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JPH077669B2 - Method for manufacturing non-aqueous electrolyte battery - Google Patents
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JPH077669B2 - Method for manufacturing non-aqueous electrolyte battery - Google Patents

Method for manufacturing non-aqueous electrolyte battery

Info

Publication number
JPH077669B2
JPH077669B2 JP59141032A JP14103284A JPH077669B2 JP H077669 B2 JPH077669 B2 JP H077669B2 JP 59141032 A JP59141032 A JP 59141032A JP 14103284 A JP14103284 A JP 14103284A JP H077669 B2 JPH077669 B2 JP H077669B2
Authority
JP
Japan
Prior art keywords
positive electrode
particles
aqueous electrolyte
electrolyte battery
water
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
Application number
JP59141032A
Other languages
Japanese (ja)
Other versions
JPS6119067A (en
Inventor
二康 岩丸
徹夫 川合
拓 笹間
富夫 北村
慶雄 植谷
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.)
Maxell Ltd
Original Assignee
Hitachi Maxell Energy 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 Hitachi Maxell Energy Ltd filed Critical Hitachi Maxell Energy Ltd
Priority to JP59141032A priority Critical patent/JPH077669B2/en
Publication of JPS6119067A publication Critical patent/JPS6119067A/en
Publication of JPH077669B2 publication Critical patent/JPH077669B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/663Selection of materials containing carbon or carbonaceous materials as conductive part, e.g. graphite, carbon fibres
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/14Cells with non-aqueous electrolyte
    • 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)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Primary Cells (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Cell Electrode Carriers And Collectors (AREA)

Description

【発明の詳細な説明】 〔技術分野〕 この発明はオキシハロゲン化物を電解液の溶媒および正
極活物質とし、リチウム金属などのアルカリ金属を負極
活物質とした非水電解質電池に関する。
Description: TECHNICAL FIELD The present invention relates to a non-aqueous electrolyte battery in which an oxyhalide is used as a solvent of an electrolytic solution and a positive electrode active material, and an alkali metal such as lithium metal is used as a negative electrode active material.

〔背景技術〕[Background technology]

この種の電池では、たとえば第1図に示されるように、
ステンレス鋼などの負極缶にリチウム金属の如きアルカ
リ金属の板状物からなる負極を密着させ、かつこの負極
にガラス繊維製のセパレータを介して対向させた炭素質
成形正極とその他の電池要素を内填させる一方、正極活
物質を兼ねる塩化チオニルや塩化スルフリルなどのオキ
シハロゲン化物にリチウムアルミニウムクロリドの如き
電解質を溶解させた電解液を注入し、ついで缶開口部に
金属蓋を溶接するハーメチツクシールにより電池内部を
密閉構造としている。
In this type of battery, for example, as shown in FIG.
A carbonaceous molded positive electrode and other battery elements that are made by closely adhering a negative electrode made of a plate of an alkali metal such as lithium metal to a negative electrode can such as stainless steel and facing the negative electrode with a glass fiber separator inside A hermetic seal in which an electrolyte solution in which an electrolyte such as lithium aluminum chloride is dissolved in an oxyhalide such as thionyl chloride or sulfuryl chloride that also serves as a positive electrode active material is injected, and then a metal lid is welded to the can opening. The inside of the battery has a sealed structure.

上記の炭素質成形正極は、アセチレンブラツクや黒鉛の
如き炭素材料とポリテトラフルオロエチレンの如き樹脂
バンイダとからなり、一般に約70容量%以上の空隙を有
するものであつて、この空隙内に前記電解液を含浸させ
て放電反応を行わせるものである。この放電反応は正極
活物質としてのオキシハロゲン化物とリチウムイオンの
如き負極イオンとの反応であり、塩化リチウムなどの電
解液不溶性の反応物を生成する。
The above-mentioned carbonaceous molded positive electrode is made of a carbon material such as acetylene black or graphite and a resin vanida such as polytetrafluoroethylene, and generally has a void of about 70% by volume or more, and the electrolysis is performed in the void. A liquid is impregnated to cause a discharge reaction. This discharge reaction is a reaction between an oxyhalide as a positive electrode active material and a negative electrode ion such as lithium ion, and produces a reaction product insoluble in an electrolytic solution such as lithium chloride.

