Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6031067B2 - Manufacturing method of battery positive electrode - Google Patents
[go: Go Back, main page]

JPS6031067B2 - Manufacturing method of battery positive electrode - Google Patents

Manufacturing method of battery positive electrode

Info

Publication number
JPS6031067B2
JPS6031067B2 JP54055982A JP5598279A JPS6031067B2 JP S6031067 B2 JPS6031067 B2 JP S6031067B2 JP 54055982 A JP54055982 A JP 54055982A JP 5598279 A JP5598279 A JP 5598279A JP S6031067 B2 JPS6031067 B2 JP S6031067B2
Authority
JP
Japan
Prior art keywords
positive electrode
battery
lithium carbonate
cupric oxide
lithium
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
JP54055982A
Other languages
Japanese (ja)
Other versions
JPS55148367A (en
Inventor
尉辞 西村
孝志 飯島
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP54055982A priority Critical patent/JPS6031067B2/en
Publication of JPS55148367A publication Critical patent/JPS55148367A/en
Publication of JPS6031067B2 publication Critical patent/JPS6031067B2/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
    • H01M4/06Electrodes for primary cells
    • H01M4/08Processes of manufacture
    • 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

  • 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)

Description

【発明の詳細な説明】 本発明な、電池、特に軽金属を負極活物質とし、酸化第
二銅を正極活物質とする有機電解質電池の正極の製造法
に関するもので、製作が容易で、放電特性に優れ、エネ
ルギー密度の高いボタン形有機電解質電池に好適な正極
を提供することを目的とする。
Detailed Description of the Invention The present invention relates to a method for manufacturing a positive electrode of a battery, particularly an organic electrolyte battery using a light metal as a negative electrode active material and cupric oxide as a positive electrode active material, which is easy to manufacture and has discharge characteristics. The purpose of this invention is to provide a positive electrode suitable for a button-type organic electrolyte battery with excellent energy density and high energy density.

従来、電解質としてプロピルカーボネートやyープチロ
ラクトンなどの有機溶媒に溶質として過塩素酸リチウム
やホウフツ化リチウム等を溶解した有機電解質を用い、
リチウム,マグネシウム,アルミニウム等の軽金属を負
極とし、金属のハロゲン化物や酸化物を正極として使用
する有機電解質電池が知られている。
Conventionally, an organic electrolyte in which a solute such as lithium perchlorate or lithium borofluoride is dissolved in an organic solvent such as propyl carbonate or y-butyrolactone is used.
Organic electrolyte batteries are known in which a light metal such as lithium, magnesium, or aluminum is used as a negative electrode and a metal halide or oxide is used as a positive electrode.

一般的に電池は全て正極,負極,セパレータおよび電解
液、そしてそれらを包む電池容器とから構成されている
Generally, a battery is composed of a positive electrode, a negative electrode, a separator, an electrolytic solution, and a battery container that encloses them.

そしてこの電池容積は、自由な大きさ、形状をとること
はできず、機器に組込むために定められた容積,形状を
有しているのが一般的であり、電池の特性として、でき
るだけ小形で高エネルギーが取り出せることが望ましい
。近年薄形のウオッチや電卓の開発に伴って、特に高エ
ネルギーであり、放電特性の優れた一次電池の要望が大
である。リチウムを負極,酸化第二銅を正極活物質とし
たボタン形電池においては、酸化第二銅が導電性を有し
ないために、アセチレンブラック等の導電村および四フ
ツ化エチレン−六フッ化プロピレン共重合体等の結着材
を加えて加圧成形したべレット状の正極を用いていた。
The capacity of this battery cannot take any size or shape; it generally has a predetermined volume and shape for incorporation into a device. It is desirable that high energy can be extracted. In recent years, with the development of thin watches and calculators, there has been a strong demand for primary batteries with particularly high energy and excellent discharge characteristics. In button-type batteries with lithium as the negative electrode and cupric oxide as the positive active material, cupric oxide has no conductivity, so conductive materials such as acetylene black and ethylene tetrafluoride-propylene hexafluoride are used. A pellet-shaped positive electrode was used that was press-molded with a binder such as a polymer added.

