JPH01149362A - Nonaqueous solvent secondary battery - Google Patents

Nonaqueous solvent secondary battery

Info

Publication number
JPH01149362A
JPH01149362A JP62307973A JP30797387A JPH01149362A JP H01149362 A JPH01149362 A JP H01149362A JP 62307973 A JP62307973 A JP 62307973A JP 30797387 A JP30797387 A JP 30797387A JP H01149362 A JPH01149362 A JP H01149362A
Authority
JP
Japan
Prior art keywords
metal core
positive electrode
metal
secondary battery
solvent secondary
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
Application number
JP62307973A
Other languages
Japanese (ja)
Inventor
Junichi Yamaki
準一 山木
Yoji Sakurai
庸司 櫻井
Kuniaki Inada
稲田 圀昭
Katsuharu Ikeda
克治 池田
Hiroyoshi Nose
博義 能勢
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.)
FDK Twicell Co Ltd
NTT Inc
Original Assignee
Toshiba Battery Co Ltd
Nippon Telegraph and Telephone Corp
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 Toshiba Battery Co Ltd, Nippon Telegraph and Telephone Corp filed Critical Toshiba Battery Co Ltd
Priority to JP62307973A priority Critical patent/JPH01149362A/en
Publication of JPH01149362A publication Critical patent/JPH01149362A/en
Pending 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
    • 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
    • H01M4/64Carriers or collectors
    • 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

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

PURPOSE:To retard gas evolution on the interface between a metal core and a positive mix in charge-discharge by forming a positive electrode by covering a metal core with the positive mix containing an active material through the conductive layer of a metal which constitutes the active material or the conductive resin layer containing the metal. CONSTITUTION:For example, metallic vanadium conductive layers 9 are formed on both sides of a metal core 8, and sheets containing vanadium pentoxide are pressed against both sides of the metal core 8 through the conductive layers 9 to form a positive mix 10 and a positive electrode is obtained. The conductivity on the interface of the metal core 8 and the positive mix 10 is increased and the generation of conductivity detective part is prevented. The current density on the interface on which gas evolved by the reaction of an electrolyte with the metal core is made uniform. Gas evolution caused by uneven current density can be retarded.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、非水溶媒二次電池に関し、特に正極の構造を
改良した非水溶媒二次電池に係わる。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a non-aqueous solvent secondary battery, and particularly to a non-aqueous solvent secondary battery with an improved structure of a positive electrode.

[従来の技術] 近年、金属カルコゲン化合物を正極合剤の活物質とし、
リチウム等のアルカリ金属を負極として用いる非水溶媒
二次電池は高いエネルギーを有するものとして注目され
ている。その巾でも最近、カルコゲン酸化物を生活物質
として、この酸化物とリチウムあるいはその酸化物の混
合物よりなる活物質を含む正極合剤を正極に用い、負極
にリチウムを用いた非水溶媒二次電池が開発されている
[Prior art] In recent years, metal chalcogen compounds have been used as active materials in positive electrode mixtures,
Non-aqueous solvent secondary batteries that use an alkali metal such as lithium as a negative electrode are attracting attention as having high energy. In recent years, nonaqueous solvent secondary batteries have been developed that use chalcogen oxide as a living material, use a positive electrode mixture containing an active material made of this oxide and lithium or a mixture of these oxides as the positive electrode, and use lithium as the negative electrode. is being developed.

このような電池としては、例えば二硫化チタン−リチウ
ム電池、二硫化モリブデン−リチウム電池、二酸化マン
ガン−リチウム電池等が知られている。
Known examples of such batteries include titanium disulfide-lithium batteries, molybdenum disulfide-lithium batteries, manganese dioxide-lithium batteries, and the like.

これら非水溶媒二次電池の正極は、ニッケル、ステンレ
ス鋼製の網、エキスバンドメタル等の金属芯体に活物質
、結着剤を含むシート状の正極合剤を圧着一体化した構
造になっている。
The positive electrodes of these nonaqueous solvent secondary batteries have a structure in which a sheet-like positive electrode mixture containing an active material and a binder is bonded to a metal core made of nickel, stainless steel mesh, expanded metal, etc. ing.