したがつて、上記正極としては、電解液を充分に含浸保
持できるとともに上記反応生成物が容易に蓄積されて放
電反応がスムースに進行しうるような空隙を有するもの
であることが望まれる。ところが、従来のこの種成形正
極は上記要求特性を必ずしも満足するものとはいえなか
つた。
Therefore, it is desired that the positive electrode has a void that can sufficiently impregnate and hold the electrolytic solution and that the reaction product can be easily accumulated and the discharge reaction can smoothly proceed. However, it cannot be said that the conventional molded positive electrode of this type always satisfies the above-mentioned required characteristics.

すなわち、従来のこの種成形正極は、前述の如き炭素材
料と樹脂バインダとをアルコールを含む水と混練してこ
れを適宜の手段で所定の粒度に造粒したのち乾燥し、こ
の乾燥造粒物を所定量秤量して金型中で圧縮成形すると
いう方法でつくられていた。第3図は、上記従来の正極
の断面を顕微鏡で観察した結果を模擬的に示したもので
ある。
That is, a conventional molded positive electrode of the related art is obtained by kneading the carbon material and the resin binder as described above with water containing alcohol, granulating the same by a suitable means to a predetermined particle size, and then drying the dried granulated product. Was weighed in a predetermined amount and compression-molded in a mold. FIG. 3 schematically shows a result of observing a cross section of the conventional positive electrode with a microscope.

この図から明らかなように、この種の正極は、各造粒物
30,30,…内に、使用した炭素材料粒子と樹脂バインダ粒
子との粒子間に形成された一般に小さ目の空隙40,40,…
を有するとともに、各造粒物30,30,…の間に上記空隙40
よりも大き目でかつ不均一な空隙50,50,…が存在し、こ
の両空隙40,50によつて所定の空隙率を有する構成とな
つている。
As is clear from this figure, this type of positive electrode is
Generally, small voids 40, 40, ... Formed between the particles of the carbon material particles and the resin binder particles used,
And has the above-mentioned voids 40 between the granules 30, 30 ,.
.. are present, which are larger and more non-uniform, and the two voids 40, 50 have a predetermined porosity.

ここで、上記空隙40内には放電反応の生成物が容易に蓄
積される。これは空隙40のごく近傍に炭素材料があるた
め放電反応がスムースに進行するからである。一方、上
記空隙50はそのごく近傍に炭素材料がないためにこれに
電解液が充分に含浸保持されていても放電反応の場所と
してはほとんど関与せず、したがつて反応生成物の蓄積
の場としてあまり寄与しない。
Here, the products of the discharge reaction are easily accumulated in the voids 40. This is because the discharge reaction proceeds smoothly because the carbon material is present in the vicinity of the void 40. On the other hand, since the void 50 does not have a carbon material in its immediate vicinity, it hardly participates in the place of the discharge reaction even if the electrolytic solution is sufficiently impregnated and held in the void 50. Does not contribute as much.

つまり、従来の成形正極は、放電反応の生成物が容易に
蓄積されうる小さな空隙部分と上記生成物が蓄積されに
くい大きな空隙部分とを有し、しかも上記蓄積されにく
い大きな空隙部分である前記空隙50の大きさ,形状は必
ずしも一定しない。このため、放電反応が全体としてス
ムースに進行せず、結果として放電電圧の低下や安定し
た放電電圧が得られないという問題が生じてくる。
That is, the conventional molded positive electrode has a small void portion in which the product of the discharge reaction can be easily accumulated and a large void portion in which the product is hard to be accumulated, and the large void portion is hard to be accumulated. The size and shape of 50 are not always constant. For this reason, the discharge reaction does not proceed smoothly as a whole, and as a result, there arises a problem that the discharge voltage decreases and a stable discharge voltage cannot be obtained.

〔発明の目的〕[Object of the Invention]

この発明は、上記従来の問題を解消した高くてかつ安定
した放電電圧を得ることができる非水電解質電池を提供
することを目的としている。
An object of the present invention is to provide a non-aqueous electrolyte battery which can solve the above-mentioned conventional problems and can obtain a high and stable discharge voltage.

〔発明の概要〕[Outline of Invention]

この発明者らは、炭素質正極の成形に際して前述した如
く炭素材料と樹脂バインダとを造粒してこれを圧縮成形
する方法を採用したときには、造粒物内と造粒物間の空
隙の大きさに差異が生じてくるのはどうしてもさけられ
ないことから、かかる造粒方式によらないで空隙率が70
容量%以上という非常に多孔質の成形正極を得る方法に
つき検討した。
When the method of granulating the carbon material and the resin binder and compressing and molding the carbon material and the resin binder as described above when molding the carbonaceous positive electrode, the present inventors have found that the size of the voids in the granulated material and between the granulated material is large. Since it is unavoidable that there is a difference in size, porosity is 70% without using this granulation method.
A method for obtaining a highly porous molded positive electrode having a volume percentage of more than 100% was examined.

