JPH06101323B2 - Battery separator - Google Patents
Battery separatorInfo
- Publication number
- JPH06101323B2 JPH06101323B2 JP62290023A JP29002387A JPH06101323B2 JP H06101323 B2 JPH06101323 B2 JP H06101323B2 JP 62290023 A JP62290023 A JP 62290023A JP 29002387 A JP29002387 A JP 29002387A JP H06101323 B2 JPH06101323 B2 JP H06101323B2
- Authority
- JP
- Japan
- Prior art keywords
- polyethylene
- polypropylene
- sulfonated
- fiber
- resin
- 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
Links
- -1 polypropylene Polymers 0.000 claims description 39
- 239000000835 fiber Substances 0.000 claims description 38
- 239000004698 Polyethylene Substances 0.000 claims description 22
- 229920000573 polyethylene Polymers 0.000 claims description 22
- 229920005672 polyolefin resin Polymers 0.000 claims description 21
- 239000004743 Polypropylene Substances 0.000 claims description 17
- 229920001155 polypropylene Polymers 0.000 claims description 17
- 239000004745 nonwoven fabric Substances 0.000 claims description 14
- 229920005989 resin Polymers 0.000 claims description 13
- 239000011347 resin Substances 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 11
- 239000002344 surface layer Substances 0.000 claims description 9
- 239000002759 woven fabric Substances 0.000 claims description 4
- 229920001577 copolymer Polymers 0.000 claims description 3
- 239000000470 constituent Substances 0.000 claims 1
- 238000006277 sulfonation reaction Methods 0.000 description 8
- HIFJUMGIHIZEPX-UHFFFAOYSA-N sulfuric acid;sulfur trioxide Chemical compound O=S(=O)=O.OS(O)(=O)=O HIFJUMGIHIZEPX-UHFFFAOYSA-N 0.000 description 7
- 230000000694 effects Effects 0.000 description 5
- 239000007864 aqueous solution Substances 0.000 description 4
- 238000007654 immersion Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 229910003307 Ni-Cd Inorganic materials 0.000 description 3
- 238000007598 dipping method Methods 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 239000003513 alkali Substances 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- 150000002430 hydrocarbons Chemical group 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 229920002647 polyamide Polymers 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 2
- 125000001174 sulfone group Chemical group 0.000 description 2
- AKEJUJNQAAGONA-UHFFFAOYSA-N sulfur trioxide Chemical compound O=S(=O)=O AKEJUJNQAAGONA-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000005486 organic electrolyte Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229920013716 polyethylene resin Polymers 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229930195735 unsaturated hydrocarbon Natural products 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/44—Fibrous material
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/411—Organic material
- H01M50/414—Synthetic resins, e.g. thermoplastics or thermosetting resins
- H01M50/417—Polyolefins
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Cell Separators (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明はセパレータとして樹脂繊維製の不織布あるいは
織布を用いる電池の保存特性、とくに高温雰囲気下にお
ける自己放電特性の改良に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to improvement in storage characteristics of a battery using a non-woven fabric or woven fabric made of resin fiber as a separator, especially in self-discharge characteristics under high temperature atmosphere.
従来の技術 最近、種々の電子機器のポータブル化やそれらのメモリ
バックアップの必要性が増加するにつれ、これらの機器
用電源としての電池需要が高まってきた。ところ、この
ような電池の用途が拡大するに従って、従来以上に高温
雰囲気等の苛酷な使用条件で電池が用いられる機会も増
大し、電池特性においてはさらに自己放電特性等の保存
特性の改善が望まれるに至っている。この用途にはNi−
Cd電池がしばしば用いられるが、この電池は従来より一
般に自己放電が大きい電池系であり、とくにこの特性の
改善は大きな課題となっていた。たとえば、通常のNi−
Cd電池を完全充電した後、45℃の雰囲気で1ケ月間放電
すると放電容量が初期の1/3以下に減少し、放置後直ち
に使用するに際しては問題であった。2. Description of the Related Art Recently, as the need for portable various electronic devices and their memory backup has increased, the demand for batteries as a power source for these devices has increased. However, as the applications of such batteries expand, the chances that the battery will be used under severer operating conditions such as a high temperature atmosphere will increase more than before, and in terms of battery characteristics, further improvement in storage characteristics such as self-discharge characteristics is desired. Has been reached. Ni- for this application
A Cd battery is often used, but this battery is a battery system that generally has a large self-discharge, and improvement of this characteristic has been a major issue. For example, normal Ni-
When the Cd battery was fully charged and then discharged in an atmosphere of 45 ° C for one month, the discharge capacity decreased to 1/3 or less of the initial value, which was a problem when used immediately after leaving.