[発明が解決しようとする問題点] しかしながら、上述した非水溶媒二次電池の正極は、製
造プロセスが簡単であり電池の製造コストを安価にでき
るにもかかわらず実用化されていない。これは、前述し
た正極を用いて電池を製造すると電池の充放電サイクル
寿命が短くなり個々の放電特性が均質でなくなるという
ことによる。
[Problems to be Solved by the Invention] However, the above-described positive electrode for a non-aqueous solvent secondary battery has not been put into practical use, although the manufacturing process is simple and the manufacturing cost of the battery can be reduced. This is because if a battery is manufactured using the above-mentioned positive electrode, the charge/discharge cycle life of the battery will be shortened and the individual discharge characteristics will not be homogeneous.

即ち、前記非水溶媒二次電池の正極において、前記金属
芯体と正極合剤との界面に導電性不良箇所や圧着不良箇
所、剥離箇所があると、電池反応が行われる際に該圧着
界面の電流分布は不均一となり電流密度の粗密化が生じ
る。この電流密度の粗密化は、電解液の分解電圧より高
い電圧で反応を行なう部分を前記界面に生じさせる。こ
のため、このような導電性不良箇所等が存在したまま電
池反応が行われると、前述した電解液の分解電圧より高
い電圧で反応がなされる部分において前記正極合剤中の
電解液と金属芯体が反応し電解液の分解が生じて水素ガ
ス、炭酸ガス等のガスが発生する。このガスは電池の充
放電の繰返しの度に前記金属芯体と正極合剤の界面に少
しづつ蓄積され、該正極合剤を金属芯体から少しづつ剥
離せしめる。
That is, in the positive electrode of the non-aqueous solvent secondary battery, if there are poor conductivity, poor crimping, or peeling at the interface between the metal core and the positive electrode mixture, the crimping interface will be damaged during the battery reaction. The current distribution becomes non-uniform and the current density becomes coarser. This coarsening of the current density creates a portion at the interface where a reaction occurs at a voltage higher than the decomposition voltage of the electrolytic solution. For this reason, if a battery reaction is performed while such conductive defects exist, the electrolyte in the positive electrode mixture and the metal core will be mixed in the areas where the reaction is carried out at a voltage higher than the decomposition voltage of the electrolyte. The body reacts and the electrolyte decomposes, producing hydrogen gas, carbon dioxide gas, and other gases. This gas accumulates little by little at the interface between the metal core and the positive electrode mixture each time the battery is repeatedly charged and discharged, causing the positive electrode mixture to be gradually peeled off from the metal core.

従って、前記金属芯体と正極合剤との界面での接触面積
は充放電の繰り返しに伴い少しづつ減少し、該金属芯体
と正極合剤との間の電子の伝導が著しく低下する。その
結果、電池の充放電の繰り返しに伴って前記正極合剤が
十分な機能を有するにもかかわらず充放電サイクル寿命
が低下し、電池性能の不均一化を生じさせるという問題
があった。
Therefore, the contact area at the interface between the metal core and the positive electrode mixture gradually decreases with repeated charging and discharging, and the conduction of electrons between the metal core and the positive electrode mixture decreases significantly. As a result, as the battery is repeatedly charged and discharged, the charge/discharge cycle life decreases even though the positive electrode mixture has sufficient functionality, resulting in a problem that the battery performance becomes non-uniform.

本発明は、上記従来の問題点を解決するためになされた
もので、前記金属芯体に対して正極合剤を電気的に良好
に被覆して充放電サイクル時においてこれらの界面にガ
ス等が発生するのを抑制した非水溶媒二次電池を提供し
ようとするものである。
The present invention has been made in order to solve the above-mentioned conventional problems, and the metal core is electrically well coated with a positive electrode mixture so that gas, etc. can be formed at these interfaces during charging and discharging cycles. The present invention aims to provide a non-aqueous solvent secondary battery that suppresses the occurrence of this problem.

[問題点を解決するための手段] 本発明は、金属芯体に活物質を含む正極合剤を該活物質
を構成する金属の導電層もしくはその金属を含む導電性
樹脂層を介し被覆した構造の正極を具備したことを特徴
とする非水溶媒二次電池である。
[Means for Solving the Problems] The present invention provides a structure in which a metal core is coated with a positive electrode mixture containing an active material via a conductive layer of a metal constituting the active material or a conductive resin layer containing the metal. This is a non-aqueous solvent secondary battery characterized by comprising a positive electrode.