その結果、炭素材料と樹脂バインダとを含む含水混練物
を押出成形によつて適宜の形状に成形しこの成形後水そ
の他の揮発分を乾燥除去したときには、高空隙率でしか
も成形体全体に亘つて空隙のほぼ一定した多孔質の成形
正極が得られ、この正極を用いた非水電解質電池は放電
電圧が高くてかつ安定したものとなることを知り、この
発明を完成するに至つた。
As a result, when a water-containing kneaded material containing a carbon material and a resin binder is molded into an appropriate shape by extrusion molding and water and other volatile components are dried and removed after the molding, the molded body has a high porosity and is spread over the entire molded body. Then, a porous molded positive electrode having substantially constant voids was obtained, and it was found that a non-aqueous electrolyte battery using this positive electrode has a high discharge voltage and is stable, and thus completed the present invention.

すなわち、この発明においては、炭素粒子と樹脂バイン
ダ粒子と低沸点の水溶性有機溶剤を含む含水混練物を押
出成形したのち、上記溶剤および水からなる低沸点揮発
分を加熱乾燥して除去することにより、炭素質成形正極
を製造するとともに、この方法で製造される炭素質成形
正極が、炭素粒子と樹脂バインダ粒子とから構成された
粒子間の空隙の大きさが0.1mm以下の範囲でかつ正極全
体で実質的に均一である非造粒の粒子結合体からなり、
かつこの正極の空隙率が70〜90容量%であることを特徴
とするものであり、このように高空隙率でしかも粒子間
の空隙の大きさが一定であるような成形正極は従来全く
知られていなかつた非水電解質電池の正極として新規で
かつきわめて有用な構成にされたものである。
That is, in this invention, after extruding a water-containing kneaded product containing carbon particles, resin binder particles and a low boiling point water-soluble organic solvent, the low boiling point volatile matter consisting of the solvent and water is dried by heating to be removed. According to the method for producing a carbonaceous molded positive electrode, the carbonaceous molded positive electrode produced by this method, the size of the voids between particles composed of carbon particles and resin binder particles is 0.1 mm or less and the positive electrode Consisting of non-granulated particle binders that are substantially uniform throughout
Moreover, this positive electrode is characterized by having a porosity of 70 to 90% by volume. Thus, a molded positive electrode having such a high porosity and a constant size of voids among particles has never been known. It has a novel and extremely useful constitution as a positive electrode of a non-aqueous electrolyte battery which has never been used.

以下、この発明を図面を参考にして詳しく説明する。Hereinafter, the present invention will be described in detail with reference to the drawings.

第1図において、1は負極端子を兼ねるステンレス鋼の
深しぼり加工缶の如き負極缶、2はリチウム金属板など
のアルカリ金属の板状物からなる負極、3はガラス繊維
不織布の如きセパレータ、4は上記負極2に対して上記
セパレータ3を介して対向させた炭素質成形正極、5は
ステンレス鋼製などの正極集電体、6はステンレス鋼な
どよりなる金属蓋で、この金属蓋6の外周側は負極缶1
の開口部内周面と溶接され、また金属蓋6の内周側には
ガラスシール7が形成されこのシール7にあらかじめ溶
着されてなる金属パイプ8から電解液9を注入したの
ち、正極集電体5と金属パイプ8とを溶接して電池内部
が密閉構造とされている。
In FIG. 1, 1 is a negative electrode can such as a stainless steel deep-drawing can also serving as a negative electrode terminal, 2 is a negative electrode made of an alkali metal plate such as a lithium metal plate, 3 is a separator such as glass fiber nonwoven fabric, 4 Is a carbonaceous molded positive electrode facing the negative electrode 2 with the separator 3 interposed therebetween, 5 is a positive electrode current collector made of stainless steel or the like, 6 is a metal lid made of stainless steel or the like, and the outer periphery of the metal lid 6 is Side is negative electrode can 1
After the glass seal 7 is welded to the inner peripheral surface of the opening of the metal lid 6 and the glass seal 7 is formed on the inner peripheral side of the metal lid 6, the electrolytic solution 9 is injected from the metal pipe 8 previously welded to the seal 7, and then the positive electrode current collector. 5 and the metal pipe 8 are welded together to form a sealed structure inside the battery.

