-A-60-221324.
上記した電解二酸化マンガンはたしかに高品
位、高活性であり、乾電池に組込まれたとき、そ
の電池は優れた重負荷放電、軽負荷放電特性を発
現するが、しかし、電解製造時の電流密度は0.8
〜2.0A/cm2と小さいのでその生産性は低く、使
用電力量も膨大となり、全体が高コストになると
いう問題点がある。又、天然二酸化マンガンは従
来から広範囲に利用されているが、これは二酸化
マンガン鉱石が比較的安価で、かつ大量に天然か
ら入手できることによるものと思われる。しかし
ながら、天然二酸化マンガンは、特に重負荷放電
特性が悪いという問題点がある。
The electrolytic manganese dioxide mentioned above is certainly of high quality and highly active, and when incorporated into a dry battery, the battery exhibits excellent heavy load discharge and light load discharge characteristics, but the current density during electrolytic manufacture is 0.8
Since it is small at ~2.0 A/cm 2 , its productivity is low, and the amount of power used is enormous, resulting in a high overall cost. Furthermore, natural manganese dioxide has been widely used, and this is probably because manganese dioxide ore is relatively inexpensive and can be obtained from nature in large quantities. However, natural manganese dioxide has a problem in that it has particularly poor heavy load discharge characteristics.
一方、従来から知られている活性化化学処理二
酸化マンガン(ACM)は、それを乾電池に充填
したとき、電池の重負荷放電特性は、電解二酸化
マンガンに近い特性を示し、低コストである為近
年注目をあびている。一般にそのタツプ密度は
1.1〜1.4g/cm3程度と小さく、非常にポーラスな
充填状態となる。したがつて、その電池における
作用物質たる二酸化マンガンの充填量は少なく、
電池の軽負荷放電が著しく低下する。 On the other hand, the conventionally known activated chemically treated manganese dioxide (ACM), when filled into a dry battery, has a heavy load discharge characteristic close to that of electrolytic manganese dioxide, and has been recently used due to its low cost. It is attracting attention. Generally, the tap density is
The filling state is as small as 1.1 to 1.4 g/cm 3 and extremely porous. Therefore, the loading amount of the active substance manganese dioxide in the battery is small;
Light load discharge of the battery is significantly reduced.
この問題を解決するために、活性化化学処理二
酸化マンガンをロールプレスして平板状の圧縮成
形体としたのち、これを所望の粒度に粉砕して重
質化する試みがなされている(特開昭60−221324
号公報)。 In order to solve this problem, an attempt has been made to roll-press activated chemically treated manganese dioxide into a flat plate-shaped compression molded product, and then crush it to the desired particle size to make it heavier (Unexamined Japanese Patent Publication No. Showa 60-221324
Publication No.).
しかし活性化化学処理二酸化マンガン(ACM)
は、塩化亜鉛を主とした乾電池に使用すると、重
負荷放電特性が優れているACMほど軽負荷放電
中に電池の内部抵抗が上昇し、その結果、パルス
放電特性がいちじるしく悪化するという問題点が
あつた。 But activated chemical treatment manganese dioxide (ACM)
When used in dry batteries that mainly contain zinc chloride, ACM, which has better heavy load discharge characteristics, has the problem that the internal resistance of the battery increases during light load discharge, and as a result, the pulse discharge characteristics deteriorate significantly. It was hot.
この内部抵抗の上昇を防止するために、電解液
の量を多くしたり、導電材であるアセチレンブラ
ツクの配合量を多くしたりしていた。しかし、電
解液を多くすると電池の漏液が多くなつたり、導
電材の量を多くすると二酸化マンガンの量が少な
くなり、軽負荷放電容量が減少する等の問題点が
あり、解決することができなかつた。 In order to prevent this increase in internal resistance, the amount of electrolyte solution or the amount of acetylene black, which is a conductive material, has been increased. However, there are problems that cannot be solved, such as increasing the amount of electrolyte will increase battery leakage, and increasing the amount of conductive material will decrease the amount of manganese dioxide, reducing light load discharge capacity. Nakatsuta.
特にACMは前記したようにタツプ密度(T.
D.)が1.1〜1.4g/cm3で、電解二酸化マンガン
(T.D.2.2〜2.4g/cm3)、天然二酸化マンガン(T.
D.2.1〜2.3g/cm3)に比べて低い為、合剤配合以
外の技術で特性改善することが重要な課題であつ
た。 In particular, ACM has tap density (T.
D.) is 1.1 to 1.4 g/cm 3 , electrolytic manganese dioxide (TD 2.2 to 2.4 g/cm 3 ), natural manganese dioxide (T.