しかしながら、導電材や結着材を用いているため、活物
質としての酸化第二鋼の充填量が減少することより、放
電容量が低下し、高エネルギー密度電池は望めなかった
。一方、導電村、結着材を最小にし充填密度を上げるこ
とも可能であるが、この電池系においては、放電反応に
伴って正極が膨潤することより、充填密度を上げすぎる
と、放電末期には電池容器のふくれを生じ、使用機器の
池部品を圧迫するという欠点があり、電池容器のふくれ
を最小限にする程度の充填量とする必要性があった。し
たがって、適当な充填量の場合には、正極としての酸化
第二銅のべレットは、粉末を加圧成形しているために厚
みが減少し、極間距離の増加,集軍体との接触不良を生
じる。以上の点から、スベーサとして含液性を有した金
属多孔体7を第3図または第4図のように負極3または
正極5の背面に挿入するか、または第5図のようにポリ
プロピレンなどの不織布7′を両極間に挿入して電池を
構成していた。
However, since a conductive material and a binder are used, the filling amount of second oxidized steel as an active material decreases, resulting in a decrease in discharge capacity, and a high energy density battery cannot be expected. On the other hand, it is possible to increase the packing density by minimizing the conductive particles and binder, but in this battery system, the positive electrode swells with the discharge reaction, so if the packing density is increased too much, it will cause problems at the end of discharge. This has the drawback of causing the battery container to bulge and putting pressure on the pond parts of the equipment in which it is used, so it is necessary to fill the battery container with a filling amount that minimizes the bulge. Therefore, in the case of an appropriate filling amount, the cupric oxide pellet used as the positive electrode will have a reduced thickness due to the pressure molding of the powder, an increase in the distance between the electrodes, and a reduction in the contact with the mass concentrator. Causes defects. From the above points, it is recommended to insert a liquid-retaining metal porous body 7 as a substrate into the back surface of the negative electrode 3 or the positive electrode 5 as shown in FIG. 3 or 4, or to use a material such as polypropylene as shown in FIG. A battery was constructed by inserting a nonwoven fabric 7' between the two electrodes.

しかしながら、このようなスベーサを挿入すると、その
容積分だけ活物質の量は減少する不都合がある。また、
正,負極間に不織布7′等を挿入することは、含浸され
た有機電解質の比電導度が水溶液に比べて約2桁低いこ
とより、内部抵抗の増大による放電電圧の低下をまねき
、特に、放電初期の電圧の立ち上がりが悪いという欠点
があった。また、電気伝導性の良い酸化鋼のみからなる
正極板の製造法として、特開昭51−12272y号公
報記載の酸化銅とアルカリ金属酸化物、例えばLi20
やNa20との混合物を焼成して、アルカリ金属を酸化
鋼中に間落させて作る方法がある。この方法により電気
伝導性に優れた多孔体の正極を得ることができるが、次
のような欠点がある。
However, when such a spacer is inserted, the amount of active material is disadvantageously reduced by the volume thereof. Also,
Inserting a nonwoven fabric 7' or the like between the positive and negative electrodes will cause a decrease in discharge voltage due to an increase in internal resistance, since the specific conductivity of the impregnated organic electrolyte is about two orders of magnitude lower than that of an aqueous solution. There was a drawback that the voltage rise at the initial stage of discharge was slow. In addition, as a method for manufacturing a positive electrode plate made only of oxidized steel with good electrical conductivity, copper oxide and alkali metal oxides, such as Li20
There is a method of making the alkali metal by firing a mixture with oxidized steel and Na20 to drop the alkali metal into oxidized steel. Although a porous positive electrode with excellent electrical conductivity can be obtained by this method, it has the following drawbacks.