しかし最近の研究結果から、この自己放電を低減させる
重要な要因としてセパレータの改善が指摘されるように
なってきた。すなわち、通常使用されるポリアミド系繊
維製のセパレータの分解による不純物が、自己放電の増
大に起因するということが判明してきた。However, recent research results have pointed out the improvement of separators as an important factor for reducing this self-discharge. That is, it has been found that the impurities due to the decomposition of the commonly used polyamide fiber separator are caused by the increase in self-discharge.
そこで、適切な耐熱性を有し、かつ高温,高濃度のアル
カリ中でも分解しないセパレータ材料として、ポリプロ
ピレン等のオレフィン系樹脂の採用が注目されてきた。Therefore, the use of an olefin resin such as polypropylene has attracted attention as a separator material that has appropriate heat resistance and does not decompose even in high temperature and high concentration alkali.
ところが、ポリオレフィン系樹脂は親水性が乏しく電池
用セパレータとして必要な保液性に難点があるため、以
下のような親水処理に関する提案がなされてきた。However, since the polyolefin-based resin is poor in hydrophilicity and has a difficulty in liquid retention required as a battery separator, the following proposals for hydrophilic treatment have been made.
(1)界面活性剤を樹脂の表面に付着させる。(1) A surfactant is attached to the surface of the resin.
(2)樹脂にプラズマ照射して−CHO基などを化学的に
吸着させる。(2) Plasma is irradiated to the resin to chemically adsorb —CHO groups and the like.
(3)親水性を有する基、たとえばアクリル酸などをグ
ラフト重合させる。(3) A group having hydrophilicity such as acrylic acid is graft-polymerized.
(4)適切な温度と濃度の条件にある発煙硫酸や濃硫酸
中に樹脂を浸漬し、スルホン基(−SO3H)を樹脂中に導
入する。(4) the resin was immersed in fuming sulfuric acid or concentrated sulfuric acid in the appropriate temperature and concentration conditions, sulfone group and (-SO 3 H) is introduced into the resin.
発明が解決しようとする問題点 前記(1)の方法では、セパレータは高温、高濃度のア
ルカリ中で、しかも過充電時に正極で発生する酸素ガス
に触れることにより、界面活性剤がポリオレフィン系樹
脂材料から離脱し、不純物となってアルカリ水溶液中に
溶解する結果、自己放電を増大させる原因となる。前記
(2),(3)の方法も同様に、電池内での苛酷な酸化
によりそれぞれカルボン酸イオンおよびアクリル酸イオ
ンがアルカリ水溶液中に溶出してイオンが自己放電を増
大させる。これに対し(4)の方法では、前記したよう
な不純物あるいは不純物イオンが溶出することがほとん
どなく極めて自己放電の低減に有効であった。Problems to be Solved by the Invention In the above method (1), the separator is exposed to oxygen gas generated in the positive electrode during overcharge in a high temperature and high concentration alkali, so that the surfactant causes the polyolefin resin material to And becomes an impurity and dissolves in the alkaline aqueous solution, which results in an increase in self-discharge. Similarly, in the methods (2) and (3), carboxylic acid ions and acrylate ions are eluted into the alkaline aqueous solution due to severe oxidation in the battery, and the ions increase self-discharge. On the other hand, the method (4) was extremely effective in reducing self-discharge because the impurities or impurity ions as described above were hardly eluted.
