JPH0620672A - Separator for nonaqueous battery - Google Patents

Separator for nonaqueous battery

Info

Publication number
JPH0620672A
JPH0620672A JP4173214A JP17321492A JPH0620672A JP H0620672 A JPH0620672 A JP H0620672A JP 4173214 A JP4173214 A JP 4173214A JP 17321492 A JP17321492 A JP 17321492A JP H0620672 A JPH0620672 A JP H0620672A
Authority
JP
Japan
Prior art keywords
separator
electrolytic solution
impregnation
battery
examples
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.)
Withdrawn
Application number
JP4173214A
Other languages
Japanese (ja)
Inventor
Akira Ono
晃 小野
Akira Yoshino
吉野  彰
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.)
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry 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 Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP4173214A priority Critical patent/JPH0620672A/en
Publication of JPH0620672A publication Critical patent/JPH0620672A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • 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

Abstract

PURPOSE:To make the impregnating property to separator of electrolyte excellent and enhance impregnating speed by using a polyolefin fine porous film treated with a specified phosphor compound in a separator. CONSTITUTION:A polyolefin fine porous film of polyethylene or polypropylene is treated with at least one kind of phosphor compounds selected from the group shown by the formulae I, II, III, for example, tributhylphosphate, to form a separator for nonaqueous battery. In the formulae, R1-R6 and R8, R9 represent C4-C30 alkyl, aryl, allyl, aralkyl or halogenated alkyl groups, and R7 represents a C1-C30 alkyl, aryl, allyl, aralkyl or halogenated alkyl group.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、非水電池用セパレータ
ーに関する。
FIELD OF THE INVENTION The present invention relates to a separator for non-aqueous batteries.

【0002】[0002]

【従来の技術】近年、一次電池、二次電池は小型、高容
量化が望まれており、正、負活物質、電解液、電池構造
等あらゆる角度から小型、高容量化の試みがなされてい
る。かかる小型、高容量化を実現する上でセパレーター
の選択は極めて重要である。即ち、電池体積に占めるセ
パレーターの体積は、当然のことながら用いるセパレー
ターの厚みに比例する。従来よりセパレーターとして
は、紙、織布、不織布、ガラスマット等が用いられてき
たが、これらは強度上の問題、短絡防止、性能上の問題
等から、どうしても一定の厚さ以上が必要であった。
2. Description of the Related Art In recent years, it has been desired to reduce the size and capacity of primary batteries and secondary batteries. Attempts have been made to reduce the size and capacity of positive and negative active materials, electrolytic solutions, battery structures, etc. There is. Selection of the separator is extremely important for realizing such a small size and high capacity. That is, the volume of the separator in the battery volume is naturally proportional to the thickness of the separator used. Conventionally, paper, woven cloth, non-woven cloth, glass mat, etc. have been used as separators, but these must have a certain thickness or more due to problems with strength, short circuit prevention, performance problems, etc. It was

【0003】一方、かかる欠点を改善するものとして、
セパレーターにポリエチレン、ポリプロピレン等の薄く
て均一な微多孔膜を用いることが主流となりつつある。
しかしながら、微多孔膜を用いる上で大きな問題があっ
た。それは電解液の含浸性が悪いという点であり、製造
工程上、極めて含浸工程が複雑になること、また、含浸
不良等で電池性能のバラツキ等の問題が発生する。
On the other hand, in order to improve such a defect,
It is becoming mainstream to use thin and uniform microporous membranes such as polyethylene and polypropylene for the separator.
However, there is a big problem in using the microporous membrane. This is because the impregnation property of the electrolytic solution is poor, and the impregnation process is extremely complicated in the manufacturing process, and problems such as variations in battery performance occur due to impregnation defects and the like.

【0004】特に近年、高電圧に耐えることで用いられ
ようとしているプロピレンカーボネート等の環状炭酸エ
ステル、γ−ブチロラクトン等の環状エステル等の溶剤
を用いた場合に、その影響は特に大きかった。これま
で、かかる欠点を解決せんと界面活性剤の添加等の方策
が提案されてきたが、電池性能に与える悪影響が著しく
用いるわけにはいかなかった。
Particularly, in recent years, when a solvent such as a cyclic ester carbonate such as propylene carbonate or a cyclic ester such as γ-butyrolactone which is about to be used by withstanding a high voltage is used, the influence thereof is particularly large. Until now, measures such as addition of a surfactant have been proposed in order to solve such a drawback, but the adverse effect on the battery performance cannot be remarkably used.

