JPH0778145B2 - Polyolefin microporous film and electrolytic solution separator comprising the same - Google Patents
Polyolefin microporous film and electrolytic solution separator comprising the sameInfo
- Publication number
- JPH0778145B2 JPH0778145B2 JP62167456A JP16745687A JPH0778145B2 JP H0778145 B2 JPH0778145 B2 JP H0778145B2 JP 62167456 A JP62167456 A JP 62167456A JP 16745687 A JP16745687 A JP 16745687A JP H0778145 B2 JPH0778145 B2 JP H0778145B2
- Authority
- JP
- Japan
- Prior art keywords
- film
- porosity
- electrolytic solution
- polyolefin microporous
- liquid paraffin
- 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
- 229920000098 polyolefin Polymers 0.000 title claims description 22
- 239000008151 electrolyte solution Substances 0.000 title claims description 14
- 229940057995 liquid paraffin Drugs 0.000 claims description 20
- 239000011148 porous material Substances 0.000 claims description 13
- 238000002844 melting Methods 0.000 description 9
- 230000008018 melting Effects 0.000 description 9
- 239000010410 layer Substances 0.000 description 7
- 239000003990 capacitor Substances 0.000 description 6
- -1 ethylene, propylene, butene Chemical class 0.000 description 6
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 5
- 239000000123 paper Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- VOWAEIGWURALJQ-UHFFFAOYSA-N Dicyclohexyl phthalate Chemical compound C=1C=CC=C(C(=O)OC2CCCCC2)C=1C(=O)OC1CCCCC1 VOWAEIGWURALJQ-UHFFFAOYSA-N 0.000 description 4
- 239000004743 Polypropylene Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 239000003792 electrolyte Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 229920001155 polypropylene Polymers 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000002344 surface layer Substances 0.000 description 3
- CXWXQJXEFPUFDZ-UHFFFAOYSA-N tetralin Chemical compound C1=CC=C2CCCCC2=C1 CXWXQJXEFPUFDZ-UHFFFAOYSA-N 0.000 description 3
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 2
- YEJRWHAVMIAJKC-UHFFFAOYSA-N 4-Butyrolactone Chemical compound O=C1CCCO1 YEJRWHAVMIAJKC-UHFFFAOYSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229920005672 polyolefin resin Polymers 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 1
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000003945 anionic surfactant Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000003093 cationic surfactant Substances 0.000 description 1
- 229960001701 chloroform Drugs 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000003851 corona treatment Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- 238000009998 heat setting Methods 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 239000002655 kraft paper Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000012982 microporous membrane Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000002736 nonionic surfactant Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- RNNGKNBZYALDNU-UHFFFAOYSA-N phosphoric acid;triphenylene Chemical compound OP(O)(O)=O.C1=CC=C2C3=CC=CC=C3C3=CC=CC=C3C2=C1 RNNGKNBZYALDNU-UHFFFAOYSA-N 0.000 description 1
- 125000005498 phthalate group Chemical class 0.000 description 1
- 238000009832 plasma treatment Methods 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000012748 slip agent Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] この発明は新規なポリオレフィンフィルム及びそれから
成る電解液セパレータに関する。TECHNICAL FIELD The present invention relates to a novel polyolefin film and an electrolytic solution separator comprising the same.
[従来の技術] 電解コンデンサ、リチウム電池、バッテリー等に用いら
れる電解液セパレータとして、古くからクラフト紙、マ
ニラ紙等の電解紙が用いられているが、最近は例えば実
開昭59-140429号、特開昭61-13614号及び特公昭59-3729
2号に記載されているように、微孔性ポリオレフィンフ
ィルムを用いることが提案されている。[Prior Art] As electrolytic solution separators used in electrolytic capacitors, lithium batteries, batteries, etc., electrolytic papers such as kraft paper and manila paper have been used for a long time, but recently, for example, Japanese Utility Model Publication No. 59-140429. JP-A-61-13614 and JP-B-59-3729
It has been proposed to use microporous polyolefin films, as described in No. 2.