D. 2.1 to 2.3 g/cm 3 ), it was an important issue to improve the properties using techniques other than compounding.
又、ACMと天然二酸化マンガンを単に混合し
たものを正極作用物質として使用する試みは行わ
れているが、パルス放電特性の著しい改善は得ら
れなかつた。 Further, attempts have been made to use a simple mixture of ACM and natural manganese dioxide as a positive electrode active material, but no significant improvement in pulse discharge characteristics has been obtained.
本発明は従来のこのような問題点を解決し、特
に電池の放電特性の向上を経済的な方法で図つた
ものである。 The present invention solves these conventional problems and particularly aims to improve the discharge characteristics of a battery in an economical manner.
本発明者らは前記目的を達成するために、鋭意
調査したところ、特定のACMと天然二酸化マン
ガンとを混合し、ロールプレスにより圧縮成形
し、次に該成形後の二酸化マンガン混合体を粉砕
したものを乾電池に使用すると、前記特性が著し
く向上してくることを見い出し、本発明の乾電池
を製造するに至つた。
In order to achieve the above object, the present inventors conducted extensive research and found that a specific ACM and natural manganese dioxide were mixed, compression molded using a roll press, and then the molded manganese dioxide mixture was pulverized. The inventors have discovered that the above-mentioned characteristics are significantly improved when used in dry batteries, and have now produced the dry batteries of the present invention.
すなわち、本発明はマンガン鉱石またはマンガ
ン塩を400℃〜1100℃の温度で焙焼後、酸処理を
施して得たACMを原料とし、このACM粉末と天
然二酸化マンガン粉末とを混合し、1〜10トン/
cm2の圧力下でロールプレスにより平板状に圧縮成
形し、つぎに、これを所定の粒度に粉砕し、正極
作用物質として乾電池に提供する。 That is, the present invention uses ACM obtained by roasting manganese ore or manganese salt at a temperature of 400°C to 1100°C and then acid-treating it as a raw material, and mixes this ACM powder with natural manganese dioxide powder, 10 tons/
It is compression molded into a flat plate using a roll press under a pressure of cm 2 , and then pulverized to a predetermined particle size and provided to a dry battery as a positive electrode active material.
ここで使用されるマンガン鉱石としては、
MnO2(軟マンガン鉱)、MnCO3(菱マンガン鉱)、
Mn2O3、Mn3O4等を主成分とするもをが好まし
い。 The manganese ore used here is
MnO 2 (soft manganese ore), MnCO 3 (rhodochosite),
Those containing Mn 2 O 3 , Mn 3 O 4 or the like as a main component are preferred.
又、マンガン塩としては、MnSO4、MnCO3、
MnCl2、Mn(NO3)2等がある。 In addition, as manganese salts, MnSO 4 , MnCO 3 ,
Examples include MnCl 2 and Mn(NO 3 ) 2 .
一般にマンガン鉱石およびマンガン塩
(MnSO4)は自成雰囲気で焙焼すると、400〜500
℃付近からMn2O3に転化し、更に800〜1000℃付
近の温度からMn3O4に転化する。焙焼する時間
は格別限定されるものではないが、通常0.5〜5
時間であればよい。 Generally, when manganese ore and manganese salt (MnSO 4 ) are roasted in an autogenous atmosphere, the
It is converted to Mn 2 O 3 from around 800°C to 1000°C, and further converted to Mn 3 O 4 from around 800 to 1000°C. The roasting time is not particularly limited, but is usually 0.5 to 5 minutes.
Any time is fine.
又、MnSO4は850℃で分解してMn3O4となり、
更に530〜940℃で加熱すると酸化反応を起こし
Mn2O3を生成する。 Also, MnSO 4 decomposes at 850℃ to become Mn 3 O 4 ,
Further heating at 530 to 940℃ causes an oxidation reaction.
Produces Mn2O3 .
本反応式の例を式(1)、(2)、(2)′に示す。 Examples of this reaction formula are shown in formulas (1), (2), and (2)′.
2MnO2→Mn2O3+1/2O2 ……(1)
3MnSO4→Mn3O4+2SO3+SO2 ……(2)
2/3Mn3O4+1/6O2→Mn2O3 ……(2)′
このような焙焼によつて得られたMn2O3又は
Mn3O4を、次に鉱酸で処理する。使用する鉱酸
としては、例えば硫酸、硝酸又は塩酸などをあげ
ることができる。 2MnO 2 →Mn 2 O 3 +1/2O 2 ...(1) 3MnSO 4 →Mn 3 O 4 +2SO 3 +SO 2 ...(2) 2/3Mn 3 O 4 +1/6O 2 →Mn 2 O 3 ...( 2)′ Mn 2 O 3 or Mn 2 O 3 obtained by such roasting
The Mn 3 O 4 is then treated with mineral acid. Examples of the mineral acids used include sulfuric acid, nitric acid, and hydrochloric acid.