上記金属芯体としては例えば、ニッケル、鉄、ニッケル
メッキを施した鉄、ステンレス鋼などの金属からなる金
網、エキスバンドメタル、パンチトメタル、金属箔等を
挙げることができる。
Examples of the metal core include a wire mesh made of metal such as nickel, iron, nickel-plated iron, and stainless steel, expanded metal, punched metal, and metal foil.

上記正極合剤は、活物質と共に導電材、結着剤とを混合
して製造され、必要に応じてリチウムを含む組成になっ
ている。ここに用いる活物質としては、例えば五酸化バ
ナジウム、二硫化チタン、二硫化モリブデン等のカルコ
ゲン化合物を挙げることができる。前記導電材としては
、例えばアセチレンブラック、カーボンブラック等の粉
末を挙げることができる。前記結着剤としては、例えば
ポリテトラフルオロエチレン、ポリオレフィン系樹脂等
を挙げることができる。
The positive electrode mixture is manufactured by mixing an active material, a conductive material, and a binder, and has a composition containing lithium as necessary. Examples of the active material used here include chalcogen compounds such as vanadium pentoxide, titanium disulfide, and molybdenum disulfide. Examples of the conductive material include powders such as acetylene black and carbon black. Examples of the binder include polytetrafluoroethylene and polyolefin resin.

上記活物質を構成する金属の導電層は、例えば該金属の
イオンが含まれる電解液中で前記金属芯体をアノードと
して電気メツキを行なうことにより該金属芯体表面に形
成される。かかる金属の導電層の厚さは、3〜50.w
の範囲にすることが望ましい。この理由は、導電層の厚
さを3p未満とすると電池の使用時における変形に伴い
正極が変形し金属芯体が部分的に露出して導電性樹脂層
としての機能が損われるばかりか、十分な導電性が得ら
れなくなる恐れがある。一方、導電層の厚さが50、を
越えると金属芯体に前記金属の層を設ける工程に手間が
かかり電池の生産能力を低下させるため好ましくない。
The conductive layer of the metal constituting the active material is formed on the surface of the metal core by electroplating, for example, in an electrolytic solution containing ions of the metal, using the metal core as an anode. The thickness of such a metal conductive layer is 3 to 50. lol
It is desirable to keep it within the range of . The reason for this is that if the thickness of the conductive layer is less than 3p, the positive electrode will deform as the battery deforms during use, and the metal core will be partially exposed, which will not only impair its function as a conductive resin layer, but also Otherwise, proper conductivity may not be obtained. On the other hand, if the thickness of the conductive layer exceeds 50 mm, it is not preferable because the step of providing the metal layer on the metal core requires time and effort and reduces the production capacity of the battery.

上記導電性樹脂層は、例えばポリオレフィン系樹脂の溶
液に活物質を構成する金属の粉末を分散させ、この分散
溶液を金属芯体に塗布、乾燥することにより形成される
。ここに用いるポリオレフィン系樹脂としては例えば、
ポリエチレン、ポリプロピレン、あるいはそれ以外とし
てポリアクリル酸等を挙げることができる。
The conductive resin layer is formed, for example, by dispersing metal powder constituting the active material in a solution of a polyolefin resin, applying this dispersed solution to a metal core, and drying it. Examples of polyolefin resins used here include:
Other examples include polyethylene, polypropylene, and polyacrylic acid.

上記導電性樹脂層を構成するポリオレフィン系樹脂等の
樹脂と活物質を構成する金属との配合割合は、3〜35
重量%の濃度のポリオレフィン系樹脂溶液に対し前記金
属を10〜50%の範囲にすることが望ましい。この理
由は、金属の量を105未満とすると該樹脂層の導電性
が低下し、内部抵抗の増加を生じて電池が作動しなくな
る恐れがあり、その金属の量が50%を越えると該樹脂
層の結着力の低下を生じると共に該樹脂層を金属芯体に
均一に形成することが困難となる。
The blending ratio of the resin such as polyolefin resin constituting the conductive resin layer and the metal constituting the active material is 3 to 35%.
It is desirable that the metal content be in the range of 10 to 50% with respect to the polyolefin resin solution having a concentration of % by weight. The reason for this is that if the amount of metal is less than 10%, the conductivity of the resin layer will decrease, causing an increase in internal resistance and the battery may not work. If the amount of metal exceeds 50%, the resin layer This results in a decrease in the binding strength of the layer and makes it difficult to uniformly form the resin layer on the metal core.