上記電解液9はリチウムアルミニウムクロリドなどの電
解質を塩化チオニル(SOCl2)や塩化スルフリル(SO2C
l)の如きオキシハロゲン化物に溶解させてなるもので
あり、上記オキシハロゲン化物は電解液の溶媒の役割と
ともに正極活物質としての作用を果たすものである。
The electrolytic solution 9 contains an electrolyte such as lithium aluminum chloride and thionyl chloride (SOCl 2 ) or sulfuryl chloride (SO 2 C).
The compound is dissolved in an oxyhalide such as l), and the oxyhalide functions as a positive electrode active material together with the role of the solvent of the electrolytic solution.

この構成において、上記炭素質成形正極4は、その断面
を顕微鏡で観察した結果を模擬的に示した第2図のとお
り、炭素粒子と樹脂バインダ粒子とから構成された粒子
間の空隙41,41,…の大きさが正極全体で実質的に均一で
ある非造粒の粒子結合体からなり、その空隙率が70〜90
容量%、特に好適には80〜90容量%に設定されている。
つまり、この正極4は前記第3図の如き造粒物30を有さ
ず、したがつて造粒物間の空隙50を持たないことを特徴
としている。なお、上記実質的とは粒子自体の大きさの
相違などにより粒子間の空隙の大きさが必ずしもすべて
同一であるとはいえないが、造粒物を有しないため従来
構成の如き粒子間の空隙に大きな差異がなく全体的にほ
ぼ同一であることを意味する。
In this configuration, the carbonaceous molded positive electrode 4 has voids 41, 41 between particles composed of carbon particles and resin binder particles, as shown in FIG. The size of ,, ... is substantially uniform throughout the positive electrode and is composed of a non-granulated particle-bonded body having a porosity of 70-90.
The volume% is set, particularly preferably 80 to 90% by volume.
That is, this positive electrode 4 is characterized by not having the granules 30 as shown in FIG. 3, and thus not having the voids 50 between the granules. The size of voids between particles is not necessarily the same due to the difference in size of the particles themselves from the above-mentioned substantially, but since there is no granulated substance, voids between particles as in the conventional structure. It means that there is no big difference in the above and that they are almost the same as a whole.

上記粒子間の空隙41の大きさは通常0.1mm以下であり、
従来の第3図の構成が一般に0.3mm〜1.0mmの空隙を有
し、特に0.8mm以上の空隙を多数有しているのとは本質
的に相違する。かかる空隙41を形成している上記正極4
の構成材の1つである炭素粒子は、通常表面積が大きく
て放電反応に有効なアセチレンブラツクの如きカーボン
ブラツク70〜100重量%と正極4の機械的強度の向上に
寄与する黒鉛30〜0重量%とからなり、上記カーボンブ
ラツクの平均粒子径は40〜70mμ、上記黒鉛の平均粒子
径は10〜30μm程度である。また正極4の構成材の他の
1つである樹脂バインダ粒子は、オキシハロゲン化物に
対して安定で放電反応に悪影響を与えないものとしてポ
リテトラフルオロエチレン粉末の如きフツ素樹脂粉末が
好ましく用いられ、この粉末の平均粒子径は0.1〜1.0μ
m程度で、使用量は上記炭素粒子100重量部に対して5
〜15重量部程度である。
The size of the voids 41 between the particles is usually 0.1 mm or less,
This is fundamentally different from the conventional configuration shown in FIG. 3 in which there are generally 0.3 mm to 1.0 mm of voids, and in particular, there are many voids of 0.8 mm or more. The positive electrode 4 forming the void 41.
The carbon particles, which are one of the constituent materials, are usually 70 to 100% by weight of carbon black such as acetylene black, which has a large surface area and is effective for discharge reaction, and 30 to 0% by weight of graphite, which contributes to the improvement of the mechanical strength of the positive electrode 4. %, The average particle size of the carbon black is 40 to 70 mμ, and the average particle size of the graphite is about 10 to 30 μm. As the resin binder particles, which is another constituent material of the positive electrode 4, fluorine resin powder such as polytetrafluoroethylene powder is preferably used because it is stable to oxyhalides and does not adversely affect the discharge reaction. , The average particle size of this powder is 0.1 ~ 1.0μ
m, the amount used is 5 with respect to 100 parts by weight of the carbon particles
It is about 15 parts by weight.