ところが、単に同質のポリオレフィン系樹脂繊維あるい
は内部が酸化されやすいポリオレフィン系樹脂繊維を使
用した場合は、均一にスルホン化するための発煙硫酸や
濃硫酸の温度,濃度,浸漬時間等の条件範囲が狭く、工
業的には種々の問題となることが判明した。すなわち、
セパレータ材料としては樹脂繊維全体がほぼ均一に親水
性を有することが重要であるが、スルホン化されやすい
ポリオレフィン樹脂の不飽和炭化水素部分が不均一に存
在するため、樹脂全体をスルホン化しようとすると、繊
維の内部がスルホン化または酸化される部分が生じ、場
合によってはこの部分で繊維が炭化される結果セパレー
タの機械的強度が低下する危険性がある。当然樹脂繊維
どうしの接合部が炭化された場合はセパレータの強度低
下は著しくなる。However, when the same quality polyolefin resin fiber or polyolefin resin fiber whose inside is easily oxidized is used, the condition range such as temperature, concentration and immersion time of fuming sulfuric acid or concentrated sulfuric acid for uniform sulfonation is narrow. However, it has been found that it causes various problems industrially. That is,
As a separator material, it is important that the entire resin fiber has a substantially uniform hydrophilicity, but since the unsaturated hydrocarbon part of the polyolefin resin that is easily sulfonated is unevenly present, when trying to sulfonate the entire resin However, there is a risk that the inside of the fiber is sulfonated or oxidized, and in some cases the fiber is carbonized at this portion, resulting in a decrease in the mechanical strength of the separator. Naturally, when the joint between resin fibers is carbonized, the strength of the separator is significantly reduced.
問題点を解決するための手段 この問題点を解決するため本発明は、ポリオレフィン系
樹脂繊維の構造として内部が比較的スルホン化または酸
化されにくい材料とし、表面層付近には比較的スルホン
化されやすい材料を配したものとし、繊維相互のからみ
合い部分では内部の材料どうしも部分的に熱融着したも
のである。Means for Solving the Problems In order to solve this problem, the present invention uses a material whose interior is relatively sulfonated or oxidized as a structure of a polyolefin resin fiber, and is relatively easily sulfonated near the surface layer. The materials are arranged, and the internal materials are partially heat-sealed at the entangled portions of the fibers.
作用 このポリオレフィン系樹脂繊維の構成によれば親水性に
必要な表面層付近のスルホン化は容易であるとともに、
均一にスルホン化するために比較的長時間発煙硫酸など
に浸漬しても内部のポリオレフィン系樹脂は炭化されに
くくセパレータとしての強度が保てる。このことは樹脂
繊維相互間の接合部に関しても同様である。すなわち、
スルホン化に際して範囲の広いスルホン化処理条件が採
用でき工業的にも適している。この結果、化学的に安定
なスルホン基が均一にポリオレフィン系樹脂繊維に導入
されやすくなり、親水性の付与とともに自己放電の低減
に役立つこととなる。Effect According to the structure of this polyolefin resin fiber, sulfonation in the vicinity of the surface layer required for hydrophilicity is easy, and
In order to uniformly sulfonate, even if it is immersed in fuming sulfuric acid for a relatively long time, the polyolefin resin inside is hardly carbonized and the strength as a separator can be maintained. This also applies to the joint between the resin fibers. That is,
A wide range of sulfonation conditions can be adopted for sulfonation, which is industrially suitable. As a result, chemically stable sulfone groups are likely to be uniformly introduced into the polyolefin resin fiber, which contributes to imparting hydrophilicity and reducing self-discharge.
実施例 以下本発明の実施例を第1図から第3図を参照して説明
する。Embodiments Embodiments of the present invention will be described below with reference to FIGS. 1 to 3.
平均径約15μm,平均長約40mmのポリプロピレン製繊維の
集合体を解きほぐして分散させ、不織布を構成する。こ
の際、ポリエチレンを分散させた有機溶媒溶液を均一に
ふりかけ、前記繊維どおしに結着性を付与させる。得ら
れた不織布を150℃の熱ロール間に通過させて各繊維ど
おしを熱融着させ、最終的に厚さ0.2mm,多孔度約60%と
し、ポリプロピレンに対するポリエチレン量を約20%と
する。なお、この製法過程でポリエチレンを分散させた
溶媒は飛散するので、ほぼ完全にポリオレフィン系樹脂
で構成された不織布が得られ、これを構成する繊維は内
部はポリプロピレン,表面層付近はポリエチレンという
構造になる。A polypropylene fiber having an average diameter of about 15 μm and an average length of about 40 mm is loosened and dispersed to form a nonwoven fabric. At this time, an organic solvent solution in which polyethylene is dispersed is evenly sprinkled to give the fibers a binding property. The resulting non-woven fabric is passed between heat rolls at 150 ° C to heat-bond each fiber to a final thickness of 0.2 mm and a porosity of about 60%, and the amount of polyethylene to polypropylene is about 20%. To do. In addition, since the solvent in which polyethylene is dispersed scatters during this manufacturing process, a non-woven fabric composed almost entirely of polyolefin resin is obtained, and the fibers constituting this have a structure of polypropylene inside and polyethylene near the surface layer. Become.