上記導電性樹脂層の厚さは、5p以上の範囲であること
が好ましく特に80〜1004の範囲が望ましい。この
理由は、導電性樹脂層の厚さを5p未満にすると該導電
性樹脂層が薄すぎるため金属芯体が部分的に露出し導電
性樹脂層としての機能が損われるばかりか、十分な導電
性が得られなくなる恐れがある。特に、導電性樹脂層を
金属芯体に設ける場合の工程の手間と電池性能の安定化
の観点から、該導電性樹脂層の厚さを880−1oft
の範囲にすることが好ましい。
The thickness of the conductive resin layer is preferably in the range of 5p or more, and particularly preferably in the range of 80 to 1004p. The reason for this is that if the thickness of the conductive resin layer is less than 5p, the conductive resin layer will be too thin and the metal core will be partially exposed, which will not only impair its function as a conductive resin layer, but also prevent sufficient conductivity. There is a risk that you will not be able to have sex. In particular, from the viewpoint of the process of providing a conductive resin layer on a metal core and the stabilization of battery performance, the thickness of the conductive resin layer was set to 880-1ft.
It is preferable to keep it within the range of .

[作用] 本発明によれば、非水溶媒二次電池の金属芯体に活物質
を含む正極合剤をその活物質を構成する金属の導電層を
介し被覆して正極とすることにより、金属芯体と正極合
剤との界面の導電性が向上され、導電性不良箇所の発生
を防止できる。このため、前記金属芯体と電解液を反応
させガスを発生させる前記界面の電流密度を均一にでき
る。その結果、金属芯体への電気的に良好な接続により
、安定した放電特性を有すると共に充放電サイクル寿命
、重負荷放電特性等が改善される非水溶媒二次電池を得
ることができる。
[Function] According to the present invention, a metal core of a non-aqueous solvent secondary battery is coated with a positive electrode mixture containing an active material through a conductive layer of metal constituting the active material, thereby forming a positive electrode. The conductivity of the interface between the core and the positive electrode mixture is improved, and the occurrence of poor conductivity can be prevented. Therefore, the current density at the interface where the metal core and the electrolyte react to generate gas can be made uniform. As a result, it is possible to obtain a non-aqueous solvent secondary battery that has stable discharge characteristics and has improved charge/discharge cycle life, heavy load discharge characteristics, etc. due to good electrical connection to the metal core.

一方、前記正極合剤を金属芯体にその正極合剤の活物質
を構成する金属を含む導電性樹脂層を介して被覆するこ
とにより、該樹脂層中の金属により前記界面の導電性が
向上され、かつ前記樹脂の結着力によって該金属芯体と
正極合剤の被覆性を良好にでき、被覆不良箇所、剥離部
の発生が抑制される。従って、前記金属芯体と電解液を
反応させガスを発生させる界面の電流密度を均一にでき
ると共に、被覆不良箇所、剥離箇所の存在が抑制される
ため、前記界面において該被覆不良箇所、剥離箇所と良
好に被覆されている箇所との電気抵抗の差異から生じる
界面での電流密度の素密化を防止でき、この電流密度の
素密化にともなうガス発生を抑制することができる。そ
の結果、正極合剤の金属芯体からの剥離、脱落の防止及
び金属芯体への電気的に良好な接続により、安定した放
電特性を有すると共に充放電サイクル寿命、重負荷放電
特性等が改善される非水溶媒二次電池を得ることができ
る。
On the other hand, by coating the metal core with the positive electrode mixture via a conductive resin layer containing a metal constituting the active material of the positive electrode mixture, the metal in the resin layer improves the conductivity of the interface. Moreover, due to the binding force of the resin, the coating properties of the metal core and the positive electrode mixture can be improved, and the occurrence of poor coating and peeling parts can be suppressed. Therefore, the current density at the interface where the metal core and the electrolytic solution react to generate gas can be made uniform, and the presence of defective coatings and peeling spots is suppressed, so that the defective coating and peeling spots at the interface are suppressed. It is possible to prevent the current density from becoming denser at the interface due to the difference in electrical resistance between the coated portion and the well-coated portion, and it is possible to suppress gas generation due to the denser current density. As a result, by preventing the positive electrode mixture from peeling off or falling off from the metal core and by providing good electrical connection to the metal core, it has stable discharge characteristics and improves charge/discharge cycle life, heavy load discharge characteristics, etc. A non-aqueous solvent secondary battery can be obtained.