このような構成からなる炭素質成形正極4は、押出成形
法によつて容易に製造される。すなわち、上記構成およ
び使用割合からなる炭素粒子と樹脂バインダ粒子とをメ
チルアルコールやエチルアルコールなどの低級アルコー
ルの如きカーボンブラツクの濡れ性を良くするための低
沸点の水溶性有機溶剤を含ませた水と混練し、この混練
物をそのまま押出成形機に供して正極4の寸法(径)に
柱状に押出成形し、この成形後所定の大きさ(高さ)に
切断したのち加熱乾燥、必要なら真空下での加熱乾燥を
行つて上記溶剤および水からなる低沸点揮発分を除去す
ることにより前記高空隙率の成形正極4を得ることがで
きる。
The carbonaceous molded positive electrode 4 having such a structure is easily manufactured by an extrusion molding method. That is, water containing a water-soluble organic solvent having a low boiling point for improving the wettability of carbon black such as lower alcohols such as methyl alcohol and ethyl alcohol, the carbon particles and the resin binder particles having the above-mentioned constitution and use ratio. Then, the kneaded product is directly subjected to an extrusion molding machine to be extruded into a column of the size (diameter) of the positive electrode 4 and then cut into a predetermined size (height), followed by heating and drying, if necessary vacuum. The molded positive electrode 4 having a high porosity can be obtained by heating and drying below to remove the low boiling point volatile matter composed of the solvent and water.

上記押出成形にあたつては、この成形中に混練物に含ま
れる揮発分が分離せず、また空気などの巻き込みを抑え
て成形に供する前の混練物の性状を可及的に維持した状
態で成形することが肝要である。すなわち、かかる成形
を行つたのちに加熱乾燥して揮発分を除去することによ
つてはじめて前記空隙率を有しかつ空隙の大きさが均一
でしかも小さい成形正極4の製造が可能となる。
In the extrusion molding, the volatile components contained in the kneaded product during the molding are not separated, and the state of the kneaded product before being subjected to the molding is suppressed by suppressing the entrainment of air etc. It is important to mold with. That is, it is possible to manufacture the molded positive electrode 4 having the above-mentioned void ratio and having a uniform size of voids only by heating and drying to remove the volatile matter after performing such shaping.

押出成形機としては、油圧式のものが好ましく用いられ
るが、スクリユータイプのものも使用可能である。押出
圧としては1〜6kg/cm2とするのがよく、1kg/cm2より小
さいと押出しが困難で、一方6kg/cm2より大きくなると
押出口で有機溶剤と水とからなる揮発分が圧出分離し、
空隙率が小さくなるため、いずれも不適当である。ま
た、スクリユー押出成形機にあつては、押出ノズルやス
クリユーの形状さらにスクリユーの回転数を適宜設定し
て空気の巻き込みや揮発分の分離をなくすように配慮す
るのが望ましい。
As the extruder, a hydraulic type is preferably used, but a screw type can also be used. The extrusion pressure well to the 1~6kg / cm 2, 1kg / cm 2 less than the extrusion difficult, whereas volatiles consisting becomes greater than 6 kg / cm 2 with an organic solvent and water in an extrusion opening pressure Out,
Both are unsuitable because the porosity becomes small. In addition, in the screw extruder, it is desirable that the shapes of the extrusion nozzle and the screw and the rotation speed of the screw are appropriately set so that entrapment of air and separation of volatile components are eliminated.

前記有機溶剤と水とからなる揮発分の使用量は、空隙率
と空隙の大きさを決定する重要な因子となるから、適正
な範囲に設定される必要がある。一般には、炭素粒子と
樹脂バインダ粒子との合計量100重量部に対して110〜20
0重量部とするのがよい。また、揮発分中の有機溶剤の
割合は30〜80重量%程度であるのがよい。なお、樹脂バ
インダ粒子としてポリテトラフルオロエチレン粉末の如
き水分散体を用いるときは、これに含まれる水分を揮発
分の一種として、揮発分の合計量が上記範囲となるよう
に設定すればよい。揮発分が多すぎると一般に粒子間の
空隙の大きさが大きくなり、また少なすぎると成形体の
機械的強度が損なわれる。
The amount of the volatile component composed of the organic solvent and water is an important factor that determines the porosity and the size of the void, and thus needs to be set in an appropriate range. Generally, 110 to 20 per 100 parts by weight of the total amount of carbon particles and resin binder particles is used.
It is recommended to use 0 part by weight. The proportion of organic solvent in the volatile matter is preferably about 30 to 80% by weight. When a water dispersion such as polytetrafluoroethylene powder is used as the resin binder particles, the water contained therein may be used as one kind of volatile matter, and the total amount of volatile matter may be set within the above range. If the volatile content is too large, the size of the voids between the particles generally becomes large, and if it is too small, the mechanical strength of the molded product is impaired.