すなわちアルカリ金属酸化物の融点は相当高く、例えば
Li20では170000以上である。このため、酸化
鋼中にアルカリ金属を固溶させる時には、酸化鋼、アル
カリ金属酸化物の両方が固体であり、固相−固相の反応
となる。酸化鋼表面のアルカリ金属酸化物の分布は、固
体であるため不均一となりやすく、そのため数度にわた
って、加熱、粉砕のサイクルを繰り返す必要がある。侍
開昭51−12272y号公報においても、まず酸化鋼
中ヘアルカリ金属を間落させるために一度加熱し、得ら
れた固港体を一度200メッシュのふるいを通るように
して、その後もう一度加熱して成形された焼緒正極板を
得ている。本発明は、この従釆の酸化リチウムの代りに
炭酸リチウムを用いることを特徴としている。
That is, the melting point of the alkali metal oxide is quite high, for example, Li20 has a melting point of 170,000 or more. Therefore, when an alkali metal is dissolved in oxidized steel, both the oxidized steel and the alkali metal oxide are solid, and a solid phase-solid reaction occurs. The distribution of alkali metal oxides on the surface of oxidized steel tends to be non-uniform because it is a solid, so it is necessary to repeat the cycle of heating and crushing several times. In Samurai Publication No. 51-12272y, the oxidized steel is first heated once in order to eliminate the alkali metals, and the obtained hard shell is passed through a 200-mesh sieve once, and then heated again. A molded sakio positive electrode plate is obtained. The present invention is characterized in that lithium carbonate is used in place of this secondary lithium oxide.

炭酸リチウムの融点は618℃であり、この温度以上で
は炭酸リチウムは液体となる。炭酸リチウムと酸化鋼の
混合物を炭酸リチウムの融点以上、酸化鋼の融点(10
2がC)以下の温度に加熱すると、まず炭酸リチウムが
溶融して、酸化鋼の表面を均一にぬらすようになり、そ
の後炭酸リチウムと酸化銅の反応が徐々に進行して、リ
チウム酸化物が固溶した酸化鋼となる。この方法によれ
ば、リチウムの分布が従釆の方法に比べて均一となり、
一度の加熱で十分である。したがって、炭酸リチウムを
用いることにより、炭酸リチウムと酸化銅の混合成形体
を一度加熱するだけで、リチウムが均一に固溶して電気
伝導性が良好で、また強度も十分大きい正極板を得るこ
とができる。以下本発明の実施例を説明する。
The melting point of lithium carbonate is 618°C, and above this temperature, lithium carbonate becomes a liquid. A mixture of lithium carbonate and oxidized steel is heated to a temperature higher than the melting point of lithium carbonate, the melting point of oxidized steel (10
When 2 is heated to a temperature below C), lithium carbonate first melts and uniformly wets the surface of the oxidized steel, and then the reaction between lithium carbonate and copper oxide proceeds gradually, and lithium oxide is formed. It becomes solid solution oxidized steel. According to this method, the distribution of lithium is more uniform than in the secondary method,
Heating once is sufficient. Therefore, by using lithium carbonate, it is possible to obtain a positive electrode plate with good electrical conductivity and sufficient strength by uniformly dissolving lithium into solid solution by simply heating a mixed molded body of lithium carbonate and copper oxide once. Can be done. Examples of the present invention will be described below.