[実施例] 以下、本発明を円筒型の五酸化バナジウム−リチウム二
次電池に適用した例について第1図を参照して詳細に説
明する。
[Example] Hereinafter, an example in which the present invention is applied to a cylindrical vanadium pentoxide-lithium secondary battery will be described in detail with reference to FIG. 1.

実施例1 図中の1は、底部に絶縁板2が配置された負極端子を兼
ねる有底円筒型の金属製の容器である。
Example 1 Reference numeral 1 in the figure is a bottomed cylindrical metal container that also serves as a negative electrode terminal and has an insulating plate 2 disposed at the bottom.

この容器I内には、円筒型の発電要素8が収納されてい
る。この発電要素3は、金属リチウムからなる負極4と
多孔性ポリプロピレン薄膜にプロピレンカーボネイトを
含浸したセパレータ5と、後述する正極Bとをこの順序
で積層して帯状物とし、この帯状物を渦巻き状に巻回す
ることにより構成されている。
Inside this container I, a cylindrical power generation element 8 is housed. This power generation element 3 consists of a negative electrode 4 made of metallic lithium, a separator 5 made of a porous polypropylene thin film impregnated with propylene carbonate, and a positive electrode B (described later), which are laminated in this order to form a band-like object, and this band-like object is formed into a spiral shape. It is constructed by winding.

前記正極6は次のような方法により製造される。The positive electrode 6 is manufactured by the following method.

まず、長手方向に沿う一側端にチタン箔のリード端子7
がスポット溶接により設けられたニッケル製の板状金属
芯体8を、アノードとして金属バナジウムイオンが含ま
れる電解液中で電気メツキを行なうことにより該金属芯
体8両面に金属バナジウムの導電層9を形成する。つづ
いて、十分に混合された五酸化バナジウム粉末と五酸化
リン粉末との混合物を800℃で溶融し、この溶融物を
ドライアイスで冷却されている銅板上に流し出し、急冷
して非晶質とし、これを184の粒径になるまで粉砕し
て活物質とし、この活物質とポリテトラフルオロエチレ
ン粉末0.5gとを混合し、0.4Mの厚みのシート状
にロール成形法により成形した後、このシート状物を前
記金属芯体8の両面の導電層9に圧着一体化して正極合
剤10を成形することにより正極6を製造した(第2図
(a)、(b)図示)。つまり、正極6はリード端子7
が接続された金属芯体8両面に導電層9を介して正極合
剤lOを被覆した構造になっている。
First, a titanium foil lead terminal 7 is attached to one end along the longitudinal direction.
A conductive layer 9 of metal vanadium is formed on both sides of the metal core 8 by electroplating the plate metal core 8 made of nickel, which is provided by spot welding, in an electrolytic solution containing metal vanadium ions as an anode. Form. Next, a well-mixed mixture of vanadium pentoxide powder and phosphorus pentoxide powder was melted at 800°C, and the melt was poured onto a copper plate cooled with dry ice, and rapidly cooled to form an amorphous material. This was ground to a particle size of 184 mm to obtain an active material, and this active material was mixed with 0.5 g of polytetrafluoroethylene powder and formed into a sheet with a thickness of 0.4 M using a roll forming method. Thereafter, this sheet-like material was crimped and integrated with the conductive layers 9 on both sides of the metal core 8 to form a positive electrode mixture 10, thereby manufacturing the positive electrode 6 (as shown in FIGS. 2(a) and 2(b)). . In other words, the positive electrode 6 is the lead terminal 7
The structure is such that both surfaces of the metal core 8 to which the electrodes are connected are coated with a positive electrode mixture lO via a conductive layer 9.

