JPS5856463B2 - Manufacturing method of non-aqueous electrolyte battery - Google Patents
Manufacturing method of non-aqueous electrolyte batteryInfo
- Publication number
- JPS5856463B2 JPS5856463B2 JP53142603A JP14260378A JPS5856463B2 JP S5856463 B2 JPS5856463 B2 JP S5856463B2 JP 53142603 A JP53142603 A JP 53142603A JP 14260378 A JP14260378 A JP 14260378A JP S5856463 B2 JPS5856463 B2 JP S5856463B2
- Authority
- JP
- Japan
- Prior art keywords
- battery
- manganese dioxide
- mixture
- temperature
- reduced pressure
- 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
- H01M4/06—Electrodes for primary cells
- H01M4/08—Processes of manufacture
-
- 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)
- Primary Cells (AREA)
- Battery Electrode And Active Subsutance (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活物質とする負極と
、活物質の二酸化マンガンと導電材および結合剤からな
る正極合剤、および非水の電解質を用いる電池、特にそ
の正極合剤の製造法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a battery using a negative electrode having a light metal such as lithium as an active material, a positive electrode mixture comprising manganese dioxide as an active material, a conductive material, and a binder, and a non-aqueous electrolyte. The present invention relates to a method for producing the positive electrode mixture.
近年、負極にリチウム、電解質に非水の有機電解質を用
いたリチウム電池が高エネルギー密度電池として注目さ
れている。In recent years, lithium batteries that use lithium for the negative electrode and nonaqueous organic electrolytes for the electrolyte have attracted attention as high-energy density batteries.
このリチウム電池の正極活物質として代表的なものにフ
ッ化黒鉛、二酸化マンガンがあり、いずれも実用化され
ている。Typical positive electrode active materials for lithium batteries include fluorinated graphite and manganese dioxide, both of which are in practical use.
この種非水電解質電池の正極活物質として二酸化マンガ
ンを用いる場合、二酸化マンガン中の結晶水を取り除く
こと、および二酸化マンガンの結晶構造はγ型よりγ−
β型またはβ型が放電性能に優れていることから、25
0〜450℃の温度で熱処理している。When manganese dioxide is used as the positive electrode active material of this type of non-aqueous electrolyte battery, it is necessary to remove crystal water in manganese dioxide, and the crystal structure of manganese dioxide is γ- rather than γ-type.
Since the β type or β type has excellent discharge performance, 25
Heat treatment is performed at a temperature of 0 to 450°C.
この熱処理二酸化マンガンに導電材および結合剤を混合
し、個々の電池の形状に合わせて底形して正極合剤ペレ
ットとし、電池組立前に付着水を取り除くため、空気中
もしくは減圧下で加熱して乾燥し、次に負極リチウム、
セパレータ、およびプロピレンカーボネイト、ジメトキ
シエタンなどの有機溶媒に過塩素酸リチウムやホウフッ
化リチウムを溶解した電解液と組み合わせて電池を構成
していた。This heat-treated manganese dioxide is mixed with a conductive material and a binder, and the bottom is shaped to match the shape of each battery to form positive electrode mixture pellets.Then, the pellets are heated in air or under reduced pressure to remove adhering water before battery assembly. and then dry the negative electrode lithium.
A battery was constructed by combining a separator and an electrolyte solution in which lithium perchlorate or lithium borofluoride was dissolved in an organic solvent such as propylene carbonate or dimethoxyethane.
このようにして構成された電池は、保存中に多量のガス
を発生し、電池の膨張の原因となったり、保存中の内部
インピーダンスが上昇したりして、保存後の放電性能が
大きく劣化する欠点があった。Batteries constructed in this way generate a large amount of gas during storage, which causes expansion of the battery and increases internal impedance during storage, resulting in a significant deterioration in discharge performance after storage. There were drawbacks.
本発明者らがこのガス発生の原因を調査した結果、電解
液や合剤中に少量残存する水分の共存下で、二酸化マン
ガンに吸着している活性な酸素が電解液中の有機溶媒、
例えばプロピレンカーボネイトに作用し、有機溶媒が分
解されて炭酸ガスを発生することが判明した。As a result of investigating the cause of this gas generation, the present inventors found that in the coexistence of a small amount of water remaining in the electrolyte or mixture, the active oxygen adsorbed on manganese dioxide is activated by the organic solvent in the electrolyte.
For example, it was found that it acts on propylene carbonate, decomposing the organic solvent and generating carbon dioxide gas.
この活性酸素は、二酸化マンガンを高温で加熱するほど
取れやすいが、逆に吸着していた活性酸素を離脱した二
酸化マンガンは高温になっているほど活性酸素を吸着し
やすいという性質を有している。This active oxygen is easier to remove as manganese dioxide is heated to a higher temperature, but conversely, the manganese dioxide that has released the adsorbed active oxygen has the property that the higher the temperature, the easier it is to adsorb active oxygen. .