この不織布を温度35℃,濃度20%の発煙硫酸中に約20分
間浸漬し、その後水洗,乾燥を施してポリエチレン部分
をスルホン化した親水性を有するセパレータを得る。こ
の後必要に応じて圧延ロール間を通過させて所望の厚さ
に調整してもよい。This non-woven fabric is immersed in fuming sulfuric acid at a temperature of 35 ° C. and a concentration of 20% for about 20 minutes, then washed with water and dried to obtain a hydrophilic separator having a sulfonated polyethylene portion. After that, it may be passed through between rolling rolls as necessary to adjust the thickness to a desired value.
第1図には、得られた不織布の概略図を示す。図中1は
表面部分がフルホン化された樹脂繊維、2は繊維間の空
間部である。第2図には、第1図1で示した繊維相互の
接合部における断面概略図を示した。斜線部3はポリプ
ロピレンの基材で、これを斜線部5のスルホン化された
ポリエチレンが覆っている。図面に平行な繊維と垂直な
繊維が6の交叉部分で熱融着され、ポリエチレン4の一
部はその内部に取り込まれている。図中黒色部は樹脂の
スルホン化された部分を示し、この部分はポリエチレン
の表面層を中心に一部はポリプロピレンにまで及んでい
る。又図中7はポリエチレンの存在しない欠陥部であ
る。スルホン化された大部分がポリエチレン層に留まっ
ているのは、ポリエチレンに比べてポリプロピレンがス
ルホン化されにくいためである。FIG. 1 shows a schematic view of the obtained nonwoven fabric. In the figure, 1 is a resin fiber whose surface portion is made into a fulphon, and 2 is a space between the fibers. FIG. 2 shows a schematic cross-sectional view of the joint portion between the fibers shown in FIG. The shaded portion 3 is a polypropylene base material, which is covered with the sulfonated polyethylene of the shaded portion 5. Fibers parallel to the drawing and fibers perpendicular to the drawing are heat-sealed at the intersections of 6 and part of the polyethylene 4 is incorporated therein. In the figure, the black part shows the sulfonated part of the resin, and this part extends from the surface layer of polyethylene to part of polypropylene. Reference numeral 7 in the figure is a defective portion where polyethylene does not exist. Most of the sulfonated compound remains in the polyethylene layer because polypropylene is less likely to be sulfonated than polyethylene.
スルホン化の進行に伴ないポリオレフィンが酸化されて
炭化し不織布としての機械的強度が低下する。そこで実
施例と同様な操作において、発煙硫酸中への浸漬時間だ
けを変えた不織布を試作し、幅20mm,長さ35mmの不織布
を長さ方向に引張り、切断されるまでの荷重を測定した
結果を次表に示した。なお、比較として平均径約15μm
のポリエチレンおよびポリプロピレン繊維だけで構成さ
れた不織布を同条件でスルホン化した場合の切断荷重も
同表に示す。また、これらの測定結果は、それぞれ5枚
の不織布の平均値で示した。As the sulfonation progresses, the polyolefin is oxidized and carbonized to lower the mechanical strength of the nonwoven fabric. Therefore, in the same operation as in the example, a non-woven fabric was produced by changing only the dipping time in fuming sulfuric acid, and the width of the non-woven fabric having a width of 20 mm and a length of 35 mm was pulled in the lengthwise direction, and the load was measured until it was cut. Is shown in the following table. For comparison, the average diameter is about 15 μm.
The same table also shows the cutting load when a non-woven fabric composed only of polyethylene and polypropylene fibers was sulfonated under the same conditions. In addition, these measurement results are shown as an average value of five nonwoven fabrics.