[従来技術の欠点] ポリオレフィン微孔性フィルムは従来の技術の電解紙に
比較し、孔の均一性、連続性に優れるために、内部抵抗
を低減する上で好ましいが、電解液の保持力に劣るた
め、電気特性の経時変化が大ききという欠点を有する。[Disadvantages of Prior Art] Polyolefin microporous film is preferable for reducing internal resistance because it has excellent pore uniformity and continuity as compared with conventional electrolytic paper. Since it is inferior, it has a drawback that the change over time in the electrical characteristics is large.
[発明が解決しようとする問題点] この発明の目的は、電解液セパレータとして用いた場合
に、電解液の保持力に優れて電気特性の経時変化が小さ
く、かつ、等価直列抵抗(ESR)の小さなポリオレフィ
ン微孔性フィルムを提供することである。[Problems to be Solved by the Invention] An object of the present invention is, when used as an electrolytic solution separator, excellent in retaining force of an electrolytic solution, small change in electrical characteristics over time, and equivalent series resistance (ESR). It is to provide a small polyolefin microporous film.
[問題点を解決するための手段] 本願発明者らは、鋭意研究の結果、フィルムの表層の見
掛け空孔率を全層の平均空孔率よりも小さくすることに
よって、等価直列抵抗を実質的に増大させることなく電
解液の保持力を有意に高めることができることを見出し
この発明を完成した。[Means for Solving the Problems] As a result of earnest research, the inventors of the present application have made the equivalent porosity substantially lower by making the apparent porosity of the surface layer of the film smaller than the average porosity of all layers. The inventors have completed the present invention by finding that the holding power of the electrolytic solution can be significantly increased without increasing the above.
すなわち、この発明は、表面での見掛け空孔率が10%か
ら45%、全層平均空孔率が50%から85%、流動パラフィ
ン透過時間が5秒以下であり、かつ、フィルム中層部の
平均空孔径が0.05μmから5μmで表面での見掛けの平
均空孔径が0.01μmから4μmであるポリオレフィン系
微孔性フィルム及びこれから成る電解液セパレータを提
供する。That is, the invention has an apparent porosity on the surface of 10% to 45%, an average porosity of all layers of 50% to 85%, a liquid paraffin permeation time of 5 seconds or less, and Provided is a polyolefin microporous film having an average pore diameter of 0.05 μm to 5 μm and an apparent average pore diameter on the surface of 0.01 μm to 4 μm, and an electrolytic solution separator comprising the same.
[発明の具体的説明] 上述したように、この発明のポリオレフィン系微孔性フ
ィルムは、その表面での見掛け空孔率が10%から45%、
好ましくは20%から40%である。表面での見掛け空孔率
が10%よりも小さいと電解液セパレーとして用いた場合
に等価直列抵抗が大きくなり、45%よりも大きいと電解
液の保持力が低下してドライアップするおそれが高くな
る。フィルム表面の見掛けの空孔率はフィルムの表側と
裏側で同じであっても異なっていてもよい。また、フィ
ルム全体の平均空孔率は50%から85%であり、好ましく
は60%から75%である。全体の平均空孔率が50%未満で
あると電解液の保持力が低下し、ドライアップする確率
が高くなり、85%を超えると機械強度が低下しショート
発生率が大きくなる。[Detailed Description of the Invention] As described above, the polyolefin microporous film of the present invention has an apparent porosity of 10% to 45% on its surface,
It is preferably 20% to 40%. If the apparent porosity on the surface is less than 10%, the equivalent series resistance will increase when used as an electrolyte solution separator, and if it is greater than 45%, the electrolyte retention will decrease and there is a high risk of dry-up. Become. The apparent porosity of the film surface may be the same or different on the front side and the back side of the film. The average porosity of the entire film is 50% to 85%, preferably 60% to 75%. If the average porosity of the whole is less than 50%, the electrolytic solution holding power decreases, and the probability of dry-up increases, and if it exceeds 85%, the mechanical strength decreases and the short-circuit occurrence rate increases.
フィルムの流動パラフィン透過時間は5秒以下であり、
好ましくは3秒以下である。流動パラフィン透過時間が
5秒を超えると等価直列抵抗が大きくなる。流動パラフ
ィン透過時間の下限は特にないが、透過時間が0.5秒未
満のものは機械特性が低い場合があるので透過時間は0.