【0005】そこで、特開平2−244565号公報で
は、かかるリン系化合物を含有する非水電解液を用いる
ことによって、セパレーターへの含浸性が優れ、電池容
量が大きく、かつ電池電圧の大きい非水電池が得られる
ことが記載されている。この場合、電池性能に与える悪
影響は少なく、電解液のセパレーターへの含浸性は優
れ、大きな進歩は見られたものの、セパレーターへの含
浸速度の向上においては、けして満足するものではなか
った。
Therefore, in Japanese Patent Laid-Open No. 2-244565, by using a non-aqueous electrolyte containing such a phosphorus compound, the impregnating property of the separator is excellent, the battery capacity is large, and the non-aqueous electrolyte having a large battery voltage is used. It is described that a battery is obtained. In this case, the adverse effect on the battery performance was small, and the impregnation property of the electrolytic solution into the separator was excellent, and although great progress was made, the improvement of the impregnation speed into the separator was not entirely satisfactory.

【0006】[0006]

【発明が解決しようとする課題】本発明は、電解液の含
浸性に優れ、かつ、含浸速度の速いセパレーターを提供
することを目的とする。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a separator which is excellent in impregnation property with an electrolytic solution and has a high impregnation rate.

【0007】[0007]

【課題を解決するための手段】本発明者らは、前記従来
法の欠点を解決すべく鋭意検討した結果、ポリオレフィ
ン系微多孔膜を、かかるリン系化合物で処理したものを
非水電池用セパレーターとして用いることによって、電
解液のセパレーターへの含浸性が優れ、かつ含浸速度も
速くなることを見出した。
Means for Solving the Problems As a result of intensive studies made by the present inventors in order to solve the drawbacks of the conventional method, a polyolefin-based microporous membrane treated with such a phosphorus-based compound was used as a separator for a non-aqueous battery. It has been found that the use of the electrolyte as a separator makes it possible to improve the impregnation property of the electrolytic solution into the separator and to increase the impregnation speed.

【0008】すなわち、本発明はポリオレフィン系微多
孔膜が、下記化4、化5、化6に示される一般式
(1)、(2)、(3)の群から選ばれる少なくとも一
種のリン系化合物で処理されてなる非水電池用セパレー
ターである。
That is, according to the present invention, the microporous polyolefin film is at least one phosphorous compound selected from the group of the general formulas (1), (2) and (3) represented by the following chemical formulas 4, 5, and 6. A separator for a non-aqueous battery, which is treated with a compound.

【0009】[0009]

【化4】 [Chemical 4]

【0010】[0010]

【化5】 [Chemical 5]

【0011】[0011]

【化6】 [Chemical 6]

【0012】本発明において、ポリオレフィン系微多孔
膜は、特に限定されるものではないが、例えば、特開昭
54−52167号公報に記載されているような微細な
連通孔からなる網目構造を形成した微多孔膜が挙げられ
る。また、材質においては、ポリエチレン、ポリプロピ
レン、ポリブテン、およびこれらの混合物、さらに、エ
チレン、プロピレン、ブテン、ヘキセンの2種以上の共
重合物であってもよい。
In the present invention, the polyolefin microporous membrane is not particularly limited, but for example, it has a network structure composed of fine communication holes as described in JP-A-54-52167. Examples of the microporous film include: The material may be polyethylene, polypropylene, polybutene, a mixture thereof, or a copolymer of two or more kinds of ethylene, propylene, butene and hexene.

【0013】本発明において、該ポリオレフィン系微多
孔膜を処理するリン系化合物は、前記一般式(1)、
(2)、(3)で表わされるもので、例えば、トリブチ
ルホスフェート、トリオクチルホスフェート、トリノニ
ルホスフェート、トリデシルホスフェート、トリラウリ
ルホスフェート、トリセチルホスフェート、トリステア
リルホスフェート、トリフェニルホスフェート、トリク
レジルホスフェート、クレジルジフェニルホスフェー
ト、トリクロロブチルホスフェート、トリフェニルホス
ファイト、トリス・トリデシルホスファイト、エチルホ
スホン酸ジブチル、ブチルホスホン酸ジブチル等が挙げ
られる。
In the present invention, the phosphorus compound for treating the polyolefin microporous membrane is a compound represented by the general formula (1):
Represented by (2) and (3), for example, tributyl phosphate, trioctyl phosphate, trinonyl phosphate, tridecyl phosphate, trilauryl phosphate, tricetyl phosphate, tristearyl phosphate, triphenyl phosphate, tricresyl phosphate. , Cresyl diphenyl phosphate, trichlorobutyl phosphate, triphenyl phosphite, tris tridecyl phosphite, dibutyl ethylphosphonate, dibutyl butylphosphonate and the like.