このため減圧下または不活性ガス中で熱処理をした二酸
化マンガンまたは正極合剤であっても、高温状態で空気
に触れさせたり、また成形後の合剤を乾燥するために空
気中で加熱したりすると、一度取り除かれた活性酸素が
再び二酸化マンガン表面に吸着されるため、このような
二酸化マンガンを用いた電池はガス発生により電池の膨
張や保存劣化が大きく茂る。For this reason, even if manganese dioxide or positive electrode mixture has been heat-treated under reduced pressure or in an inert gas, it may not be exposed to air at high temperatures, or heated in air to dry the mixture after molding. Then, the active oxygen that has been removed is adsorbed again on the surface of manganese dioxide, and batteries using such manganese dioxide are subject to expansion and storage deterioration due to gas generation.
本発明は、正極合剤の製造法を改良して、前記のガス発
生の主要因である二酸化マンガン中の活性酸素を取り除
き、電池膨張や保存劣化のない電池を提供するものであ
る。The present invention improves the method for producing a positive electrode mixture, removes active oxygen in manganese dioxide, which is the main cause of gas generation, and provides a battery that does not undergo battery expansion or storage deterioration.
すなわち本発明は、熱処理してγ−β型またはβ型に変
換した二酸化マンガンに導電材、例えばアセチレンブラ
ック、および結合剤、例えばポリ4フツ化エチレン、4
7ツ化エチレン−6フツ化プロピレン共重合体を混合し
た正極合剤を減圧下もしくは不活性ガス雰囲気中で加熱
乾燥し、つぎに同じく減圧下もしくは不活性ガス雰囲気
中で冷却することを特徴とする。That is, the present invention applies a conductive material such as acetylene black, and a binder such as polytetrafluoroethylene, 4
The method is characterized by heating and drying a positive electrode mixture of ethylene heptafluoride and propylene hexafluoride copolymer under reduced pressure or in an inert gas atmosphere, and then cooling it under reduced pressure or in an inert gas atmosphere. do.
以下本発明をその実施例により詳細に説明する。The present invention will be explained in detail below with reference to Examples.
γ型二酸化マンガンを50vItHg以下の減圧下にお
いて350℃の温度で4時間熱処理した二酸化マンガン
を用いる。Manganese dioxide obtained by heat-treating γ-type manganese dioxide at a temperature of 350° C. for 4 hours under reduced pressure of 50 vItHg or less is used.
なおγ型二酸化マンガンなγ−β型またはβ型に変換す
るための熱処理条件は、温度250〜450℃、時間2
〜8時間が適当であり、この場合の雰囲気は、空気中、
減圧下、不活性ガス中を問わない。The heat treatment conditions for converting γ-type manganese dioxide into γ-β type or β type are: temperature 250-450°C, time 2
~8 hours is appropriate, and the atmosphere in this case is air,
It does not matter whether it is under reduced pressure or in an inert gas.
上記の熱処理二酸化マンガン100重量部に対し、アセ
チレンブラック4重量部と、樹脂分5重量部に相当する
ポリ4フツ化エチレンのディスパージョンを混合した正
極合剤を直径177g、厚さ1.1uの円板状に加圧成
形する。A positive electrode mixture of 100 parts by weight of the above heat-treated manganese dioxide, 4 parts by weight of acetylene black, and a dispersion of polytetrafluoroethylene corresponding to 5 parts by weight of resin was prepared into a material with a diameter of 177 g and a thickness of 1.1 μ. Pressure mold into a disc shape.
つぎにこの成形合剤を50 vtt Hg以下の減圧下
において、150〜320℃の温度で加熱乾燥し、同じ
減圧下で自然冷却し、合剤温度が50℃以下に低下した
後、大気中に取り出す。Next, this molding mixture is heated and dried at a temperature of 150 to 320°C under a reduced pressure of 50 vtt Hg or less, and then naturally cooled under the same reduced pressure. After the mixture temperature has decreased to 50°C or less, it is released into the atmosphere. Take it out.
この乾燥工程により合剤中の水分とともに二酸化マンガ
ンに吸着している活性酸素が取り除かれる。This drying process removes the active oxygen adsorbed on the manganese dioxide along with the moisture in the mixture.
この乾燥温度は150〜320℃が適当である。A suitable drying temperature is 150 to 320°C.
150℃以下の温度でも水分の除去には充分であるが、
吸着している活性酸素は充分には取り除かれない。Although temperatures below 150°C are sufficient for removing moisture,
Adsorbed active oxygen is not removed sufficiently.
また乾燥温度が320℃を超えると、二酸化マンガンの
結晶構造が進みすぎたり、結合剤が分解して合剤の形部
れを生じ、電池の組立が困難になる。Furthermore, if the drying temperature exceeds 320° C., the crystal structure of manganese dioxide will advance too much, the binder will decompose, and the shape of the mixture will become distorted, making it difficult to assemble the battery.