なお、第1図中、10は前記セパレータ3と同質の材料で
構成されて負極缶1の底面と正極4とを隔離するための
底紙、11は前記セパレータ3と同質の材料で構成されて
正極4の上面に載置された上紙である。
In FIG. 1, reference numeral 10 denotes a bottom paper made of the same material as the separator 3 for separating the bottom surface of the negative electrode can 1 from the positive electrode 4, and 11 a material made of the same material as the separator 3. The top paper is placed on the upper surface of the positive electrode 4.

〔発明の効果〕〔The invention's effect〕

上記説明にて明らかなように、この発明の非水電解質電
池は、押出成形法にて製造される粒子間の空隙が正極全
体で実質的に均一である高空隙率の炭素質成形正極を用
いているから、この正極中で放電反応をスムースに進行
させることができ、またその反応生成物を上記空隙に容
易に蓄積することができる。したがつて、従来に比し高
くてかつ安定した放電電圧が得られる非水電解質電池を
提供することができる。
As is clear from the above description, the non-aqueous electrolyte battery of the present invention uses a high porosity carbonaceous molded positive electrode in which the voids between particles produced by an extrusion molding method are substantially uniform throughout the positive electrode. Therefore, the discharge reaction can proceed smoothly in the positive electrode, and the reaction product can be easily accumulated in the void. Therefore, it is possible to provide a non-aqueous electrolyte battery which is higher than the conventional one and can obtain a stable discharge voltage.

〔実施例〕〔Example〕

以下に、この発明の実施例を記載してより具体的に説明
する。
Hereinafter, examples of the present invention will be described to more specifically describe.

アセチレンブラツク(平均粒子径約50mμ)90重量%と
黒鉛(平均粒子径約15μm)10重量%とをあらかじめよ
く乾式混合した。この混合物100重量部に対し、ポリテ
トラフルオロエチレンの水分散体(固型分60重量%)20
重量部、メチルアルコール120重量部および水40重量部
を加えて混練した。この混練物を油圧式の押出成形機
(押出し圧4kg/cm2)にて直径10mmの柱状に押出成形
し、その後高さ30mmの大きさに切断したのち130℃で真
空乾燥することにより、空隙率88容量%の炭素質成形正
極を得た。この正極の断面を倍率20倍の顕微鏡で観察し
た結果を模擬的に示したのが前記第2図であり、粒子間
の空隙の大きさは0.1mm以下であつた。なお、ポリテト
ラフルオロエチレンの粒子は上述の混練工程で直径約0.
1μmの繊維状になるので図中には認められない。
90% by weight of acetylene black (average particle size: about 50 mμ) and 10% by weight of graphite (average particle size: about 15 μm) were well dry-mixed in advance. To 100 parts by weight of this mixture, an aqueous dispersion of polytetrafluoroethylene (solid content 60% by weight) 20
By weight, 120 parts by weight of methyl alcohol and 40 parts by weight of water were added and kneaded. This kneaded product was extruded into a column with a diameter of 10 mm by a hydraulic extrusion molding machine (extrusion pressure 4 kg / cm 2 ), then cut into a size of 30 mm in height, and then vacuum dried at 130 ° C. A carbonaceous molded positive electrode having a rate of 88% by volume was obtained. The results of observing the cross section of this positive electrode with a microscope at a magnification of 20 times are shown in FIG. 2 in a simulated manner, and the size of the voids between the particles was 0.1 mm or less. The particles of polytetrafluoroethylene had a diameter of about 0.
It cannot be seen in the figure because it becomes 1 μm fibrous.