この処理により二酸化マンガンが生成する。反
応式は次のようになる。 This treatment produces manganese dioxide. The reaction formula is as follows.
Mn2O3+H2SO4→MnO2+MnSO4+H2O
Mn3O4+2H2SO4→MnO2+2MnSO4+2H2O
得られた二酸化マンガンのケーキを、例えば流
水中で充分洗浄し、アンモニア水、苛性ソーダ水
溶液または、炭酸ソーダ水溶液で中和処理を行つ
た後、60〜110℃の温度で乾燥して水の除去を行
うことにより製造することができる。これらの二
酸化マンガンはγ型を主体とした結晶構造を有し
ている。 Mn 2 O 3 +H 2 SO 4 →MnO 2 +MnSO 4 +H 2 O Mn 3 O 4 +2H 2 SO 4 →MnO 2 +2MnSO 4 +2H 2 O The obtained manganese dioxide cake is thoroughly washed, for example, in running water, and ammonia It can be produced by neutralizing with water, an aqueous caustic soda solution, or an aqueous sodium carbonate solution, followed by drying at a temperature of 60 to 110°C to remove water. These manganese dioxides have a crystal structure mainly composed of the γ type.
又、本発明に使用する天然二酸化マンガン粉末
は、純度が75%以上の乾電池用二酸化マンガンで
あり、ガボン鉱、オーストラリヤ鉱等の純度80%
〜86%のものが好適である。 In addition, the natural manganese dioxide powder used in the present invention is manganese dioxide for use in dry batteries with a purity of 75% or more, and 80% purity of Gabon ore, Australian ore, etc.
~86% is preferred.
具体的なプレスの方法としては、マンガン鉱石
またはマンガン塩を焙焼し得られるMn2O3また
はMn3O4を酸処理した活性化化学処理二酸化マ
ンガン(ACM)粉末と、天然二酸化マンガン粉
末を共に100mesh(径150μm)以下に粉砕する。 As a specific pressing method, activated chemically treated manganese dioxide (ACM) powder obtained by acid-treating Mn 2 O 3 or Mn 3 O 4 obtained by roasting manganese ore or manganese salt, and natural manganese dioxide powder are used. Both are crushed to 100mesh (150μm in diameter) or less.
その混合比はACMを40〜70%、天然二酸化マ
ンガンを60〜30%の範囲で混合し、プレスし粉砕
することが、放電特性の優れた乾電池にする為に
有利である。この範囲でプレスすると、単独でプ
レスするよりも混合することにより成形密度が増
加し、両二酸化マンガンの電気科学的活性を引き
出す結果となり、両二酸化マンガンの電池特性の
算術平均値よりもすぐれた特性を示すようにな
る。 It is advantageous to mix ACM in a range of 40 to 70% and natural manganese dioxide in a range of 60 to 30%, press and crush the mixture in order to obtain a dry battery with excellent discharge characteristics. When pressed in this range, the compacted density increases by mixing rather than pressing alone, and the electrochemical activity of both manganese dioxides is brought out, resulting in better properties than the arithmetic average value of the battery characteristics of both manganese dioxides. It comes to show that.
圧縮成形する際のロールプレスの圧力は、一般
に1〜10トン/cm2であるが、1〜4トン/cm2の範
囲の低圧力でも充分に目的を達成する。 The pressure of the roll press during compression molding is generally 1 to 10 tons/cm 2 , but even a low pressure in the range of 1 to 4 tons/cm 2 can sufficiently achieve the purpose.
又、プレス圧力およびプレス回数は、原料の二
酸化マンガンの配合比、粒度およびその分布、更
に形状により異なるが、タツプ密度を2.0g/cm2
にする場合はプレス圧2トン/cm2で2〜4回で充
分であり、5回以上プレスしても効果上に顕著な
差はみられない。 In addition, the press pressure and number of presses vary depending on the blending ratio of raw manganese dioxide, particle size and its distribution, and shape, but the tap density is 2.0 g/cm 2
In this case, it is sufficient to press 2 to 4 times at a pressure of 2 tons/cm 2 , and there is no noticeable difference in the effect even if the press is pressed 5 or more times.
両者の二酸化マンガン粉末を圧縮成形粉砕する
ことにより、混合のみの場合では得られない下記
に示す、すぐれた特徴を有するようになる。
By compressing and pulverizing both manganese dioxide powders, they have the following excellent characteristics that cannot be obtained by mixing alone.