また乾燥時間は温度によって異なるが2〜8時間が適当
である。The drying time varies depending on the temperature, but 2 to 8 hours is appropriate.
乾燥雰囲気は非酸素雰囲気である真空中またはアルゴン
、窒素などの不活性ガス雰囲気が好ましいが、実用的に
は50rRXtHg以下の減圧下で充分である。The drying atmosphere is preferably an oxygen-free vacuum or an inert gas atmosphere such as argon or nitrogen, but a reduced pressure of 50rRXtHg or less is practically sufficient.
上記のように加熱乾燥した合剤は、同じ雰囲気中で充分
に冷却すると、その後に空気に触れても活性酸素の二酸
化マンガンへの吸着は起こらない。If the mixture heated and dried as described above is sufficiently cooled in the same atmosphere, active oxygen will not be adsorbed to manganese dioxide even if it is subsequently exposed to air.
冷却後大気中へ取り出すときの合剤の温度1.高くとも
50°Cが適当で、これより高い温度で酸素雰囲気に触
れさせると、活性酸素が再び二酸化マンガンに吸着する
。Temperature of the mixture when taken out into the atmosphere after cooling 1. A temperature of at most 50°C is suitable; if exposed to an oxygen atmosphere at a temperature higher than this, active oxygen will be adsorbed to manganese dioxide again.
こうして乾燥し、冷却した正極合剤に、負極リチウム、
およびプロピレンカーボネイトと1,2−ジメトキシエ
タンとを容量比で5:2の割合で混合した溶媒に1.0
モル/lの過塩素酸リチウムを溶解した電解液を組み合
わせて直径23M、厚さ2.5uのコイン形リチウム電
池を構成する。The thus dried and cooled positive electrode mixture is filled with negative electrode lithium,
and 1.0% in a solvent containing propylene carbonate and 1,2-dimethoxyethane mixed at a volume ratio of 5:2.
A coin-shaped lithium battery with a diameter of 23M and a thickness of 2.5U is constructed by combining electrolytes in which mol/l of lithium perchlorate is dissolved.
以上のようにして製造した本発明の電池り二酸化マンガ
ンに吸着している活性酸素が取り除かれ、かつ再吸着が
ないので、従来のようなガス発生もほとんどなく、かつ
保存後の性能も良好である。Since the active oxygen adsorbed to the manganese dioxide in the battery cell of the present invention produced as described above is removed and there is no re-adsorption, there is almost no gas generation as in the conventional case, and the performance after storage is also good. be.
つぎに本発明の効果を具体例をもって説明する。Next, the effects of the present invention will be explained using specific examples.
第1図&東前記の正極合剤を50gHg以下の減圧下に
おいて、各種温度で2時間乾燥した後、同じ減圧下で2
5℃まで冷却した合剤を用いた場合(a)と、乾燥後、
直ちに空気中に取り出して冷却した合剤を用いた場@b
)について、電池を60℃で3日間放置したときの電池
の膨張度合と乾燥温度との関係を示す。Figure 1 & East The above positive electrode mixture was dried at various temperatures for 2 hours under a reduced pressure of 50 gHg or less, and then dried under the same reduced pressure for 2 hours.
(a) using a mixture cooled to 5°C and after drying,
When using a mixture that was immediately taken out into the air and cooled @b
), the relationship between the degree of expansion of the battery and the drying temperature when the battery was left at 60°C for 3 days is shown.
膨張度合は電池の膨張後の厚さと初度の厚さとの差で示
した。The degree of expansion was expressed as the difference between the thickness of the battery after expansion and the initial thickness.
また第2図は前記と同様の電池を60℃で1力月保存し
た後の25℃における電池の内部インピーダンスと合剤
の乾燥温度との関係を示す。Further, FIG. 2 shows the relationship between the internal impedance of the battery and the drying temperature of the mixture at 25° C. after the same battery as above was stored at 60° C. for one month.
これらの図には減圧下における合剤の加熱乾燥および冷
却による効果が顕著に表れている。These figures clearly show the effects of heating and cooling the mixture under reduced pressure.
乾燥温度は150℃以上、特に200℃以上の場合に電
池の膨張および内部インピーダンスが少ないが320℃
を超えると結合剤が分解する。The drying temperature is 150℃ or higher, especially if it is 200℃ or higher, the expansion and internal impedance of the battery will be small, but 320℃
The binder will decompose if it exceeds
第3図は、501rutt Hg以下の減圧下において
250℃の温度で2時間乾燥した後、同じ雰囲気下で各
種温度まで冷却した後大気中に取り出した合剤を用いた
電池の前記と同条件下での電池の膨張度合と冷却温度と
の関係を示す。Figure 3 shows a battery using a mixture that was dried at a temperature of 250°C for 2 hours under a reduced pressure of 501 rutt Hg or less, cooled to various temperatures in the same atmosphere, and then taken out into the atmosphere under the same conditions as above. The relationship between the degree of expansion of the battery and the cooling temperature is shown.