まず酸化第二銅粉末と炭酸リチウム粉末とをモル比で聡
:2の割合で混合し、その混合物55雌を直径4.2肌
,厚さ1.仇舷の円盤状に成形した。この成形体の多孔
度37%であった。次にこの成形体を大気中で温度80
0qoにて5時間焼成し、酸化第二銅と炭酸リチウムを
反応,競結させ、多孔性正極を得た。正極の多孔度は、
焼成前のべレットで、多孔度40%以上にすると、成形
後の取り扱い中にくずれやすく、40%以下の多孔度と
することが望ましい。また、35%以下の多孔度では、
ベレットの厚みが減少し、電池に組み入れた場合、正極
端子を兼ねるケースとの接触が不安定である。炭酸リチ
ウム粉末の添加は、酸化第二銅粉末のみでは、焼結後の
べレットもくずれやすく、取り扱い困難であり、炭酸リ
チウムを添加し、焼結させることによって、酸化第二銅
と反応し、リチウム金属酸化物が固落した酸化第二銅と
なり、電気伝導性が著しく増大し、また凝結後のべレッ
トも十分取り扱うことが可能な強度になる。
First, cupric oxide powder and lithium carbonate powder were mixed at a molar ratio of 2:2, and the mixture was mixed with a diameter of 4.2 mm and a thickness of 1.5 mm. It was shaped like a disc on the side of the ship. The porosity of this molded body was 37%. Next, this molded body was placed in the atmosphere at a temperature of 80°C.
The product was fired at 0 qo for 5 hours to cause the cupric oxide and lithium carbonate to react and bind together, thereby obtaining a porous positive electrode. The porosity of the positive electrode is
If the pellet before firing has a porosity of 40% or more, it will easily collapse during handling after molding, so it is desirable to have a porosity of 40% or less. In addition, with a porosity of 35% or less,
The thickness of the pellet is reduced, and when it is incorporated into a battery, the contact with the case, which also serves as the positive terminal, is unstable. Addition of lithium carbonate powder is difficult when using only cupric oxide powder, as the pellet after sintering tends to crumble and is difficult to handle. By adding lithium carbonate and sintering, it reacts with cupric oxide, The lithium metal oxide solidifies into cupric oxide, which significantly increases electrical conductivity, and the pellet after solidification becomes strong enough to be handled.

第1図は混合物中の炭酸リチウムの量と得られた暁結多
孔体の電気伝導度。
Figure 1 shows the amount of lithium carbonate in the mixture and the electrical conductivity of the resulting precipitated porous material.

(Q・肌)の関係を示すもので、炭酸リチウム含有量1
.5〜3.0モル%の範囲で、電気伝導度が最大となる
。焼成温度については、実施例では、800qoにて焼
成したが、炭酸リチウム,酸化第二銅の融点がそれぞれ
、618qo、1026qoであり、618qo以下で
は、電気伝導性が低く、競結も十分でなかった。
It shows the relationship between (Q and skin), and the lithium carbonate content is 1
.. The electrical conductivity is maximum in the range of 5 to 3.0 mol%. Regarding the firing temperature, in the example, firing was performed at 800 qo, but the melting points of lithium carbonate and cupric oxide are 618 qo and 1026 qo, respectively, and below 618 qo, the electrical conductivity is low and the competitive bond is not sufficient. Ta.

また1026qo以上では、酸化第二銅が溶融し、ベレ
ットとしては存在しなかった。618oC〜102がo
の範囲においては、大きな差はなく、電気伝導性,競精
とも良好であった。
Moreover, at 1026 qo or more, cupric oxide melted and did not exist as pellets. 618oC~102o
There was no big difference in the range of , and both electrical conductivity and sperm competition were good.

以上のようにして得られた多孔性正極を用いた電池にお
いては、極間距離を最4・限にし、正極それ自体保液性
を有し電解液の表面接触が最大限に行なわれることによ
り、反応表面積が増加し、放鰭特性の向上および安定化
が望めるとともに、導亀村や結着材、または含液材等の
スベーサを含まず、放電容量のすぐれた高エネルギー密
度電池が期待できる。
In the battery using the porous positive electrode obtained in the above manner, the distance between the electrodes is set to a maximum of 4 mm, and the positive electrode itself has a liquid-retaining property to maximize the surface contact of the electrolyte. , the reaction surface area is increased, and it is expected that the radiation fin characteristics will be improved and stabilized, and a high-energy density battery with excellent discharge capacity can be expected because it does not contain any substrates such as lead-in capacitors, binding materials, or liquid-containing materials.