【0014】本発明において、ポリオレフィン系微多孔
膜におけるリン系化合物の付着量は、特に限定されるも
のではないが、好ましくは0.01g(リン化合物)/
2(微多孔膜)〜6g/m2 さらに好ましくは0.0
5g/m2 〜3g/m2 、特に好ましくは0.1g/m
2 〜2g/m2 の範囲である。付着量が0.01g/m
2 未満の場合は、電解液のセパレーターへの含浸性が悪
いか、または含浸速度が遅いため、含浸工程が複雑にな
り、時間もかかり好ましくない、含浸性が悪い場合は、
含浸不良による電池性能の低下及びバラツキ等が発生し
好ましくない。付着量が6g/m2 を越える場合は、サ
イクル性及び高負荷特性等の劣下等のため、性能の良好
な電池が得られ難い。
In the present invention, the amount of the phosphorus compound attached to the polyolefin microporous membrane is not particularly limited, but is preferably 0.01 g (phosphorus compound) /
m 2 (microporous membrane) to 6 g / m 2 and more preferably 0.0
5g / m 2 ~3g / m 2 , particularly preferably 0.1 g / m
It is in the range of 2 to 2 g / m 2 . Adhesion amount is 0.01g / m
If less than 2 , impregnating property of the electrolytic solution into the separator is poor, or because the impregnation rate is slow, the impregnation step becomes complicated, and it is time-consuming and unfavorable.
Poor impregnation causes deterioration of battery performance and variations, which is not preferable. When the adhesion amount exceeds 6 g / m 2 , it is difficult to obtain a battery having good performance due to deterioration of cycleability and high load characteristics.

【0015】本発明において、ポリオレフィン系微多孔
膜を、かかるリン系化合物で処理する方法は、特に限定
されるものではないが、その一例を挙げれば、リン系化
合物の油性分散体を用いて各種含浸方式、コーティング
方式等によりポリオレフィン系微多孔膜に含浸、塗布
し、その後は、ポリオレフィン系微多孔膜が大きく変形
しない温度で乾燥することができる。
In the present invention, the method of treating the polyolefin microporous membrane with such a phosphorus compound is not particularly limited, but one example thereof is various methods using an oily dispersion of a phosphorus compound. The polyolefin-based microporous membrane can be impregnated and applied by an impregnation method, a coating method, or the like, and then dried at a temperature at which the polyolefin-based microporous membrane is not significantly deformed.

【0016】本発明における該セパレーターを、セパレ
ーターとして用いる電池としては特に限定されるもので
はないが、正極活物質として、例えば、TiS2 、Ti
3、MoS3 、FeS2 、Li(1-x) MnO2 、Li
(1-x) CoO2 、Li(1-x)NiO2 、V2 5 、V6
13等が挙げられる。負極活物質としては、例えば、リ
チウム、リチウム合金、炭素質材料、導電性ポリマー等
が挙げられる。
The battery using the separator of the present invention as a separator is not particularly limited, but examples of the positive electrode active material include TiS 2 and Ti.
S 3 , MoS 3 , FeS 2 , Li (1-x) MnO 2 , Li
(1-x) CoO 2 , Li (1-x) NiO 2 , V 2 O 5 , V 6
O 13 and the like can be mentioned. Examples of the negative electrode active material include lithium, lithium alloys, carbonaceous materials, conductive polymers and the like.