上記の炭素質成形正極を用いて以下の要領でこの発明に
係る非水電解質電池を得た。すなわち、SUS304製の缶径
14mm,高さ47mmの負極缶の内面に厚さ0.8mm,幅37mm,高さ
37mmのリチウム金属板を密着させ、その内側にガラス繊
維不織布をセパレータとして挿入し、さらにその内側に
前記の炭素質成形正極を挿入した。つぎに、内周側にガ
ラスシールを介して金属パイプを溶接した金属蓋を前記
負極缶の開口部に圧入してこの圧入部を溶接する一方、
金属パイプからリチウムアルミニウムクロリドを溶解し
た塩化チオニルを注入したのち、注入口を溶接により封
口して、第1図に示されるようなこの発明の非水電解質
電池を作製した。
A non-aqueous electrolyte battery according to the present invention was obtained using the above-mentioned carbonaceous molded positive electrode in the following manner. That is, can diameter made of SUS304
0.8mm thick, 37mm wide, high on the inner surface of a 14mm, 47mm high negative electrode can
A 37 mm lithium metal plate was brought into close contact, a glass fiber nonwoven fabric was inserted as a separator inside the plate, and the carbonaceous molded positive electrode was inserted inside the separator. Next, while the metal lid welded metal pipe through the glass seal on the inner peripheral side is press-fitted into the opening of the negative electrode can to weld the press-fitted portion,
After injecting thionyl chloride in which lithium aluminum chloride was dissolved from a metal pipe, the injection port was sealed by welding to prepare a non-aqueous electrolyte battery of the present invention as shown in FIG.

この電池につき、10mAの電流で放電したときの閉路電圧
と放電時間との関係を調べたところ、第4図の曲線−A
にて示されるとおりであつた。なお、第4図中の曲線−
Bは下記の方法で成形した従来の炭素質成形正極を用い
た以外は上記実施例と同様にして作製した電池の結果で
ある。
When the relationship between the closed circuit voltage and the discharge time when the battery was discharged at a current of 10 mA was examined, the curve -A in FIG.
It was as shown in. The curve in FIG.
B is the result of the battery manufactured in the same manner as in the above-mentioned example except that the conventional carbonaceous molded positive electrode molded by the following method was used.

上記従来の炭素質成形正極は、まず実施例と同じアセチ
レンブラツク90重量%と黒鉛10重量%とからなる混合物
100重量部に対してポリテトラフルオロエチレンの水分
散体(固型分60重量%)20重量部、メチルアルコール60
重量部および水20重量部を加えて混練し、これを造粒機
で直径約0.8mmの粒状物とした。この粒状物を真空乾燥
したのちその所定量を金型に入れて圧縮成形することに
より、直径10mmの成形体とした。この成形体を前記要領
で負極缶内に挿入しこの缶内で押圧して空隙率85容量%
の成形正極とした。なお、この正極の断面を倍率10倍の
顕微鏡で観察した結果を模擬的に示したのが前記第3図
であり、この正極の粒子間の空隙の大きさは0.3〜1.0mm
と大きくかつばらついていた。
The above-mentioned conventional carbonaceous molded positive electrode is a mixture of 90% by weight of acetylene black and 10% by weight of graphite, which is the same as the example.
20 parts by weight of an aqueous dispersion of polytetrafluoroethylene (solid content 60% by weight), 60 parts by weight of methyl alcohol to 100 parts by weight
Parts by weight and 20 parts by weight of water were added and kneaded, and this was made into granules having a diameter of about 0.8 mm by a granulator. After vacuum-drying the granular material, a predetermined amount of the granular material was put into a mold and compression-molded to obtain a molded body having a diameter of 10 mm. This molded product was inserted into the negative electrode can in the same manner as described above, and pressed in this can to obtain a porosity of 85% by volume.
Of the molded positive electrode. The result of observing the cross section of the positive electrode with a microscope having a magnification of 10 is shown in FIG. 3, and the size of the voids between the particles of the positive electrode is 0.3 to 1.0 mm.
It was big and scattered.

上記第4図の結果からも明らかなように、この発明の実
施例の電池は、従来構成の電池に比し閉路電圧が2.1mV
も高く、また放電中期での電圧の降下が全く認められな
い安定した放電特性を有するものであることが判る。
As is clear from the results shown in FIG. 4, the battery of the embodiment of the present invention has a closed circuit voltage of 2.1 mV as compared with the battery of the conventional configuration.
It is understood that the battery has a stable discharge characteristic in which the voltage drop is not observed at all in the middle of discharge.