第2図は上記の正極を用いたりチウム電池を示すもので
ある。
FIG. 2 shows a lithium battery using the above-mentioned positive electrode.

1はステンレス鋼製上ケースで、その周縁にポリプロピ
レン製パッキング2を挿入してある。
Reference numeral 1 denotes an upper case made of stainless steel, and a packing 2 made of polypropylene is inserted around its periphery.

この上ケース1の内面に、直径4.6帆,厚さ0.9仇
岬の円板状金属リチウム負極3を圧着し、ポリプロピレ
ンからなるマイクロポーラスフィルムのセパレータ4、
本発明の多孔性正極5を挿入した後、1モル/その過塩
素酸リチウムを溶解したプロピレンカーボネートからな
る電解液を注入し、ステンレス鋼製下ケース6をパッキ
ング2に合わせ、下ケースの口縁をかしめて密封してあ
る。上記の構成の電池Aと、各々酸化第二節粉末を成形
した正極を用いた第3図,第4図,第5図に示す従来の
構成の電池B,C,Dおよび第2図と同様の構成である
が酸化第二銅100重量部と導鰭材5重軍部と結着剤7
重量部の混合物を成形した正極を用いた電池Eについて
、2び0で1雛0の定抵抗放電をしたときの放電特性を
第6図に示す。
A disk-shaped metal lithium negative electrode 3 having a diameter of 4.6 mm and a thickness of 0.9 mm is crimped onto the inner surface of the upper case 1, and a separator 4 made of a microporous film made of polypropylene,
After inserting the porous positive electrode 5 of the present invention, an electrolytic solution consisting of propylene carbonate in which 1 mole of lithium perchlorate is dissolved is injected, and the stainless steel lower case 6 is aligned with the packing 2, and the opening of the lower case is It is caulked and sealed. Battery A with the above configuration, and batteries B, C, D with conventional configurations shown in Figures 3, 4, and 5, each using a positive electrode made of oxidized second node powder, and batteries similar to Figure 2. The composition is 100 parts by weight of cupric oxide, 5 parts of guide fin material, and 7 parts of binder.
FIG. 6 shows the discharge characteristics when a constant resistance discharge of 2 and 0 and 1 and 0 was performed for a battery E using a positive electrode formed from a mixture of 2 and 0 parts by weight.

第6図から明らかなように、本発明による正極を用いた
電池は、電圧安定性も良好であり、放電時間も従釆品に
比べて約15%優れている。以上のように本発明は、製
作が容易で、放電特性に優れ、特にエネルギー密度の高
いボタン形の有機電解質電池を与える正極を提供するも
のである。
As is clear from FIG. 6, the battery using the positive electrode according to the present invention has good voltage stability and is about 15% better in discharge time than the conventional product. As described above, the present invention provides a positive electrode that is easy to manufacture, has excellent discharge characteristics, and provides a button-shaped organic electrolyte battery that has particularly high energy density.

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

第1図は酸化第二銅と炭酸リチウムの混合物中の炭酸リ
チウムの含有量と得られた正極の電気伝導度との関係を
示す図、第2図は本発明の正極を用いたりチウム電池の
縦断面図、第3〜5図は従釆の電池の縦断面図、第6図
は各種電池の放電時性を示す。 第1図 第2図 第3図 第4図 第5図 第6図
Fig. 1 shows the relationship between the content of lithium carbonate in a mixture of cupric oxide and lithium carbonate and the electrical conductivity of the obtained positive electrode, and Fig. 2 shows the relationship between the content of lithium carbonate in a mixture of cupric oxide and lithium carbonate and the electrical conductivity of the obtained positive electrode. FIGS. 3 to 5 are longitudinal sectional views of subordinate batteries, and FIG. 6 shows discharge characteristics of various batteries. Figure 1 Figure 2 Figure 3 Figure 4 Figure 5 Figure 6

Claims (1)