【0017】非水電解液の電解質としては、例えば、L
iClO4 、LlBF4 、LlAsF6 、CF3 SO3
Li、LiPF6 、LiI、LiAlCl4 、NaCl
4、NaBF4 、NaI等が挙げられる。又、用いら
れる電解液の有機溶媒としては、例えば、エーテル類、
ケトン類、ニトリル類、塩素化炭化水素類、カーボネー
ト類、スルホラン系化合物等を用いることができるが、
これらの代表例としては、テトラヒドロフラン、2−メ
チルテトラヒドロフラン、1,4−ジオキサン、アニソ
ール、モノグライム、アセトニトリル、プロピオニトリ
ル、4−メチル−2−ペンタン、ブチロニトリル、バレ
ロニトリル、ベンゾニトリル、1,2−ジクロロエタ
ン、γ−ブチロラクトン、ジメトキシエタン、メチルフ
ォルメイト、プロピレンカーボネート、エチレンカーボ
ネート、ビニレンカーボネート、ジメチルホルムアミ
ド、ジメチルスルホキシド、ジメチルチオホルムアミ
ド、スルホラン、3−メチル−スルホランおよびこれら
の混合溶媒等を挙げることができる。
As the electrolyte of the non-aqueous electrolyte, for example, L
iClO 4 , LlBF 4 , LlAsF 6 , CF 3 SO 3
Li, LiPF 6 , LiI, LiAlCl 4 , NaCl
O 4 , NaBF 4 , NaI and the like can be mentioned. The organic solvent used in the electrolytic solution is, for example, ethers,
Although ketones, nitriles, chlorinated hydrocarbons, carbonates, sulfolane compounds, etc. can be used,
As typical examples of these, tetrahydrofuran, 2-methyltetrahydrofuran, 1,4-dioxane, anisole, monoglyme, acetonitrile, propionitrile, 4-methyl-2-pentane, butyronitrile, valeronitrile, benzonitrile, 1,2- Examples thereof include dichloroethane, γ-butyrolactone, dimethoxyethane, methyl formate, propylene carbonate, ethylene carbonate, vinylene carbonate, dimethylformamide, dimethylsulfoxide, dimethylthioformamide, sulfolane, 3-methyl-sulfolane, and mixed solvents thereof. .

【0018】特に、プロピレンカーボネート、エチレン
カーボネート等の環状炭酸エステル類、γ−ブチロラク
トン等の環状エステル類、ジメチルスルフォキシド等の
スルフォキシド類などの高沸点系の溶媒および混合溶媒
を用いたとき、その中でも特開平2−215059号公
報に記載されている、環状炭酸エステル及び環状エステ
ルとその混合溶媒を用いたときに、リン系化合物で処理
されてなる非水電池用セパレーターを用いたことによる
含浸性及び含浸速度の向上効果が、たいへん顕著に現れ
る。また、これら電解液に該リン系化合物を少量添加し
てもなんらさしつかえなく、逆に電解液のセパレーター
に対する含浸性及び含浸速度は、添加しない場合と比較
すると、その効果に向上が見られる。
In particular, when high-boiling point solvents and mixed solvents such as cyclic carbonic acid esters such as propylene carbonate and ethylene carbonate, cyclic esters such as γ-butyrolactone, and sulfoxides such as dimethyl sulfoxide are used, Among them, impregnating property obtained by using a separator for a non-aqueous battery, which is treated with a phosphorus-based compound, when a cyclic ester carbonate and a cyclic ester and a mixed solvent thereof are used, which are described in JP-A-2-215059. And, the effect of improving the impregnation speed is very remarkable. Further, even if a small amount of the phosphorus-based compound is added to these electrolytes, it does not matter at all, and conversely, the effect of impregnating the electrolyte with respect to the separator and the impregnation speed are improved as compared with the case of not adding.

【0019】[0019]

【実施例】以下、本発明を詳細に説明するために実施例
を示すが、本発明は以下の実施例に特に限定されるもの
ではない。
EXAMPLES Examples will be shown below for illustrating the present invention in detail, but the present invention is not limited to the following examples.

【0020】[0020]

【実施例1】本実施例はポリオレフィン系微多孔膜にリ
ン系化合物を付着させる処理例を示す。ポリエチレン微
多孔膜であるハイポア4030U〔旭化成工業(株)
製、商品名〕をトリオクチルホスフェートの1重量%メ
タノール溶液中に、浸漬方式により含浸処理した後、6
0℃熱風乾燥を行い、付着量0.3g/m2 のセパレー
ターを得た。
Example 1 This example shows a treatment example in which a phosphorus compound is attached to a polyolefin microporous film. Hypore 4030U, a microporous polyethylene membrane [Asahi Kasei Corporation
Made by trade name] in a 1% by weight methanol solution of trioctyl phosphate by a dipping method.
It was dried with hot air at 0 ° C. to obtain a separator having an adhesion amount of 0.3 g / m 2 .