前記容器lの開口部付近には、絶縁性封n板11がかし
めにより液密に設けられており、かつ該封目板11には
正極端子12が嵌合されている。この正極端子12には
、前記リード端子7がスポット溶接により接続されてい
る。なお、前記負極4にはニッケル箔のリード端子13
が圧着され、かつ該リード端子13は前記容器lの内側
面にスポット溶接により接続されている。
An insulating sealing plate 11 is provided in the vicinity of the opening of the container l in a fluid-tight manner by caulking, and a positive electrode terminal 12 is fitted into the sealing plate 11. The lead terminal 7 is connected to this positive electrode terminal 12 by spot welding. Note that the negative electrode 4 has a lead terminal 13 made of nickel foil.
is crimped, and the lead terminal 13 is connected to the inner surface of the container l by spot welding.

比較例 導電性樹脂層を介さず直接金属芯体に正極合剤を被覆し
て構成される正極を用いた以外、上記実施例1と同様な
構造の非水溶媒二次電池を組立てた。
Comparative Example A non-aqueous solvent secondary battery was assembled with the same structure as in Example 1, except that a positive electrode was used in which a positive electrode mixture was directly coated on a metal core without intervening a conductive resin layer.

しかして、本実施例1及び比較例の非水溶媒二次電池に
ついて20℃の室温で150mAの電流により7時間充
電を行ない、この後t、OVの放電電圧を示すまで放電
を行なう工程を1サイクルとして電池容量の測定を行な
う放電容量維持率の特性評価試験を行なった。その結果
、第3図に示す特性図を得た。なお、図中のAは本実施
例1の非水溶媒二次電池の特性線を、Bは比較例の非水
溶媒二次電池の特性線を示す。この第3図から明らかな
ように本実施例1の二次電池は、サイクル数の増加に伴
う放電容量維持率の低下は穏やかで優れた放電特性を有
する。これに対し、比較例の二次型゛  池においては
サイクル数の増加に伴う放電容量維持率の低下が著しく
なる。特に、サイクル数が100回付近になると放電容
量維持率は極端に低下する。
Therefore, the nonaqueous solvent secondary batteries of Example 1 and Comparative Example were charged for 7 hours at a room temperature of 20° C. with a current of 150 mA, and then discharged until a discharge voltage of t, OV was shown. A characteristic evaluation test of discharge capacity retention rate was conducted in which battery capacity was measured as a cycle. As a result, a characteristic diagram shown in FIG. 3 was obtained. In addition, A in the figure shows the characteristic line of the non-aqueous solvent secondary battery of Example 1, and B shows the characteristic line of the non-aqueous solvent secondary battery of the comparative example. As is clear from FIG. 3, the secondary battery of Example 1 has excellent discharge characteristics in which the discharge capacity retention rate decreases moderately as the number of cycles increases. On the other hand, in the secondary type battery of the comparative example, the discharge capacity retention rate decreases significantly as the number of cycles increases. In particular, when the number of cycles approaches 100, the discharge capacity retention rate decreases extremely.

また、本実施例1及び比較例の非水溶媒二次電池につい
て750mAの負荷による重負荷放電を行なった。その
結果、第4図に示す放電時間と電池電圧との関係の特性
図を得た。図中のAは本実施例1の非水溶媒二次電池の
特性線を、Bは比較例の非水溶媒二次電池の特性線を示
す。この第4図から明らかなように本実施例1の二次電
池は、比較例の二次電池に比べて放電電圧が急激に減少
するまでの放電時間が長くなり、重負荷における放電特
性が大幅に改善されていることがわかる。特に比較例の
電池は、放電時間が25分を越えると急激に電圧が低下
するのに対して、実施例1の電池は45分を越えても急
激な電圧低下が生じず、安定した電池特性を示している
In addition, heavy load discharge was performed with a load of 750 mA for the non-aqueous solvent secondary batteries of Example 1 and Comparative Example. As a result, a characteristic diagram of the relationship between discharge time and battery voltage shown in FIG. 4 was obtained. In the figure, A indicates the characteristic line of the non-aqueous solvent secondary battery of Example 1, and B indicates the characteristic line of the non-aqueous solvent secondary battery of the comparative example. As is clear from FIG. 4, the secondary battery of Example 1 has a longer discharge time until the discharge voltage suddenly decreases than the secondary battery of the comparative example, and the discharge characteristics under heavy loads are significantly improved. It can be seen that this has been improved. In particular, the battery of Comparative Example had a rapid voltage drop when the discharge time exceeded 25 minutes, whereas the battery of Example 1 did not experience a sudden voltage drop even after 45 minutes, and had stable battery characteristics. It shows.