【特許請求の範囲】 1 酸化第二銅粉末と炭酸リチウムとの混合物を成形し
、この成形体を酸化第二銅の融点以下でかつ炭酸リチウ
ムの融点以上の温度で焼結して酸化第二銅の多孔体を得
ることを特徴とする電池用正極の製造法。 2 前記混合物の炭酸リチウムの含有量が1.5〜3.
0モル%である特許請求の範囲第1項記載の電池用正極
の製造法。 3 前記成形体の多孔度が35〜40%である特許請求
の範囲第1項または第2項記載の電池用正極の製造法。
[Claims] 1. A mixture of cupric oxide powder and lithium carbonate is molded, and the molded body is sintered at a temperature below the melting point of cupric oxide and above the melting point of lithium carbonate to form cupric oxide powder. A method for producing a positive electrode for a battery, characterized by obtaining a porous copper body. 2. The content of lithium carbonate in the mixture is 1.5 to 3.
The method for producing a positive electrode for a battery according to claim 1, wherein the content is 0 mol%. 3. The method for producing a battery positive electrode according to claim 1 or 2, wherein the molded body has a porosity of 35 to 40%.
JP54055982A 1979-05-08 1979-05-08 Manufacturing method of battery positive electrode Expired JPS6031067B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54055982A JPS6031067B2 (en) 1979-05-08 1979-05-08 Manufacturing method of battery positive electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54055982A JPS6031067B2 (en) 1979-05-08 1979-05-08 Manufacturing method of battery positive electrode

Publications (2)

Publication Number Publication Date
JPS55148367A JPS55148367A (en) 1980-11-18
JPS6031067B2 true JPS6031067B2 (en) 1985-07-19

Family

ID=13014278

Family Applications (1)

Application Number Title Priority Date Filing Date
JP54055982A Expired JPS6031067B2 (en) 1979-05-08 1979-05-08 Manufacturing method of battery positive electrode

Country Status (1)

Country Link
JP (1) JPS6031067B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57174863A (en) * 1981-04-20 1982-10-27 Hitachi Maxell Ltd Organic electrolyte cell
JPS62226560A (en) * 1986-03-27 1987-10-05 Fuji Elelctrochem Co Ltd Nonaqueous electrolyte battery

Also Published As

Publication number Publication date
JPS55148367A (en) 1980-11-18

Similar Documents

Publication Publication Date Title
US4658498A (en) Process for producing rechargeable electrochemical device
JPH11191417A (en) Non-aqueous electrolyte secondary battery and method of manufacturing the same
JP5827103B2 (en) Small non-aqueous electrolyte secondary battery and manufacturing method thereof
EP0573040B1 (en) A positive electrode for lithium secondary battery and its method of manufacture, and a nonaqueous electrolyte lithium secondary battery employing the positive electrode
JPS623547B2 (en)
JP2003217663A (en) Non-aqueous electrolyte battery
US3998658A (en) High voltage organic electrolyte batteries
JPS6031067B2 (en) Manufacturing method of battery positive electrode
JPS6335069B2 (en)
JPS62234876A (en) Manufacture of battery
JP2002110152A (en) Non-aqueous electrolyte secondary battery
JP6734155B2 (en) Alkaline battery
JPH10255766A (en) Non-aqueous electrolyte secondary battery
JP2000277119A (en) Lithium battery
JP2608561B2 (en) Stacked battery
JPH05325961A (en) Lithium battery
JP2612002B2 (en) Battery
US3989543A (en) Electrochemical cell having lead fluoride cathode
JP2812943B2 (en) Organic electrolyte battery
CN100411241C (en) organic electrolyte battery
JP2002203559A (en) Non-aqueous electrolyte secondary battery and method for producing positive electrode active material
JPS60170172A (en) rechargeable electrochemical device
JP3176702B2 (en) Lithium battery
JPH06231767A (en) Lithium secondary battery positive electrode, its manufacture, and non-aqueous electrolyte lithium secondary battery using this electrode
JPS5849965B2 (en) Manufacturing method of lithium ion conductive solid electrolyte