5秒以上のものが望ましい。The liquid paraffin permeation time of the film is 5 seconds or less,
It is preferably 3 seconds or less. If the liquid paraffin permeation time exceeds 5 seconds, the equivalent series resistance increases. There is no particular lower limit for the liquid paraffin permeation time, but if the permeation time is less than 0.5 seconds, the mechanical properties may be low, so the permeation time is 0.
5 seconds or more is desirable.
等価直列抵抗及びショート発生率の観点から、フィルム
中層部の平均空孔径は0.05μmから5μmとし、特に0.
1μmから3μmであることが好ましい。また、表面で
の見掛けの平均空孔径は電解液の保持力及び等価直列抵
抗の観点から0.01μmから4μmとし、特に0.05μmか
ら2μmが好ましい。From the viewpoint of equivalent series resistance and occurrence rate of short circuit, the average pore diameter of the middle layer of the film is set to 0.05 μm to 5 μm, especially
It is preferably 1 μm to 3 μm. Further, the apparent average pore diameter on the surface is 0.01 μm to 4 μm, and particularly preferably 0.05 μm to 2 μm, from the viewpoint of holding power of the electrolytic solution and equivalent series resistance.
フィルムの厚みは取扱い性、電気特性の観点から10μm
から50μm、特に20μmから40μmであることが好まし
い。The thickness of the film is 10 μm from the viewpoint of handleability and electrical characteristics.
To 50 μm, particularly preferably 20 to 40 μm.
本発明でいうポリオレフィンとは、エチレン、プロピレ
ン、ブテン、ペンテン、ヘキセン等に示されるα−オレ
フィンの単独重合体あるいは共重合体及びこれらのブレ
ンド物であるが、この中でもポリエチレン、ポリプロピ
レンが耐熱性、耐寒性、機械特性が優れているので好ま
しく、よく使用される。さらに、ポリプロピレンの中で
も、極限粘度([η])が1.8〜3.3dl/g、より好ましく
は2.7〜3.1dl/g、アイソタクチックインデックス(II)
が93%以上のものは、寸法安定性、耐溶剤性に優れるの
で好ましい。また、素子製造中に加えられる熱に対する
耐熱性の観点から、ポリオレフィンの融点は120℃以上
であることが好ましい。The polyolefin referred to in the present invention is ethylene, propylene, butene, pentene, homopolymers or copolymers of α-olefins represented by hexene and blends thereof, among which polyethylene, polypropylene is heat resistant, It is often used because it has excellent cold resistance and mechanical properties. Furthermore, among polypropylene, the intrinsic viscosity ([η]) is 1.8 to 3.3 dl / g, more preferably 2.7 to 3.1 dl / g, and the isotactic index (II).
Is preferably 93% or more because it is excellent in dimensional stability and solvent resistance. Further, from the viewpoint of heat resistance against heat applied during element production, the melting point of the polyolefin is preferably 120 ° C. or higher.
この発明のポリオレフィン系微孔性フィルムは以下のよ
うにして製造することができる。ポリオレフィン樹脂10
0容量部に、ジシクロヘキシルフタレート(DCHP)又は
トリフェニレンフォスフェイト(TPP)のような塩化ビ
ニル等の可塑剤として使用されているフタル酸エステル
又はリン酸エステル等の有機固体80容量部から180容量
部、好ましくは90容量部から160容量部を配合し、溶融
押出しした後、トリクロルメタン、トリクロルエタン、
アセトン、メチルエチルケトン、酢酸エチル、メタノー
ル、トルエン、キシレン等の有機固定の良溶媒を用い
て、上記有機固体の添加量の95%以上を抽出するのが好
ましく、より好ましくは98%以上である。次に、ポリオ
レフィンのガラス転移点以上で融点−10℃の温度下でロ
ール延伸を行なう。この際、表面の空孔率を小さくする
ために、低速ロール又は高速ロールのいずれか一方、好
ましくは両方の上でフィルムをニップする。ニップの圧
力は線圧で2kg/cmから50kg/cmが適当である。延伸後、
ポリオレフィンの溶融結晶化温度以上で融点−5℃の温
度範囲で熱固定することが好ましい。The polyolefin microporous film of the present invention can be manufactured as follows. Polyolefin resin 10
In 0 parts by volume, from 80 parts by volume to 180 parts by volume of organic solids such as phthalates or phosphates used as plasticizers such as vinyl chloride such as dicyclohexyl phthalate (DCHP) or triphenylene phosphate (TPP), Preferably from 90 parts by volume to 160 parts by volume, after melt extrusion, trichloromethane, trichloroethane,
It is preferable to extract 95% or more, and more preferably 98% or more of the added amount of the organic solid using a good organic fixed solvent such as acetone, methyl ethyl ketone, ethyl acetate, methanol, toluene, xylene. Next, roll drawing is carried out at a temperature not lower than the glass transition point of the polyolefin and having a melting point of -10 ° C. At this time, in order to reduce the porosity of the surface, the film is nipped on either the low speed roll or the high speed roll, preferably both. A suitable pressure for the nip is a linear pressure of 2 kg / cm to 50 kg / cm. After stretching,
It is preferable to heat-set in the temperature range of melting point -5 ° C or higher than the melting crystallization temperature of the polyolefin.