まず第1には、軽負荷放電時のパルス放電が大
幅に改善される。 First of all, pulse discharge during light load discharge is significantly improved.
第2には、合剤にした場合の充填密度が向上
し、軽負荷放電特性が大幅に改善される。 Secondly, when used as a mixture, the packing density is improved and the light load discharge characteristics are significantly improved.
実施例 A
純度84%のマンガン酸化物鉱石(軟マンガン
鉱)を粉砕して60mesh以下の粉末とした。この
粉末を約850℃の自成雰囲気中で焙焼した。主成
分はα−Mn2O3であつた。焙焼後の粉末を
100mesh以下に微粉砕し、90℃の3規定硫酸溶液
に投入して2時間反応させた。ついで、反応処理
物を充分に水洗、過したのち、アンモニア水で
中和処理し、更に水洗し、最後に乾燥してACM
粉末を得た。このACM粉末は純度82.1%であり、
X線回折の結果、結晶構造はγ型主体の二酸化マ
ンガンであつた。
Example A Manganese oxide ore (soft manganese ore) with a purity of 84% was crushed into a powder of 60 mesh or less. This powder was roasted in an autogenous atmosphere at about 850°C. The main component was α-Mn 2 O 3 . Powder after roasting
The powder was pulverized to 100 mesh or less, poured into a 3N sulfuric acid solution at 90°C, and reacted for 2 hours. Next, the reaction product was thoroughly washed with water, filtered, neutralized with aqueous ammonia, further washed with water, and finally dried with ACM.
A powder was obtained. This ACM powder has a purity of 82.1%,
As a result of X-ray diffraction, the crystal structure was manganese dioxide mainly in the γ type.
又、天然二酸化マンガンはガボン産の乾電用二
酸化マンガンを、粉砕器により100mesh以下に微
粉砕して得た。純度は83.8%であり、結晶構造は
γ型主体の二酸化マンガンである。 Natural manganese dioxide was obtained by pulverizing manganese dioxide for dry electricity production from Gabon to 100 mesh or less using a pulverizer. The purity is 83.8%, and the crystal structure is mainly γ-type manganese dioxide.
つぎに、ACM粉末を80重量部と天然二酸化マ
ンガンを30重量部とを混合し、ロールプレス機に
かけ3トン/cm2の圧力で成形したのち、この成形
体を粉砕し、100mesh以下の粉末とした。 Next, 80 parts by weight of ACM powder and 30 parts by weight of natural manganese dioxide were mixed, molded using a roll press at a pressure of 3 tons/cm 2 , and the molded body was crushed to form a powder of 100 mesh or less. did.
これらの粉末を正極作用物質として、以下に示
す方法により電池を製造した。 A battery was manufactured using these powders as a positive electrode active material by the method shown below.
本発明の混合二酸化マンガン4.00gとアセチレ
ンブラツク0.67gとをよく混合し、25重量%塩化
亜鉛、2.5重量%塩化アンモニウムとを含有する
水溶液3.33gを加え均一な正極合剤とし、これを
用いてR6型乾電池の本発明品Aを製造した。 4.00 g of mixed manganese dioxide of the present invention and 0.67 g of acetylene black were thoroughly mixed, and 3.33 g of an aqueous solution containing 25% by weight zinc chloride and 2.5% by weight ammonium chloride was added to form a uniform positive electrode mixture. Inventive product A, which is an R6 type dry battery, was manufactured.
実施例 B、C
実施例Aと同様なACMと天然二酸化マンガン
を使用し、ACM粉末を50重量部、天然二酸化マ
ンガンを50重量部を混合し、同様な条件でロール
プレス、粉砕したものから本発明品Bの同型乾電
池を製造した。又、ACM粉末を40重量部、天然
二酸化マンガン60重量部を混合し、ロールプレ
ス、粉砕したものから製造した同型乾電池を本発
明品Cとした。Examples B and C Using the same ACM and natural manganese dioxide as in Example A, 50 parts by weight of ACM powder and 50 parts by weight of natural manganese dioxide were mixed, roll pressed and pulverized under the same conditions. A dry battery of the same type as Invention B was manufactured. In addition, a dry battery of the same type was manufactured by mixing 40 parts by weight of ACM powder and 60 parts by weight of natural manganese dioxide, roll pressing, and pulverizing the mixture, and designated it as product C of the present invention.