更に、本実施例1及び比較例の非水溶媒二次電池各々1
00個について、前述した放電容量維持率の特性評価試
験を、50サイクル行なった時点での電池容量分布につ
いて調べた。その結果を下記第1表に示す。なお、下記
第1表中のXは本実施例1及び比較例の非水溶媒二次電
池各々100個の電池容量の平均値であり、δは前記各
容量値から得られた標準偏差を示す。
Furthermore, 1 each of the non-aqueous solvent secondary batteries of Example 1 and Comparative Example
For 00 batteries, the battery capacity distribution was investigated after 50 cycles of the above-described discharge capacity retention rate characteristic evaluation test. The results are shown in Table 1 below. Note that X in Table 1 below is the average value of the battery capacity of 100 non-aqueous solvent secondary batteries of Example 1 and Comparative Example, and δ represents the standard deviation obtained from each of the above capacity values. .

第    1    表 上記第1表から明らかなように、本実施例1の二次電池
は比較例の二次電池に比べ電池容量にバラツキが少なく
個々の電池の性能が向上されかつ均一化されており、本
発明によって電池性能の安定化がなされていることがわ
かる。
Table 1 As is clear from Table 1 above, the secondary battery of Example 1 has less variation in battery capacity than the secondary battery of Comparative Example, and the performance of each individual battery is improved and made uniform. It can be seen that the present invention stabilizes the battery performance.

実施例2 まず、30w t%濃度のポリアクリル酸のメタノール
溶液に金属バナジウム粉末を30重置火分散させて導電
性樹脂層溶液を調製し、この溶液を長手方向に沿う一側
端にチタン箔のリード端子がスポット溶接により設けら
れたステンレス製の板状金属芯体の両面に塗布し、乾燥
して導電性樹脂層を形成した。つづいて、前記実施例1
と同様なシート状物を前記金属芯体の両面の導電性樹脂
層上に圧着し、乾燥して正極合剤を形成することにより
正極を製造した。こうした正極を用いた以外、実施例1
と同様な非水溶媒二次電池を組立てた。
Example 2 First, a conductive resin layer solution was prepared by dispersing metal vanadium powder 30 times over a methanol solution of polyacrylic acid with a concentration of 30wt%, and a titanium foil was attached to one end along the longitudinal direction of the solution. The lead terminals were applied to both sides of a plate-shaped metal core made of stainless steel provided by spot welding, and dried to form a conductive resin layer. Continuing, the above-mentioned Example 1
A positive electrode was manufactured by pressing a sheet similar to the above onto the conductive resin layers on both sides of the metal core and drying to form a positive electrode mixture. Example 1 except for using such a positive electrode
A non-aqueous solvent secondary battery similar to the above was assembled.

しかして、本実施例2の非水溶媒二次電池について実施
例1と同様な放電容量維持率、重負荷放電及び電池容量
分布を調べた。その結果は、実施例1と同様な優れた特
性を有することが確認された。
Therefore, the discharge capacity retention rate, heavy load discharge, and battery capacity distribution of the non-aqueous solvent secondary battery of Example 2 were investigated in the same manner as in Example 1. The results confirmed that it had the same excellent properties as Example 1.

なお、上記実施例ではセパレータに含浸した非水溶媒電
解液としてIMoノのLiCノ04を溶解したプロピレ
ンカーボネイトを用いたがこれに限定されない。例えば
、1,2ジメトキシエタン、エチレンカーボネイト、テ
トラヒドロフラン等の非プロトン性溶媒を、また電解質
についてはLiC,i’04を用いているが、このほか
LiA、7704、LiBF4、LiPF6゜LiAs
Fb等についても同様に用いることができる。
In the above embodiment, propylene carbonate in which IMo's LiC No. 04 was dissolved was used as the non-aqueous electrolyte with which the separator was impregnated, but the present invention is not limited thereto. For example, aprotic solvents such as 1,2 dimethoxyethane, ethylene carbonate, and tetrahydrofuran are used, and LiC, i'04 is used as the electrolyte, but in addition, LiA, 7704, LiBF4, LiPF6゜LiAs
Fb and the like can also be used in the same manner.