上記製造方法では延伸時にロール上でフィルムをニップ
することにより表面の見掛け空孔率を小さくしたが、フ
ィルム延伸前又は延伸後にポリオレフィンの融点−50℃
から融点−5℃の加熱ロールで上記圧力でニップするこ
とによっても表面の見掛け空孔率を小さくすることがで
きる。さらに、上記有機固体の配合量が比較的少ないも
のと多いものを準備し、配合量が多いものが中央にくる
ようにして3層の共押出しをすることによっても表面の
見掛け空孔率が小さなフィルムを得るころができる。In the above production method, the apparent porosity of the surface was reduced by nipping the film on a roll during stretching, but the melting point of the polyolefin before or after stretching the film was −50 ° C.
Therefore, the apparent porosity of the surface can also be reduced by nipping with a heating roll having a melting point of −5 ° C. at the above pressure. Furthermore, the apparent porosity of the surface is also small by preparing one with a relatively small amount of the organic solid and a large amount of the organic solid, and coextruding three layers so that the one with a large amount of the compound is in the center. It's time to get a film.
この発明のポリオレフィン微孔性膜は、性能の観点から
ポリオレフィンのみから成っていることが好ましいが、
上記した見掛け空孔率、平均空孔率及び流動パラフィン
透過時間がこの発明の範囲内に入るならば、微量の不純
物を含んでいても差支えなく、また、例えば熱安定剤、
酸化防止剤、滑り剤、帯電防止剤等の添加剤やオレフィ
ン以外のモノマーを微量配合しても差支えない。特許請
求の範囲でいう「ポリオレフィン系微孔性フィルム」と
はこのような不純物、添加剤等を含んだポリオレフィン
微孔性フィルムをも包含する意味で用いている。The polyolefin microporous membrane of the present invention is preferably composed only of polyolefin from the viewpoint of performance,
If the above-mentioned apparent porosity, average porosity and liquid paraffin permeation time are within the scope of the present invention, it may be possible to contain a trace amount of impurities, and, for example, a heat stabilizer,
Additives such as antioxidants, slip agents, antistatic agents, and monomers other than olefins may be added in small amounts. The term "polyolefin microporous film" used in the claims is meant to include a polyolefin microporous film containing such impurities and additives.
ポリオレフィン系微孔性フィルムを電解セパレータとし
て用いる場合には、電解液との親和性を良くするために
親水化処理を施しておくことが好ましい。親水化処理
は、非イオン系界面活性剤、アニオン若しくはカチオン
系界面活性剤等のコーティング、コロナ若しくはプラズ
マ処理、グラフト処理、紫外線処理又はこれらの組合せ
によって行なうことができる。When the polyolefin microporous film is used as the electrolytic separator, it is preferable that a hydrophilic treatment is performed in order to improve the affinity with the electrolytic solution. The hydrophilic treatment can be performed by coating with a nonionic surfactant, an anionic or cationic surfactant, corona or plasma treatment, graft treatment, ultraviolet treatment, or a combination thereof.