【図面の簡単な説明】[Brief description of drawings]

第1図はこの発明の非水電解質電池の一例を示す半截断
面図、第2図は上記電池に用いた炭素質成形正極の断面
を顕微鏡で観察した結果を模擬的に示す図、第3図は同
従来の炭素質成形正極を示す図、第4図はこの発明の非
水電解質電池を従来の非水電解質電池と対比して示す放
電特性図である。 2…負極、3…セパレータ、4…炭素質成形正極、41…
空隙、9…電解液
FIG. 1 is a half cross-sectional view showing an example of the non-aqueous electrolyte battery of the present invention, and FIG. 2 is a diagram schematically showing a result of observing a cross-section of a carbonaceous molded positive electrode used in the battery with a microscope, FIG. Shows a conventional carbonaceous molded positive electrode, and FIG. 4 is a discharge characteristic diagram showing the non-aqueous electrolyte battery of the present invention in comparison with a conventional non-aqueous electrolyte battery. 2 ... Negative electrode, 3 ... Separator, 4 ... Carbonaceous molded positive electrode, 41 ...
Void, 9 ... Electrolyte

───────────────────────────────────────────────────── フロントページの続き (72)発明者 北村 富夫 大阪府茨木市丑寅1丁目1番88号 日立マ クセル株式会社内 (72)発明者 植谷 慶雄 大阪府茨木市丑寅1丁目1番88号 日立マ クセル株式会社内 (56)参考文献 特開 昭59−128772(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Tomio Kitamura 1-188, Tora, Ibaraki-shi, Osaka Prefecture Hitachi Maxel Co., Ltd. (72) Inventor Yoshio Uetani 1-1-88, Tora, Ibaraki-shi, Osaka Hitachi Maxel Co., Ltd. (56) Reference JP-A-59-128772 (JP, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】オキシハロゲン化物を電解液の溶媒および
正極活物質とし、アルカリ金属からなる負極に対してセ
パレータを介して対向させた電解液が含浸保持される空
隙を有する炭素質成形正極を備えてなる非水電解質電池
において、上記の炭素質成形正極を、炭素粒子と樹脂バ
インダ粒子と低沸点の水溶性有機溶剤を含む含水混練物
を押出成形したのち、上記溶剤および水からなる低沸点
揮発分を加熱乾燥して除去することにより、製造すると
ともに、この方法で製造される上記の炭素質成形正極
が、炭素粒子と樹脂バインダ粒子とから構成された粒子
間の空隙の大きさが0.1mm以下の範囲でかつ正極全体で
実質的に均一である非造粒の粒子結合体からなり、かつ
この正極の空隙率が70〜90容量%であることを特徴とす
る非水電解質電池の製造方法。
1. A carbonaceous molded positive electrode comprising an oxyhalide as a solvent of an electrolytic solution and a positive electrode active material, and having a void which is impregnated with and holds an electrolytic solution which is opposed to a negative electrode made of an alkali metal via a separator. In a non-aqueous electrolyte battery consisting of, the above-mentioned carbonaceous molded positive electrode is extruded with a water-containing kneaded product containing carbon particles, resin binder particles and a low boiling point water-soluble organic solvent, and then low boiling point volatilization consisting of the solvent and water is carried out. By removing by heating and drying minutes, the carbonaceous molded positive electrode produced by this method, the size of the voids between the particles composed of carbon particles and resin binder particles is 0.1 mm. Manufacture of a non-aqueous electrolyte battery comprising a non-granulated particle binder in the following range and being substantially uniform throughout the positive electrode, and having a porosity of 70 to 90% by volume of the positive electrode. Law.
JP59141032A 1984-07-06 1984-07-06 Method for manufacturing non-aqueous electrolyte battery Expired - Lifetime JPH077669B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59141032A JPH077669B2 (en) 1984-07-06 1984-07-06 Method for manufacturing non-aqueous electrolyte battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59141032A JPH077669B2 (en) 1984-07-06 1984-07-06 Method for manufacturing non-aqueous electrolyte battery

Publications (2)

Publication Number Publication Date
JPS6119067A JPS6119067A (en) 1986-01-27
JPH077669B2 true JPH077669B2 (en) 1995-01-30

Family

ID=15282630

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59141032A Expired - Lifetime JPH077669B2 (en) 1984-07-06 1984-07-06 Method for manufacturing non-aqueous electrolyte battery

Country Status (1)

Country Link
JP (1) JPH077669B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013051091A (en) * 2011-08-30 2013-03-14 Honda Motor Co Ltd Metal oxygen battery

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59128772A (en) * 1983-01-14 1984-07-24 Toshiba Corp Nonaqueous solvent battery

Also Published As

Publication number Publication date
JPS6119067A (en) 1986-01-27

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