比較例 D、E、F
実施例Aで製造したACMをロールプレス機に
かけ3トン/cm2の圧力で圧縮成形したのち、この
成形体を粉砕し、100mesh以下の粉末とした。こ
の粉末70、50、40重量部と実施例Aと同様の天然
二酸化マンガン30、50、60重量部とをそれぞれ混
合し、プレス粉砕しないで、実施例Aと同様の配
合組成のR6乾電池を製造した比較品を、それぞ
れD,EおよびFとした。Comparative Examples D, E, F The ACM produced in Example A was compression molded using a roll press machine at a pressure of 3 tons/cm 2 , and then the molded body was crushed to form a powder of 100 mesh or less. By mixing 70, 50, and 40 parts by weight of this powder with 30, 50, and 60 parts by weight of natural manganese dioxide similar to Example A, an R6 dry battery having the same composition as Example A was produced without press crushing. The comparative products were designated as D, E, and F, respectively.
これらのR6型乾電池について、それぞれ放電
試験を行い、その結果を第1図に示した。 A discharge test was conducted on each of these R6 type dry batteries, and the results are shown in Figure 1.
第1図には、本発明品A,BおよびC、比較品
D,EおよびFについて、1.2KΩの負荷抵抗で
連続放電したときの電池内部抵抗の変化を、A,
B,C,D,EおよびFで示し、1.2KΩの連続
放電中に1日1回10Ω3秒間のパルス放電を重畳
したときの端子電圧の変化を、A′,B′,C′,D′,
E′およびF′として示した。 Figure 1 shows the changes in battery internal resistance when the invention products A, B, and C and the comparative products D, E, and F were continuously discharged with a load resistance of 1.2KΩ.
B, C, D, E, and F, and the changes in terminal voltage when a pulse discharge of 10 Ω for 3 seconds is superimposed once a day during a continuous discharge of 1.2 KΩ are A', B', C', D' ,
Denoted as E′ and F′.
以上のように、本発明の混合二酸化マンガンを
正極作用物質とした乾電池は、軽負荷、中負荷放
電時のパルス放電特性を向上させ、更に軽負荷放
電を向上せしめたものである。
As described above, the dry battery of the present invention using mixed manganese dioxide as a positive electrode active material has improved pulse discharge characteristics during light and medium load discharges, and further improved light load discharge.
第1図は実施例の本発明品A,A′,B,B′,
C,C′と、比較品D,D′,E,E′,F,F′との放
電曲線と内部抵抗値とについての比較図である。
A,B,C,D,E,F……連続放電時の内部
抵抗曲線、A′,B′,C′,D′,E′,F′……連続放
電時にパルス放電を重畳したときの放電曲線。
Figure 1 shows examples of products A, A', B, B',
It is a comparison diagram regarding the discharge curve and internal resistance value of C and C' and comparative products D, D', E, E', F, and F'. A, B, C, D, E, F... Internal resistance curve during continuous discharge, A', B', C', D', E', F'... Internal resistance curve when pulse discharge is superimposed during continuous discharge. discharge curve.
Claims (1)
られたマンガン酸化物(Mn2O3またはMn3O4)
を酸処理を施して活性化化学処理二酸化マンガン
粉末とし、この粉末と天然二酸化マンガン粉末と
を混合し、1〜10トン/cm2の圧力下でロールプレ
スにより圧縮成型し、次に混合二酸化マンガン成
形体を粉砕し、正極作用物質とすることを特徴と
する乾電池の製造法。1 Manganese oxide (Mn 2 O 3 or Mn 3 O 4 ) obtained by roasting manganese ore or manganese salt
is acid-treated to produce an activated chemically treated manganese dioxide powder, this powder is mixed with natural manganese dioxide powder, and compression molded using a roll press under a pressure of 1 to 10 tons/cm 2 , and then mixed manganese dioxide is obtained. A method for producing a dry battery, characterized by pulverizing a molded body and using it as a positive electrode active material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61228195A JPS6386263A (en) | 1986-09-29 | 1986-09-29 | Manufacture of dry battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61228195A JPS6386263A (en) | 1986-09-29 | 1986-09-29 | Manufacture of dry battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6386263A JPS6386263A (en) | 1988-04-16 |
| JPH0555983B2 true JPH0555983B2 (en) | 1993-08-18 |
Family
ID=16872693
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61228195A Granted JPS6386263A (en) | 1986-09-29 | 1986-09-29 | Manufacture of dry battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6386263A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2021075136A1 (en) * | 2019-10-18 | 2021-04-22 | Jfeスチール株式会社 | Method for recovering manganese from waste dry-cell batteries and recovery equipment |
-
1986
- 1986-09-29 JP JP61228195A patent/JPS6386263A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6386263A (en) | 1988-04-16 |
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