また、上記実施例では円筒型の非水溶媒二次電池に適応
した例について説明したがこれに限定されない。例えば
、ボタン型、扁平型、角型等の非水溶媒二次電池にも同
様に適応できる。
Further, in the above embodiment, an example was explained in which the present invention was applied to a cylindrical non-aqueous solvent secondary battery, but the present invention is not limited thereto. For example, it can be similarly applied to non-aqueous solvent secondary batteries of button type, flat type, square type, etc.

[発明の効果コ 以上詳述したように、本発明によれば金属芯体に対して
正極合剤を電気的に良好に被覆して充放電サイクル時に
おいてこれらの界面にガス等が発生するのを抑制し、ひ
いては電池容量の安定化を達成して充放電サイクル寿命
、重放電特性を向上した非水溶媒二次電池を提供するこ
とができる。
[Effects of the Invention] As detailed above, according to the present invention, the metal core is electrically well coated with the positive electrode mixture to prevent gas etc. from being generated at the interface during charging and discharging cycles. It is possible to provide a non-aqueous solvent secondary battery that suppresses this, thereby achieving stabilization of battery capacity and improving charge/discharge cycle life and heavy discharge characteristics.

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

第1図は本発明の一実施例を示す非水溶媒二次電池の断
面図、第2図(a)は第1図に示される非水溶媒二次電
池の正極の正面図、同図(b)は同図(a)のA−A線
に沿う断面図、第3図は本実施例及び比較例の非水溶媒
二次電池おける充放電サイクル数と放電容量維持率との
関係を示す特性図、第4図は本実施例及び比較例の非水
溶媒二次電池における重負荷放電時間と電池電圧との関
係を示す特性図である。 1・・・容器、3・・・発電要素、4・・・負極、5・
・・セパレータ、6・・・正極、8・・・金属芯体、9
・・・導電層、10・・・正極合剤。 出願人代理人  弁理士 鈴江武彦
FIG. 1 is a sectional view of a non-aqueous solvent secondary battery showing an embodiment of the present invention, FIG. 2(a) is a front view of the positive electrode of the non-aqueous solvent secondary battery shown in FIG. b) is a cross-sectional view taken along the line A-A in Fig. 3 (a), and Fig. 3 shows the relationship between the number of charge/discharge cycles and the discharge capacity retention rate of the non-aqueous solvent secondary batteries of the present example and comparative example. The characteristic diagram, FIG. 4, is a characteristic diagram showing the relationship between heavy load discharge time and battery voltage in the non-aqueous solvent secondary batteries of the present example and the comparative example. DESCRIPTION OF SYMBOLS 1... Container, 3... Power generation element, 4... Negative electrode, 5...
... Separator, 6... Positive electrode, 8... Metal core, 9
... Conductive layer, 10... Positive electrode mixture. Applicant's agent Patent attorney Takehiko Suzue

Claims (2)

【特許請求の範囲】[Claims] (1)金属芯体に、活物質を含む正極合剤を該活物質を
構成する金属の導電層もしくはその金属を含む導電性樹
脂層を介し被覆した構造の正極を具備したことを特徴と
する非水溶媒二次電池。
(1) A positive electrode having a structure in which a metal core is coated with a positive electrode mixture containing an active material via a conductive layer of a metal constituting the active material or a conductive resin layer containing the metal. Non-aqueous solvent secondary battery.
(2)正極合剤の活物質が、五酸化バナジウムであるこ
とを特徴とする特許請求の範囲第1項記載の非水溶媒二
次電池。
(2) The non-aqueous solvent secondary battery according to claim 1, wherein the active material of the positive electrode mixture is vanadium pentoxide.
JP62307973A 1987-12-05 1987-12-05 Nonaqueous solvent secondary battery Pending JPH01149362A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62307973A JPH01149362A (en) 1987-12-05 1987-12-05 Nonaqueous solvent secondary battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62307973A JPH01149362A (en) 1987-12-05 1987-12-05 Nonaqueous solvent secondary battery

Publications (1)

Publication Number Publication Date
JPH01149362A true JPH01149362A (en) 1989-06-12

Family

ID=17975385

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62307973A Pending JPH01149362A (en) 1987-12-05 1987-12-05 Nonaqueous solvent secondary battery

Country Status (1)

Country Link
JP (1) JPH01149362A (en)

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