ここで、切断荷重は工業化に際しての経験値から約6kg
以上必要とされる。この基準を採用するとすれば、本発
明品は40分以内という広い浸漬時間範囲が許容されるの
に対し、ポリエチレン単独をスルホン化した場合は約5
分以内、ポリプロピレン単独をスルホン化した場合は約
30分以内の狭い範囲が要求される。また親水性の観点か
ら評価すると、本発明品の場合は浸漬時間が10分間以上
であれば、通常の充放電に全く支障をきたさない親水性
を有していた。これに対し、ポリプロピレン単独の場合
は約25分以上の浸漬時間が必要とされた。これらの結果
から本発明品は、10〜40分間の広い浸漬時間が許容され
工業的な大量処理に極めて好都合であることが明らかで
ある。この主たる原因は、本発明のような2重構造のポ
リオレフィン系樹脂繊維にスルホン化処理を施すと、ス
ルホン化されやすい、低級の炭化水素を出発物質とする
ポリエチレンの層が容易にスルホン化されるが、内部の
ポリプロピレンには、発煙硫酸が到達しにくいことも手
伝って、容易にスルホン化されにくいことに起因すると
考えられる。したがって比較的短時間の浸漬でほぼ均一
に繊維の表面がスルホン化され、ある程度長時間の浸漬
を行なっても繊維の深部は堅牢であるために機械的な強
度を保つことができると考えられる。又、繊維どうしの
接合部において、内部のポリプロピレンどおしが熱融着
されていることも強度向上に貢献していると考えられ
る。 Here, the cutting load is about 6 kg from the experience value in industrialization.
More than required. If this standard is adopted, a wide dipping time range of 40 minutes or less is allowed for the product of the present invention, whereas it is about 5 when polyethylene alone is sulfonated.
Within minutes, approx. When sulfonated polypropylene alone
A narrow range within 30 minutes is required. Further, when evaluated from the viewpoint of hydrophilicity, the product of the present invention had hydrophilicity that did not hinder normal charge / discharge at all when the immersion time was 10 minutes or more. On the other hand, when polypropylene was used alone, a soaking time of about 25 minutes or more was required. From these results, it is clear that the product of the present invention allows a wide dipping time of 10 to 40 minutes and is extremely convenient for industrial large-scale processing. The main reason for this is that when a polyolefin resin fiber having a double structure as in the present invention is subjected to a sulfonation treatment, a polyethylene layer having a lower hydrocarbon as a starting material, which is easily sulfonated, is easily sulfonated. However, it is considered that this is due to the fact that fuming sulfuric acid does not easily reach the polypropylene inside, and thus it is difficult to be easily sulfonated. Therefore, it is considered that the surface of the fiber is sulfonated almost uniformly by the immersion for a relatively short time, and the mechanical strength can be maintained because the deep part of the fiber is strong even after the immersion for a certain time. Further, it is considered that the polypropylene inside is heat-sealed at the joint between the fibers, which also contributes to the strength improvement.
このような観点から、ポリプロピレンとポリプロピレン
−ポリエチレンの共重合体を組み合わせた繊維およびポ
リプロピレン−ポリエチレンの共重合体とポリエチレン
を本発明のように組み合わせて繊維を採用しても、同様
な効果が得られることが明らかである。From such a point of view, the same effect can be obtained even if the fiber obtained by combining the polypropylene and the copolymer of polypropylene-polyethylene and the fiber of the polypropylene-polyethylene copolymer and polyethylene is combined as in the present invention. It is clear.
実施例で得られたセパレータを汎用のAAサイズのNi−Cd
電池に応用し、完全充電後45℃で保存したときの自己放
電を調べた結果を第3図のaで示した。比較例として、
ポリアミド系セパレータを用いた汎用の同型電池の結果
をbで示した。図中縦軸のパラメータである残存容量は
(100%−自己放電量%)を意味する。この結果から本
発明によるセパレータを使用したNi−Cd電池は、自己放
電が極めて少なく、45℃で約1ケ月放置してもまだ70%
程度の容量を保持していることがわかる。The separator obtained in the example was used as a general-purpose AA-sized Ni-Cd.
The result of examining self-discharge when applied to a battery and stored at 45 ° C. after fully charged is shown in a of FIG. As a comparative example,
The result of a general-purpose battery of the same type using a polyamide-based separator is shown by b. The remaining capacity, which is a parameter on the vertical axis in the figure, means (100% -self-discharge amount%). From this result, the Ni-Cd battery using the separator according to the present invention has very little self-discharge, and it is still 70% even if left at 45 ° C for about 1 month.
It can be seen that the capacity is maintained.