【0021】[0021]

【実施例2〜7】実施例1において、リン系化合物及び
そのメタノール溶液の濃度を表1に示すように変えた以
外は、全く同じ操作を行った。その時の付着量を合わせ
て表1に示す。
Examples 2 to 7 The same operation as in Example 1 was carried out except that the concentrations of the phosphorus compound and its methanol solution were changed as shown in Table 1. Table 1 also shows the amount of adhesion at that time.

【0022】[0022]

【実施例9】電解液1として、プロピレンカーボネート
にホウフッ化リチウムを1.0Mの濃度に調整した液を
用いて、実施例1で得られたセパレーターを、縦100
mm、幅15mmに切り取り、下端5mmを電解液中に
入れ、10分間でしみ上がった液面までの長さを測定
し、含浸速度(mm/10min)とした。その結果を
表2に示す。
[Example 9] As the electrolytic solution 1, a solution prepared by adjusting lithium borofluoride to a concentration of 1.0 M in propylene carbonate was used.
mm, width 15 mm, the lower end 5 mm was put into the electrolytic solution, and the length up to the liquid surface swelled in 10 minutes was measured to obtain the impregnation speed (mm / 10 min). The results are shown in Table 2.

【0023】次に電解液2として、プロピレンカーボネ
ートとエチレンカーボネートとγ−ブチロラクトンの混
合溶媒(体積比=1:1:2)にホウフッ化リチウムを
1.0Mの濃度に調整した液を用いて、以下同様の操作
を行った。その結果を表2に示す。さらに、電解液3と
して、上記3元系混合電解液に0.5重量%のトリオク
チルホスフェートを添加した液を用いて、以下同様の操
作を行った。その結果を表2に示す。
Next, as the electrolytic solution 2, a solution prepared by adjusting lithium borofluoride to a concentration of 1.0 M in a mixed solvent of propylene carbonate, ethylene carbonate and γ-butyrolactone (volume ratio = 1: 1: 2) is used. The same operation was performed thereafter. The results are shown in Table 2. Further, as the electrolytic solution 3, a solution obtained by adding 0.5% by weight of trioctyl phosphate to the above ternary mixed electrolytic solution was used, and the same operation was performed. The results are shown in Table 2.

【0024】[0024]

【実施例10〜16】セパレーターとして、実施例2〜
8で得られたものを用いた以外は、実施例9と同様の操
作を行った。その結果を表2に示す。
Examples 10 to 16 As a separator, Examples 2 to
The same operation as in Example 9 was performed except that the product obtained in 8 was used. The results are shown in Table 2.

【0025】[0025]

【比較例1】セパレーターとして、ポリエチレン微多孔
膜であるハイポア4030U〔旭化成工業(株)製、商
品名〕をトリオクチルホスフェートで処理しない以外
は、実施例9と同様の操作を行った。その結果を表2に
示す。
[Comparative Example 1] The same operation as in Example 9 was carried out except that, as a separator, a polyethylene microporous membrane, Hypore 4030U (trade name, manufactured by Asahi Kasei Kogyo KK) was not treated with trioctyl phosphate. The results are shown in Table 2.

【0026】[0026]

【実施例17】市販の石油系ニードルコークス〔興亜石
油(株)製 KOA−SJ COKE〕をボールミルで
平均粒径10μmに粉砕した。尚、このニードルコーク
スのBET表面積は、11m2 /g、真密度は、2.1
3g/cm3 、X線回折より得られる面間隔d002 、L
(002) はそれぞれ、3.44Å、52Åであった。こ
の粉末1重量部とポリアクリロニトリルのジメチルホル
ムアミド溶液(濃度4重量%)1重量部を混合した後、
10μm銅箔の両面に75μmの膜厚に製膜した。
Example 17 A commercially available petroleum-based needle coke [KOA-SJ COKE manufactured by Koa Oil Co., Ltd.] was crushed with a ball mill to an average particle size of 10 μm. The BET surface area of this needle coke was 11 m 2 / g and the true density was 2.1.
3 g / cm 3 , surface spacing d 002 , L obtained by X-ray diffraction
The c (002) was 3.44Å and 52Å, respectively. After mixing 1 part by weight of this powder with 1 part by weight of a solution of polyacrylonitrile in dimethylformamide (concentration 4% by weight),
A film having a thickness of 75 μm was formed on both surfaces of a 10 μm copper foil.