[発明の効果] この発明のポリオレフィン微孔性フィルムでは、フィル
ム全体の平均空孔率が50%から85%と高いにもかかわら
ず表面の空孔率が低く、かつ、フィルム中層部と表面で
の平均空孔径を等価直列抵抗等の観点から最適な範囲と
したため、電解液セパレータとして用いた場合に電解液
の保持力に優れ、電気特性の経時変化が少ない。また、
流動パラフィン透過時間が5秒以下であるので等価直列
抵抗が低い。さらに、フィルムの表層構造がしっかりし
ているので耐ピンホール性も良好である。[Effect of the Invention] In the polyolefin microporous film of the present invention, although the average porosity of the entire film is as high as 50% to 85%, the porosity of the surface is low, and the film middle layer portion and the surface have Since the average pore diameter of 1 is set in the optimum range from the viewpoint of equivalent series resistance and the like, when used as an electrolyte separator, the electrolyte retainability is excellent and the change in electrical characteristics over time is small. Also,
Since the liquid paraffin permeation time is 5 seconds or less, the equivalent series resistance is low. Furthermore, since the surface layer structure of the film is firm, the pinhole resistance is also good.
[特性の測定方法及び効果の評価方法] 次にこの発明に関する特性の測定方法及び評価方法につ
いて、まとめて示す。[Characteristic Measuring Method and Effect Evaluation Method] Next, the characteristic measuring method and evaluation method relating to the present invention will be summarized.
(1)極限粘度([η]) 試料0.1gを135℃のテトラリン100mlに完全溶解させ、こ
の溶液を粘度計で135℃の恒温槽中で測定した比粘度S
より次式に従って極限粘度を求める。(1) Intrinsic viscosity ([η]) 0.1 g of a sample was completely dissolved in 100 ml of tetralin at 135 ° C, and this solution was measured with a viscometer in a constant temperature bath at 135 ° C to obtain a specific viscosity S.
The intrinsic viscosity is calculated according to the following equation.
[η]=S/{0.1×(1+0.22×S)} (2)アイソタクチックインデックス(II) 試料を130℃で2時間真空乾燥する。これから重量W(m
g)の試料を取り、ソックスレー抽出器に入れ、沸騰n
−ペプタンで12時間抽出する。次にこの試料を取り出
し、アセトンで十分洗浄した後、130℃で6時間真空乾
燥し、その後重量W−(mg)を測定し、次式で求める。[Η] = S / {0.1 × (1 + 0.22 × S)} (2) Isotactic index (II) The sample is vacuum dried at 130 ° C. for 2 hours. From now on, weight W (m
Take the sample of g), put it in a Soxhlet extractor, and boil it n
-Extract for 12 hours with peptane. Next, this sample is taken out, thoroughly washed with acetone, and then vacuum dried at 130 ° C. for 6 hours, and then the weight W- (mg) is measured and calculated by the following formula.
II(%)=(W-/W)×100 (3)ポリオレフィンの融点 走査型熱量DSC−2型(パーキン・エルマー社製)を用
い、試料5mgを窒素気流下で、昇温速度20℃/分にて室
温より測定し、融解に伴う吸熱ピーク温度を融点とす
る。II (%) = (W − / W) × 100 (3) Melting point of polyolefin Scanning calorific value DSC-2 type (manufactured by Perkin Elmer Co., Ltd.) was used, and 5 mg of the sample was heated under nitrogen stream at a heating rate of 20 ° C. / It is measured from room temperature in minutes, and the endothermic peak temperature associated with melting is taken as the melting point.
(4)平均空孔径及び見掛け空孔率 サンプル表面の走査型電子顕微鏡(SEM)観察により各
孔の面積を算出し、その平均値(Sab)、総和(Sδ)
より次式により算出する。(4) Average Pore Diameter and Apparent Porosity The area of each hole was calculated by observing the sample surface with a scanning electron microscope (SEM), and the average value (Sab) and sum (Sδ) were calculated.
It is calculated by the following formula.
空孔率(%)=Sδ/S×100 (ただし、Sは観測している面積) また、フィルム中層部の平均空孔径は、フィルムを液体
窒素温度に凍結した後、厚み方向中央部をスライスし、
そのスライス面を上記方法にて観察、計算した。 Porosity (%) = Sδ / S × 100 (where S is the observed area) The average porosity of the middle layer of the film is determined by slicing the center in the thickness direction after freezing the film to liquid nitrogen temperature. Then
The sliced surface was observed and calculated by the above method.