なお、本実施例では不織布ついてのみ記載したが織布に
ついても同様な効果が認められた。また、このセパレー
タは、アルカリ水溶液を使用する電池に対してはもちろ
んのこと、その他の水溶液および有機電解質を用いる電
池に対しても適用が可能であり、化学的な安定性と親液
性に優れることから保存性および電解液の注液性の向上
に有効である。またスルホン化の処理には発煙硫酸など
の溶液を用いる他に、三酸化イオウのガスを使用しても
よい。In this example, only the non-woven fabric was described, but the same effect was observed for the woven fabric. Further, this separator can be applied not only to a battery using an alkaline aqueous solution but also to a battery using another aqueous solution and an organic electrolyte, and is excellent in chemical stability and lyophilicity. Therefore, it is effective in improving the storage stability and the electrolyte injection property. In addition to the solution such as fuming sulfuric acid, a gas of sulfur trioxide may be used for the sulfonation treatment.
発明の効果 以上の説明から明らかなように、表面層付近が内部より
もスルホン化されやすいポリオレフィン系樹脂繊維で構
成された不織布あるいは織布をスルホン化したセパレー
タはスルホン化の工程で範囲の広い条件、たとえば処理
時間などが採用できしかも均一に繊維全体が処理できる
ため工業的に適しており、このセパレータを用いた電池
では自己放電特性が著しく改善できるという効果があ
る。EFFECTS OF THE INVENTION As is apparent from the above description, the sulfonated separator of the non-woven fabric or the woven fabric composed of the polyolefin resin fiber in which the surface layer is more easily sulfonated than the interior has a wide range of conditions in the sulfonation process. For example, a treatment time can be adopted and the entire fiber can be uniformly treated, which is industrially suitable, and a battery using this separator has an effect of remarkably improving self-discharge characteristics.
第1図は本発明によるセパレータの概略図、第2図は第
1図で示したスルホン化されたポリオレフィン系樹脂繊
維の拡大断面図、第3図は同セパレータを用いたNi−Cd
電池の自己放電特性を示す図である。 1……スルホン化されたポリオレフィン系樹脂繊維、2
……空間部、3……ポリプロピレン、4……ポリエチレ
ン、5……スルホン化されたポリエチレン樹脂部、6…
…繊維どおしの接合部、7……ポリエチレンの欠陥部。FIG. 1 is a schematic view of a separator according to the present invention, FIG. 2 is an enlarged cross-sectional view of the sulfonated polyolefin resin fiber shown in FIG. 1, and FIG. 3 is a Ni-Cd using the same separator.
It is a figure which shows the self-discharge characteristic of a battery. 1 ... Sulfonated polyolefin resin fiber, 2
...... Space, 3 ... Polypropylene, 4 ... Polyethylene, 5 ... Sulfonated polyethylene resin part, 6 ...
… Bonded parts of fibers, 7 …… Defective parts of polyethylene.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 池山 正一 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 岩崎 和隆 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (56)参考文献 特開 昭57−141862(JP,A) 特開 昭57−131233(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Shoichi Ikeyama 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (72) Inventor Kazutaka Iwasaki 1006 Kadoma, Kadoma City, Osaka Matsushita Electric Industrial Co., Ltd. (56) References JP 57-141862 (JP, A) JP 57-131233 (JP, A)
Claims (4)
繊維の不織布あるいは織布から成る電池用セパレータで
あって前記繊維は内部と大部分の表面層とが異質のポリ
オレフィン系樹脂材料で構成され、表面層の樹脂材料の
方が内部のそれよりもスルホン化されやすい材料であ
り、主にこの表面層の樹脂材料がスルホン化されている
ことを特徴とする電池用セパレータ。1. A battery separator comprising a non-woven fabric or a woven fabric of a fiber whose main constituent is a polyolefin-based resin, wherein the fiber is composed of a polyolefin-based resin material whose inside and most of the surface layer are different from each other, A battery separator characterized in that the resin material of the surface layer is a material that is more easily sulfonated than that of the inside, and that the resin material of the surface layer is mainly sulfonated.
ピレンまたはポリプロピレンとポリエチレンとの共重合
体である特許請求の範囲第1項記載の電池用セパレー
タ。2. The battery separator according to claim 1, wherein the internal polyolefin resin is polypropylene or a copolymer of polypropylene and polyethylene.