【0027】一方、LiCoO2 をボールミル平均粒径
3μmに粉砕した後、この粉末1重量部に対し、グラフ
ァイト0.05重量部、アセチレンブラック0.05重
量部、ポリフッ化ビニリデンのジメチルホルムアミド溶
液(濃度2重量%)1重量部を混合した後、15μmア
ルミ箔の両面に100μmの膜厚に製膜した。前記、ニ
ードルコークス塗膜を負極とし、LiCoO2 塗膜を正
極とし、実施例1で得られたものをセパレーターとして
介し、直径19mm、高さ78mmの円筒型電極コイル
を作製する。
On the other hand, after pulverizing LiCoO 2 into a ball mill having an average particle size of 3 μm, 0.05 part by weight of graphite, 0.05 part by weight of acetylene black, and a solution of polyvinylidene fluoride in dimethylformamide (concentration: 1 part by weight of this powder). After mixing 1 part by weight (2% by weight), a film having a thickness of 100 μm was formed on both sides of a 15 μm aluminum foil. A cylindrical electrode coil having a diameter of 19 mm and a height of 78 mm is produced by using the needle coke coating film as a negative electrode, the LiCoO 2 coating film as a positive electrode, and the one obtained in Example 1 as a separator.

【0028】次に図1に示した先端の内径19mmのガ
ラス製容器に、上記円筒型電極コイルを挿入し、真空度
20Torrに真空排気した後、コック操作により、実
施例9における電解液1を7.5ml注入し、その後、
容器内を大気圧にもどした。その時の電解液を注入して
から液が電極コイル内に完全にしみ込むまでの時間を測
定し含浸時期とした。その結果を表3に示す。
Next, the above cylindrical electrode coil was inserted into a glass container having an inner diameter of 19 mm at the tip shown in FIG. 1, and after evacuation to a vacuum degree of 20 Torr, the electrolytic solution 1 in Example 9 was operated by a cock operation. Inject 7.5 ml, then
The inside of the container was returned to atmospheric pressure. The impregnation time was measured by measuring the time from the injection of the electrolytic solution to the time when the solution completely permeated into the electrode coil. The results are shown in Table 3.

【0029】次に、電解液を実施例9における電解液2
を用いて、以下同様の操作を行った。その結果を表3に
示す。さらに、電解液を実施例9における電解液3を用
いて、以下同様の操作を行った。その結果を表3に示
す。
Next, the electrolytic solution was used as the electrolytic solution 2 in Example 9.
Then, the same operation was performed. The results are shown in Table 3. Furthermore, the same operation was performed using the electrolytic solution 3 of Example 9 as the electrolytic solution. The results are shown in Table 3.

【0030】[0030]

【実施例18〜24】セパレーターとして、実施例2〜
8で得られたものを用いた以外は、実施例17と同様の
操作を行った。その結果を表3に示す。
Examples 18 to 24 As a separator, Examples 2 to
The same operation as in Example 17 was performed except that the product obtained in 8 was used. The results are shown in Table 3.

【0031】[0031]

【比較例2】セパレーターとして、リン系化合物で処理
していないポリエチレン微多孔膜であるハイポア403
0U〔旭化成工業(株)製、商品名〕を用いた以外は、
実施例17と同様の操作を行った。その結果を表3に示
す。
[Comparative Example 2] Hypore 403, which is a polyethylene microporous membrane not treated with a phosphorus compound, as a separator
0 U [Asahi Kasei Kogyo KK, trade name] was used,
The same operation as in Example 17 was performed. The results are shown in Table 3.

【0032】[0032]

【表1】 [Table 1]

【0033】[0033]

【表2】 [Table 2]

【0034】[0034]

【表3】 [Table 3]

【0035】[0035]

【発明の効果】本発明によれば、電解液のセパレーター
への含浸性が優れ、かつ含浸速度も速くなることから非
水電池用のセパレーターとして非常に有用である。
EFFECTS OF THE INVENTION According to the present invention, the impregnating property of the electrolytic solution into the separator is excellent, and the impregnation speed is also high, and therefore it is very useful as a separator for a non-aqueous battery.