(5)流動パラフィン透過時間 サンプル及び流動パラフィンを25℃、50%湿度雰囲気に
24時間保持後、サンプルを水平面に置き、サンプル上5
〜20mmの高さより流動パラフィン0.03〜0.06gを自然落
下させる。(5) Liquid paraffin permeation time Samples and liquid paraffin were placed in an atmosphere of 25 ° C and 50% humidity.
After holding for 24 hours, place the sample on a horizontal surface and
Liquid paraffin 0.03 to 0.06 g is dropped naturally from a height of ~ 20 mm.
このとき流動パラフィンがサンプル面に接した時より、
サンプルを透過し反対面を湿すまでの時間を測定し流動
パラフィン透過時間(sec)とする。At this time, when the liquid paraffin touches the sample surface,
The time taken to permeate the sample and wet the opposite surface is measured and used as the liquid paraffin permeation time (sec).
流動パラフィンは、JIS K 9003に規定された、37.8℃に
おける粘度が77±1センチストークスのものを用いる。The liquid paraffin used has a viscosity of 77 ± 1 centistokes at 37.8 ° C specified in JIS K 9003.
試料に流動パラフィンを滴下し、反対面を湿すまでの時
間を流動パラフィン透過時間(秒)とする。Liquid paraffin is dropped on the sample, and the time until the opposite surface is wetted is defined as the liquid paraffin permeation time (second).
(6)空孔率(Pr) 試料(10cm×10cm)を流動パラフィンに24時間浸漬し、
表層の流動パラフィンを十分に拭き取った後の重量
(W2)を測定し、該試料の浸漬前の重量(W1)及び流動
パラフィンの密度(ρ)より空孔体積(V0)を次式によ
り求める。(6) Porosity (Pr) A sample (10 cm x 10 cm) was immersed in liquid paraffin for 24 hours,
The weight (W 2 ) of the surface layer after the liquid paraffin was sufficiently wiped off was measured, and the pore volume (V 0 ) was calculated from the weight (W 1 ) of the sample before immersion and the density (ρ) of the liquid paraffin as follows. Ask by.
V0=(W2−W1)/ρ 空孔率(Pr)は、見掛け体積(厚み、寸法より計算され
る値)Vと空孔体積V0より次の式により計算される。V 0 = (W 2 −W 1 ) / ρ Porosity (P r ) is calculated from the apparent volume (value calculated from thickness and dimensions) V and the pore volume V 0 by the following formula.
Pr=V0/V×100(%) (7)等価直列抵抗(ESR) 特開昭61-187221号に記載された方法に基づき、γブチ
ロラクトンにトリエチルアミンとフタル酸を溶解し、3.
1mS/cmの電解液を用意した。この電解液中での微孔性フ
ィルムの1kHでの直流抵抗成分をESR(Ω)とした。P r = V 0 / V × 100 (%) (7) Equivalent series resistance (ESR) Triethylamine and phthalic acid were dissolved in γ-butyrolactone according to the method described in JP-A-61-187221, and 3.
An electrolytic solution of 1 mS / cm was prepared. The direct current resistance component at 1 kH of the microporous film in this electrolytic solution was defined as ESR (Ω).
ここで、比較サンプルとして、電解コンデンサ紙(マニ
ラ紙MER2.5 50)の値(2.0Ω)を基準とし、1.7Ω以下
を○、1.8〜2.2Ωを△、2.3Ω以上をXとした。Here, as a comparative sample, the value (2.0Ω) of electrolytic capacitor paper (Manila paper MER2.5 50) was used as a reference, and 1.7Ω or less was ◯, 1.8 to 2.2Ω was Δ, and 2.3Ω or more was X.
なお、測定条件は次の通りであった。The measurement conditions were as follows.