図から冷却工程においては、合剤を50℃以下に冷却し
た後、大気中に取り出すのが活性酸素の再吸着等を生じ
なく、電池としての膨張を抑制する上からも適当である
ことがわかる。The figure shows that in the cooling process, it is appropriate to cool the mixture to below 50°C and then take it out into the atmosphere to avoid re-adsorption of active oxygen and to suppress expansion of the battery. .
上記の例では減圧下において乾燥、冷却したが、アルゴ
ン、窒素などの不活性ガス雰囲気中で処理した場合も同
様の効果が得られた。In the above example, drying and cooling were performed under reduced pressure, but similar effects were obtained when processing was performed in an inert gas atmosphere such as argon or nitrogen.
以上のように、本発明によれば、ガス発生による膨張が
なく、保存性の良好な非水電解質電池を得ることができ
る。As described above, according to the present invention, it is possible to obtain a nonaqueous electrolyte battery that does not expand due to gas generation and has good storage stability.
第1図は合剤を減圧下で加熱乾燥した後、減圧下または
大気中で冷却した場合の合剤乾燥温度と電池の膨張度合
との関係を示す図、第2図は同じく合剤乾燥温度と電池
保存後の内部インピーダンスとの関係を示す図、第3図
は冷却工程における合剤の冷却後の温度と電池の膨張度
合との関係を示す図である。Figure 1 shows the relationship between the mixture drying temperature and the degree of expansion of the battery when the mixture is heated and dried under reduced pressure and then cooled under reduced pressure or in the atmosphere. Figure 2 is also a diagram showing the relationship between the mixture drying temperature and the degree of expansion of the battery. FIG. 3 is a diagram showing the relationship between the temperature and the internal impedance after storage of the battery, and FIG. 3 is a diagram showing the relationship between the temperature after cooling the mixture in the cooling process and the degree of expansion of the battery.
Claims (1)
結合剤からなる正極合剤を、減圧下もしくは不活性ガス
雰囲気中で150〜320°Cの温度で加熱乾燥した後
、減圧下もしくは不活性ガス雰囲気中で50℃以下の温
度に冷却する工程を有することを特徴とする非水電解質
電池の製造法。1 A positive electrode mixture consisting of γ-β type or β type manganese dioxide, a conductive material, and a binder is heated and dried at a temperature of 150 to 320°C under reduced pressure or in an inert gas atmosphere, and then dried under reduced pressure or in an inert gas atmosphere. A method for manufacturing a non-aqueous electrolyte battery, comprising a step of cooling to a temperature of 50° C. or lower in a gas atmosphere.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53142603A JPS5856463B2 (en) | 1978-11-17 | 1978-11-17 | Manufacturing method of non-aqueous electrolyte battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53142603A JPS5856463B2 (en) | 1978-11-17 | 1978-11-17 | Manufacturing method of non-aqueous electrolyte battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5569960A JPS5569960A (en) | 1980-05-27 |
| JPS5856463B2 true JPS5856463B2 (en) | 1983-12-15 |
Family
ID=15319146
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP53142603A Expired JPS5856463B2 (en) | 1978-11-17 | 1978-11-17 | Manufacturing method of non-aqueous electrolyte battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5856463B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03297192A (en) * | 1990-04-17 | 1991-12-27 | Mitsubishi Cable Ind Ltd | Circuit board and manufacture thereof |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5746473A (en) * | 1980-09-05 | 1982-03-16 | Hitachi Ltd | Production of anode body for lithium battery |
| JPS57128462A (en) * | 1981-02-03 | 1982-08-10 | Seiko Instr & Electronics Ltd | Manufacture of non-aqueous electrolyte battery |
| JPS5819860A (en) * | 1981-07-30 | 1983-02-05 | Toshiba Corp | Manufacture of positive electrode for organic solvent battery |
| US5609975A (en) * | 1994-05-13 | 1997-03-11 | Matsushita Electric Industrial Co., Ltd. | Positive electrode for non-aqueous electrolyte lithium secondary battery and method of manufacturing the same |
| WO2019044771A1 (en) * | 2017-08-28 | 2019-03-07 | 株式会社村田製作所 | Nonaqueous electrolyte battery and communication equipment |
-
1978
- 1978-11-17 JP JP53142603A patent/JPS5856463B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03297192A (en) * | 1990-04-17 | 1991-12-27 | Mitsubishi Cable Ind Ltd | Circuit board and manufacture thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5569960A (en) | 1980-05-27 |
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