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

【図1】本発明の実施例および比較例に用いた電極コイ
ル含浸装置の断面図である(電解液及び電極コイルも合
わせて示す。)。
FIG. 1 is a cross-sectional view of an electrode coil impregnating apparatus used in Examples and Comparative Examples of the present invention (electrolyte solution and electrode coil are also shown).

【符号の説明】[Explanation of symbols]

1 電極コイル 2 ガラス製容器 3 電解液 4A,4B コック 1 Electrode Coil 2 Glass Container 3 Electrolyte 4A, 4B Cock

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ポリオレフィン系微多孔膜が下記化1、
化2、化3に示される一般式(1)、(2)、(3)の
群から選ばれる少なくとも一種のリン系化合物で処理さ
れてなる非水電池用セパレーター。 【化1】 【化2】 【化3】
1. A microporous polyolefin film is represented by the following chemical formula 1,
A separator for a non-aqueous battery, which is treated with at least one phosphorus compound selected from the group of formulas (1), (2) and (3) shown in Chemical formulas 2 and 3. [Chemical 1] [Chemical 2] [Chemical 3]
JP4173214A 1992-06-30 1992-06-30 Separator for nonaqueous battery Withdrawn JPH0620672A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4173214A JPH0620672A (en) 1992-06-30 1992-06-30 Separator for nonaqueous battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4173214A JPH0620672A (en) 1992-06-30 1992-06-30 Separator for nonaqueous battery

Publications (1)

Publication Number Publication Date
JPH0620672A true JPH0620672A (en) 1994-01-28

Family

ID=15956246

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4173214A Withdrawn JPH0620672A (en) 1992-06-30 1992-06-30 Separator for nonaqueous battery

Country Status (1)

Country Link
JP (1) JPH0620672A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018037310A (en) * 2016-08-31 2018-03-08 住友化学株式会社 Separator for nonaqueous electrolyte secondary battery

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018037310A (en) * 2016-08-31 2018-03-08 住友化学株式会社 Separator for nonaqueous electrolyte secondary battery

Similar Documents

Publication Publication Date Title
US11588143B2 (en) Battery
KR101854718B1 (en) Electrolyte for rechargeable lithium battery and rechargeable lithium battery including the same
EP2741362B1 (en) Electrolyte for rechargeable lithium battery and rechargeable lithium battery including the same
KR101706393B1 (en) Electrolyte for lithium secondary battery and lithium secondary battery comprising the same
KR101183939B1 (en) High Density Electrode and Battery Using the Electrode
KR20190116534A (en) Localized Super Concentrated Electrolyte for Stable Cycling of Electrochemical Devices
KR101784742B1 (en) Separator for rechargeable lithium battery, and electrode structure and rechargeable lithium battery including the same
US7976988B2 (en) Non-aqueous electrolyte and lithium secondary battery using the same
US20130040185A1 (en) Separator for rechargeable lithium battery, and electrode structure and rechargeable lithium battery including the same
KR101845878B1 (en) Positive electrode for rechargeable lithium battery, and rechargeable lithium battery including same
JPH0586032B2 (en)
JP6712782B2 (en) Battery positive electrode material and lithium ion battery
WO2020131175A1 (en) High efficiency electrolytes for high voltage battery systems
JPH0927328A (en) Nonaqueous battery
US20030148190A1 (en) Non-aqueous electrolyte and lithium secondary battery using the same
KR100368438B1 (en) Polymer electrolyte having multilayer structure, method for preparing the same and lithium secondary battery employing the same
KR102010325B1 (en) Lithium secondary battery comprising non-aqueous liquid electrolyte
JPH0620672A (en) Separator for nonaqueous battery
KR102151156B1 (en) Additive for non-aqueous liquid electrolyte, coating agent for separator and lithium secondary cell comprising the same
US20040048165A1 (en) Electrolyte for a secondary cell
WO2019171436A1 (en) Electrochemical device
JP2006004873A (en) Nonaqueous electrolyte secondary battery
US20240021872A1 (en) Electrode for quasi-solid li-ion battery
DE102023122226A1 (en) ION CONDUCTIVE MOLECULAR THERMAL BLANKETS
US20230021479A1 (en) Alkali metal electrodes and methods for preparing the same

Legal Events

Date Code Title Description
A300 Withdrawal of application because of no request for examination

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 19990831