(a)電極:白金電極(25mm角) 測定荷重240g (b)インピーダンス測定機: AG−4311 LCR METER (安藤電気(株)製) 測定条件:1kH、5Vレンジ (8)電解コンデンサ試験 220μF、6.3WVの電解コンデンサ素子を30個作製し、重
量及びESRの製造直後の値(W1,R1)と105℃、500時間
後での値(W2,R2)を測定し、変化率(ΔW、ΔR)を
測定した。(A) Electrode: Platinum electrode (25mm square) Measuring load 240g (b) Impedance measuring machine: AG-4311 LCR METER (manufactured by Ando Electric Co., Ltd.) Measuring condition: 1kH, 5V range (8) Electrolytic capacitor test 220μF, 6.3 We fabricated 30 WV electrolytic capacitor elements, measured the weight and ESR values immediately after manufacturing (W 1 , R 1 ) and the values after 500 hours at 105 ° C (W 2 , R 2 ) and measured the change rate ( ΔW, ΔR) was measured.
ΔW及びΔRは次式により算出した。ΔW and ΔR were calculated by the following equations.
ΔW(%)=(W2−W1)/W1×100 ΔR(%)=(R2−R1)/R1×100 [発明の実施例] 次にこの発明の実施例及び比較例を示し、この発明の効
果を具体的に説明する。ΔW (%) = (W 2 −W 1 ) / W 1 × 100 ΔR (%) = (R 2 −R 1 ) / R 1 × 100 [Examples of the invention] Examples and comparative examples of the present invention The effect of the present invention will be specifically described.
実施例1 ポリオレフィン樹脂としてポピプロピレンパウダー(三
井東圧化学株式会社製、EBタイプ)40重量%及びジシク
ロヘキシルフタレート(DCHP,大阪有機化学工業株式会
社製)60重量%とのブレンド物を40mm押出機を用いてT
ダイより溶融押出しし、水槽に導き冷却固化した。Example 1 As a polyolefin resin, a 40 mm extruder was used to prepare a blend of 40 wt% popipropylene powder (EB type, manufactured by Mitsui Toatsu Chemicals, Inc.) and 60 wt% dicyclohexyl phthalate (DCHP, manufactured by Osaka Organic Chemical Industry, Ltd.). Using T
It was melt-extruded from a die, introduced into a water tank, and solidified by cooling.
次に、このキャストフィルムを1−1−1−トリクロル
エタン抽出槽に導いて抽出を行ない、引き続き、ロール
延伸装置を用いて130℃にて3.5倍に延伸した。延伸時に
は、低速ロール及び高速ロール上でフィルムを5kg/cmの
線圧でニップした。次に長手方向に5%のリラックスを
許しながら150℃にて熱固定を行ない、厚み30μmのフ
ィルムを得た。Next, this cast film was introduced into a 1-1-1-trichloroethane extraction tank for extraction, and subsequently stretched 3.5 times at 130 ° C. using a roll stretching device. During stretching, the film was nipped on a low speed roll and a high speed roll at a linear pressure of 5 kg / cm. Next, while allowing 5% relaxation in the longitudinal direction, heat setting was performed at 150 ° C. to obtain a film having a thickness of 30 μm.
このようにして得られたフィルムの特性を下記表に示す
が、全体の平均空孔率が65%と大きい割に表面の空孔率
が38%と低いため、電解液の保持性が高温まで良好であ
り、重量減少が少なく耐ドライアップ性に優れることが
わかる。The properties of the film thus obtained are shown in the table below. The overall average porosity is 65%, but the surface porosity is as low as 38%, so the electrolyte retention is high up to a high temperature. It can be seen that it is good, has little weight loss, and is excellent in dry-up resistance.
比較例1 実施例1において、抽出したフィルムを延伸する前に、
140℃の鏡面加圧ロールで強くニップすることにより、
下記の特性を有するフィルムを得た。Comparative Example 1 In Example 1, before stretching the extracted film,
By strongly nipping with a 140 ° C mirror surface pressure roll,
A film having the following characteristics was obtained.
このようにして得られたフィルムは、全体での空孔率は
60%と大きいものの表面の空孔率が8%と低く、流動パ
ラフィン透過時間が6秒と遅く、ESRの点で劣ってい
た。又、電解コンデンサ試験でのESR変化が小さくなっ
ているのはもともとの初期ESRが著しく大きいためであ
る。The film thus obtained has an overall porosity of
Although it was as large as 60%, the porosity of the surface was as low as 8%, the liquid paraffin permeation time was as slow as 6 seconds, and the ESR was inferior. Also, the reason why the ESR change in the electrolytic capacitor test is small is that the original initial ESR is extremely large.
比較例2 ポリプロピレン樹脂としてポリプロピレンペレット(三
井東圧化学株式会社製、JSタイプ)を220℃にてTダイ
より溶融押出しし、ドラフト比50にてキャスティングド
ラム上で冷却固化し巻きとった。次に該キャストフィル
ムを150℃にて2分間の熱処理をした。こうして得られ
たフィルムは、特公昭50-2176に記載の弾性回復率が92
%であった。次に該熱処理フィルムを80℃にて長手方向
に延伸速度100%/分にて2倍に延伸し、さらに140℃に
て5分熱処理し巻きとった。Comparative Example 2 Polypropylene pellets (JS type, manufactured by Mitsui Toatsu Chemicals, Inc.) as a polypropylene resin were melt extruded from a T die at 220 ° C., cooled and solidified on a casting drum at a draft ratio of 50, and wound. Next, the cast film was heat-treated at 150 ° C. for 2 minutes. The film thus obtained has an elastic recovery rate of 92 as described in Japanese Examined Patent Publication No. 50-2176.
%Met. Next, the heat-treated film was stretched twice at 80 ° C. in the longitudinal direction at a stretching rate of 100% / min, further heat-treated at 140 ° C. for 5 minutes and wound.
こうして得られたフィルムは、厚みが25μmであり、表
に示すように空孔率は表面、全層いずれもほぼ等しく32
〜35%と低く、ESRも大きいばかりか電解コンデンサで
の経時変化も大きい。The film thus obtained had a thickness of 25 μm, and as shown in the table, the porosity was almost the same on both the surface and all layers.
It is as low as ~ 35% and not only has a large ESR but also has a large change over time in electrolytic capacitors.
Claims (2)
ィルム全体の平均空孔率が50%から85%、流動パラフィ
ン透過時間が5秒以下であり、かつ、フィルム中層部の
平均空孔径が0.05μmから5μmで表面での見掛けの平
均空孔径が0.01μmから4μmであるポリオレフィン系
微孔性フィルム。1. An apparent porosity on the surface of 10% to 45%, an average porosity of the entire film of 50% to 85%, a liquid paraffin permeation time of 5 seconds or less, and an intermediate layer of the film. A polyolefin microporous film having an average pore diameter of 0.05 μm to 5 μm and an apparent average pore diameter on the surface of 0.01 μm to 4 μm.
ィルム全体の平均空孔率が50%から85%、流動パラフィ
ン透過時間が5秒以下であり、かつ、フィルム中層部の
平均空孔径が0.05μmから5μmで表面での見掛けの平
均空孔径が0.01μmから4μmであるポリオレフィン系
微孔性フィルムから成る電解液セパレータ。2. The apparent porosity on the surface is 10% to 45%, the average porosity of the entire film is 50% to 85%, the liquid paraffin permeation time is 5 seconds or less, and An electrolytic solution separator comprising a polyolefin microporous film having an average pore diameter of 0.05 μm to 5 μm and an apparent average pore diameter on the surface of 0.01 μm to 4 μm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62167456A JPH0778145B2 (en) | 1987-07-04 | 1987-07-04 | Polyolefin microporous film and electrolytic solution separator comprising the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62167456A JPH0778145B2 (en) | 1987-07-04 | 1987-07-04 | Polyolefin microporous film and electrolytic solution separator comprising the same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6411140A JPS6411140A (en) | 1989-01-13 |
| JPH0778145B2 true JPH0778145B2 (en) | 1995-08-23 |
Family
ID=15850020
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62167456A Expired - Lifetime JPH0778145B2 (en) | 1987-07-04 | 1987-07-04 | Polyolefin microporous film and electrolytic solution separator comprising the same |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0778145B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112768764B (en) * | 2021-01-08 | 2022-06-24 | 上海恩捷新材料科技有限公司 | High-strength solid electrolyte membrane |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1412983A (en) * | 1971-11-30 | 1975-11-05 | Debell & Richardson | Method of producing porous plastic materials |
-
1987
- 1987-07-04 JP JP62167456A patent/JPH0778145B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6411140A (en) | 1989-01-13 |
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