プロピレンとポリエチレンの共重合体またはポリエチレ
ンである特許請求の範囲第1項記載の電池用セパレー
タ。3. The battery separator according to claim 1, wherein the polyolefin resin with a surface layer is a copolymer of polypropylene and polyethylene or polyethylene.
融着されており、この融着部では繊維の内部のポリオレ
フィン系樹脂どおしも熱融着されている特許請求の範囲
第1項記載の電池用セパレータ。4. The contact portion between the polyolefin resin fibers is heat-sealed, and the polyolefin resin inside the fibers is also heat-sealed at this weld portion. The battery separator described.
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62290023A JPH06101323B2 (en) | 1987-11-17 | 1987-11-17 | Battery separator |
| US07/272,998 US5100723A (en) | 1987-11-17 | 1988-11-17 | Separator material for storage batteries |
| EP19880119142 EP0316916B1 (en) | 1987-11-17 | 1988-11-17 | Separator material for storage batteries and method for making the same |
| DE3887460T DE3887460T2 (en) | 1987-11-17 | 1988-11-17 | Separator material for storage batteries and method for the production thereof. |
| US07/795,141 US5213722A (en) | 1987-11-17 | 1991-11-20 | Method of making a separator material for a storage battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62290023A JPH06101323B2 (en) | 1987-11-17 | 1987-11-17 | Battery separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01132044A JPH01132044A (en) | 1989-05-24 |
| JPH06101323B2 true JPH06101323B2 (en) | 1994-12-12 |
Family
ID=17750791
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62290023A Expired - Lifetime JPH06101323B2 (en) | 1987-11-17 | 1987-11-17 | Battery separator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH06101323B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001043843A (en) * | 1999-05-21 | 2001-02-16 | Oji Paper Co Ltd | Method for producing separator for alkaline battery |
| JP2001167748A (en) * | 1999-12-09 | 2001-06-22 | Japan Vilene Co Ltd | Battery separator |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07122164B2 (en) * | 1990-03-26 | 1995-12-25 | 金井重要工業株式会社 | Battery separator and manufacturing method thereof |
| DE60229345D1 (en) | 2001-11-12 | 2008-11-27 | Toyota Motor Co Ltd | Alkaline storage battery |
| FR2918389B1 (en) | 2007-07-06 | 2009-09-25 | Saft Groupe Sa | NEGATIVE ACTIVE MATERIAL FOR ACCUMULATOR NICKEL METAL HUDRURE |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5365931A (en) * | 1976-11-25 | 1978-06-12 | Kanai Hiroyuki | Sepator for alkaline battery and method of manufacturing same |
| JPS563973A (en) * | 1979-06-21 | 1981-01-16 | Matsushita Electric Ind Co Ltd | Manufacture of separator for battery |
| JPS5740527A (en) * | 1980-08-22 | 1982-03-06 | Asahi Chem Ind Co Ltd | Hydrophilic membrane and its preparation |
| JPS57131233A (en) * | 1981-02-06 | 1982-08-14 | Asahi Chem Ind Co Ltd | Production of hydrophilic membrane having good durability |
| JPS57141862A (en) * | 1981-02-23 | 1982-09-02 | Yuasa Battery Co Ltd | Separator for battery |
| JPS57191956A (en) * | 1981-05-19 | 1982-11-25 | Matsushita Electric Ind Co Ltd | Manufacture of separator for battery |
| JPS58149905A (en) * | 1982-03-03 | 1983-09-06 | Asahi Chem Ind Co Ltd | Sulfonation of polyolefin |
| JPS58210906A (en) * | 1982-06-02 | 1983-12-08 | Asahi Chem Ind Co Ltd | Treatment of sulfonated polyolefin |
| JPS599255A (en) * | 1982-06-29 | 1984-01-18 | チッソ株式会社 | Heat adhesive nonwoven fabric |
| JPS62115657A (en) * | 1985-11-13 | 1987-05-27 | Matsushita Electric Ind Co Ltd | Sealed nickel-hydrogen storage battery |
-
1987
- 1987-11-17 JP JP62290023A patent/JPH06101323B2/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2001043843A (en) * | 1999-05-21 | 2001-02-16 | Oji Paper Co Ltd | Method for producing separator for alkaline battery |
| JP2001167748A (en) * | 1999-12-09 | 2001-06-22 | Japan Vilene Co Ltd | Battery separator |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01132044A (en) | 1989-05-24 |
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| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |