JPH01203439A - Porous film and production thereof - Google Patents

Porous film and production thereof

Info

Publication number
JPH01203439A
JPH01203439A JP2653088A JP2653088A JPH01203439A JP H01203439 A JPH01203439 A JP H01203439A JP 2653088 A JP2653088 A JP 2653088A JP 2653088 A JP2653088 A JP 2653088A JP H01203439 A JPH01203439 A JP H01203439A
Authority
JP
Japan
Prior art keywords
film
magnesium hydroxide
fatty acid
porous film
weight
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2653088A
Other languages
Japanese (ja)
Inventor
Junko Hayakawa
早川 淳子
Michiyasu Ito
伊藤 道康
Jiyuuichi Tsuji
従一 辻
Hisatoshi Suzuki
鈴木 久利
Tae Tanaka
田中 多栄
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.)
Mitsui Toatsu Chemicals Inc
Original Assignee
Mitsui Toatsu Chemicals Inc
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 Mitsui Toatsu Chemicals Inc filed Critical Mitsui Toatsu Chemicals Inc
Priority to JP2653088A priority Critical patent/JPH01203439A/en
Publication of JPH01203439A publication Critical patent/JPH01203439A/en
Pending legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Abstract

PURPOSE:To obtain the present film, excellent in moisture and air permeability, water resistance and flexibility and suitable as rain apparels, disposable diapers, packaging materials, etc., by blending a polyolefinic resin with specific magnesium hydroxide, melt forming a film and drawing the resultant film. CONSTITUTION:The aimed film obtained by blending (A) 100pts.wt. polyolefinic resin with (B) 50-400pts.wt., preferably 60-200pts.wt. magnesium hydroxide, having 0.3-2.0mum, preferably 0.5-1.0mum average particle diameter and <=10m<2>/g, preferably 0.5-5.0m<2>/g specific surface area and subjected to surface treatment, then melt forming a film and drawing the resultant film in at least an uniaxial direction at >=1.1 times.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、多孔性フィルム及びその製造方法に関し、さ
らに詳しくは、ポリオレフィン系樹脂と表面処理を施し
た水酸化マグネシウムからなる多孔性フィルム及びその
製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a porous film and a method for producing the same, and more specifically to a porous film made of a polyolefin resin and surface-treated magnesium hydroxide, and its production method. This relates to a manufacturing method.

〔従来技術〕[Prior art]

従来よりポリオレフィン系樹脂に、有機または無機の非
相溶性物質を特定の割合で配合した後、公知の方法で溶
融製膜し、次いで延伸加工して得られた多孔性フィルム
は知られている。
BACKGROUND ART Porous films obtained by blending a polyolefin resin with an organic or inorganic incompatible substance in a specific ratio, melting the film by a known method, and then stretching the film have been known.

しかしながら、ポリオレフィン系樹脂と非相溶性物質と
して炭酸カルシウムを使用した場合、粒子同志の凝集及
び粒度分布が広いために、粗大粒子が存在することから
、延伸による応力が凝集体あるいは粗大粒子に集中する
ため、低倍率で延伸切れをおこしやすく、薄いフィルム
を得ることは困難であった。また、たとえ延伸切れをお
こさなくても孔径が0.1au+以上の穴となって、耐
水圧が低下し、多孔性フィルムとしての機能が劣ったも
のとなる。また、剛性があり過ぎてパサパサしたフィル
ムになることなどの欠点があった。
However, when calcium carbonate is used as a substance incompatible with polyolefin resin, the stress due to stretching is concentrated on the aggregates or coarse particles due to the presence of coarse particles due to the agglomeration of particles and the wide particle size distribution. Therefore, stretch breakage easily occurs at low magnification, making it difficult to obtain a thin film. Further, even if no stretching breakage occurs, holes with a pore diameter of 0.1 au+ or more are formed, resulting in a decrease in water pressure resistance and poor functionality as a porous film. In addition, there was a drawback that the film was too rigid and dry.

柔軟性を改良し、低倍率で均一多孔化するために、ポリ
オレフィン系樹脂と充填剤に、さらに液状の化合物を添
加する方法が開発され、例えば、液状の化合物として、
液状ポリブタジェンや液状ポリブテン(特開昭57−4
7334号公報)、液状のポリヒドロキシ飽和炭化水素
(特開昭57−203520号公報)、液状ポリイソプ
レンゴム(特開昭58−149925号公報)あるいは
ポリヒドロキシ飽和炭化水素およびエポキシ基含有有機
化合物(特開昭59−140235号公報)を添加して
いる。
In order to improve flexibility and create uniform porosity at low magnification, a method has been developed in which a liquid compound is added to the polyolefin resin and filler.For example, as a liquid compound,
Liquid polybutadiene and liquid polybutene (JP-A-57-4
7334), liquid polyhydroxy saturated hydrocarbon (JP-A-57-203520), liquid polyisoprene rubber (JP-A-58-149925), or polyhydroxy saturated hydrocarbon and epoxy group-containing organic compound (JP-A-58-149925). JP-A-59-140235) is added.

しかし、これらの添加剤は多量に配合しないと均一多孔
化しなかったり、溶剤や薬品に接触すると溶出してしま
う問題があった。
However, these additives have the problem of not forming uniform pores unless they are blended in large amounts, or of eluting when they come into contact with solvents or chemicals.

また、これらの液状の化合物を添加すると、充填剤とポ
リオレフィン樹脂マトリックスとの界面剥離がおきにく
くなり、通気性及び透湿性が低下する問題があった。
Further, when these liquid compounds are added, interfacial peeling between the filler and the polyolefin resin matrix becomes difficult to occur, resulting in a problem that air permeability and moisture permeability are reduced.

これら液状添加剤について更に改良されており、例えば
、特開昭62−129321号公報ではシリコーン油の
使用が提案されているが、やはり上記した添加剤と同様
に液状であるため浮き出しによる表面のベタツキが避け
られないという問題があった。
These liquid additives have been further improved; for example, JP-A-62-129321 proposes the use of silicone oil, but since it is also liquid like the above-mentioned additives, it does not cause stickiness on the surface due to embossment. The problem was that it was unavoidable.

上記ベタツキなどの欠点を補い、添加剤を含まないもの
として、例えば、非相溶性物質に粗粒子部と細粒子部の
二つの粒子部からなる炭酸カルシウムの使用が提案され
ている(特開昭62−201941号公報)が、粒子の
取り扱いが困難であり、また、二つの粒子部を均一に分
散するのが困難となるために得られたフィルムの通気性
にむらが生じるとしいう欠点があった。
To compensate for the above-mentioned disadvantages such as stickiness and do not contain additives, it has been proposed to use calcium carbonate, which is composed of two particle parts, a coarse particle part and a fine particle part, as an incompatible substance (Japanese Patent Application Laid-open No. 62-201941), but it has the disadvantage that the particles are difficult to handle and that the air permeability of the obtained film is uneven because it is difficult to uniformly disperse the two particle parts. Ta.

同様に、添加剤を含まないものとして、では非相溶性物
質として硫酸バリウムを使用することが提示されている
(特開昭60−129240号公報)。このものは延伸
性がよく、高い透湿性と均一で微細な孔径をもち、かつ
柔軟性に優れ、延伸方向の物性強度が高い等の特徴を有
し、さらに、特に大きい粒子は存在しないため、厚みの
薄いフィルムが得られている。
Similarly, it has been proposed that barium sulfate is used as an incompatible substance without additives (Japanese Patent Application Laid-open No. 129240/1982). This material has characteristics such as good stretchability, high moisture permeability, uniform and fine pore size, excellent flexibility, and high physical strength in the direction of stretching.Furthermore, since there are no particularly large particles, A thin film is obtained.

しかし、硫酸バリウムは比重が大きいために、得られた
多孔性フィルムは比重が高く、坪量当たり20g/rr
f以下のフィルムが工業的には安定して得られないとい
う問題点を有している。
However, since barium sulfate has a high specific gravity, the resulting porous film has a high specific gravity of 20 g/rr per basis weight.
There is a problem that a film having a diameter of f or less cannot be stably obtained industrially.

また、硫酸バリウムのモース硬度は3.0〜3.8と高
いために押出機のシリンダ一部が摩耗しやすいという問
題点を有している。
In addition, barium sulfate has a high Mohs hardness of 3.0 to 3.8, which poses a problem in that a part of the cylinder of the extruder is easily worn out.

ポリオレフィン系樹脂と非相溶性物質から得られる多孔
性フィルム及びその製造法については種々の検討が行わ
れているが、多孔性フィルムの成形性及び品質等の特性
について上記に示すような問題点、欠点を有している。
Various studies have been conducted on porous films obtained from substances incompatible with polyolefin resins and their manufacturing methods, but there are problems with the properties such as moldability and quality of porous films, as shown above. It has its drawbacks.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

本発明の課題は液状の化合物を含まず、ポリオレフィン
系樹脂からなる、引張物性、透湿性、通気性、生産安定
性に優れ、厚みが薄く、低坪量が可能な多孔性フィルム
を提供することにある。
An object of the present invention is to provide a porous film that does not contain liquid compounds and is made of polyolefin resin, has excellent tensile properties, moisture permeability, air permeability, and production stability, and is thin in thickness and can be produced with a low basis weight. It is in.

〔課題を解決するための手段〕[Means to solve the problem]

本発明者らは、上記課題を達成するため、鋭意検討し、
遂に本発明に到った。
In order to achieve the above-mentioned problem, the present inventors have made extensive studies,
We have finally arrived at the present invention.

すなわち、本発明はポリオレフィン系樹脂100重量部
と、平均粒径が0.3〜2.0μ麟、比表面積が10r
rr/g以下であり、かつ表面処理を施した水酸化マグ
ネシウム50〜400重量部とからなる樹脂組成物を溶
融製膜した後、少なくとも一軸方向に1.1倍以上延伸
したものであることを特徴とする多孔性フィルム及びそ
の製造方法である。
That is, the present invention uses 100 parts by weight of a polyolefin resin, an average particle size of 0.3 to 2.0 μm, and a specific surface area of 10 μm.
rr/g or less, and a resin composition consisting of 50 to 400 parts by weight of surface-treated magnesium hydroxide is melt-formed into a film and then stretched at least 1.1 times in one axis direction. The present invention provides a porous film and a method for producing the same.

以下、本発明の詳細な説明する。The present invention will be explained in detail below.

本発明におけるポリオレフィン系樹脂とは、ポリプロピ
レン(PP)、低密度ポリエチレン(LDPE)、高密
度ポリエチレン(■叶E)、線状低密度ポリエチレン(
L−LDPE)、ポリブテン等のホモ重合体、エチレン
−プロピレン共重合体、エチレン−ブチレン共重合体、
エチレン−酢酸ビニル共重合体等の共重合体、および、
これらのブレンド物である。
In the present invention, polyolefin resins include polypropylene (PP), low density polyethylene (LDPE), high density polyethylene (■Ko E), linear low density polyethylene (
L-LDPE), homopolymers such as polybutene, ethylene-propylene copolymers, ethylene-butylene copolymers,
Copolymers such as ethylene-vinyl acetate copolymers, and
It is a blend of these.

線状低密度ポリエチレンとは、エチレン−α−オレフィ
ン共重合体の一種であり、ここに共重合するα−オレフ
ィンとしてはブテン−1,4−メチルペンテン−1,ヘ
キセン−I、オクテン−1,デセン−1、ドデセン−1
などがある。
Linear low density polyethylene is a type of ethylene-α-olefin copolymer, and the α-olefins copolymerized here include butene-1,4-methylpentene-1, hexene-I, octene-1, Decene-1, Dodecene-1
and so on.

本発明における水酸化マグネシウムとしては、平均粒径
0.3〜2.0μm、好ましくは0.5〜1.0μ−の
ものが適当である。
Suitable magnesium hydroxide in the present invention has an average particle size of 0.3 to 2.0 μm, preferably 0.5 to 1.0 μm.

平均粒径が0.3μ−未満のものは良好な多孔性フィル
ムが得られず、逆に2.0μ−より大きいものでは延伸
切れを起こすなどフィルムの延伸性が悪く、孔径が大き
くなり、多孔性フィルムとしての機能が劣ったものとな
る。
If the average particle size is less than 0.3μ, it will not be possible to obtain a good porous film, and if it is larger than 2.0μ, the film will have poor stretchability, such as breakage, and the pore size will become large. The function as a sex film becomes inferior.

また、比表面積は10nf/g以下であり、0.5〜5
.0m2/gの範囲がより好ましい。
In addition, the specific surface area is 10nf/g or less, and 0.5 to 5
.. A range of 0 m2/g is more preferable.

比表面積が1Onl/gを越えると、水酸化マグネシウ
ムの形状が無定型、板状などとなるので粒径分布が広く
なり、フィルムの延伸性が低下し、フィルムの多孔化が
達成できない。
When the specific surface area exceeds 1 Onl/g, the shape of magnesium hydroxide becomes amorphous, plate-like, etc., resulting in a wide particle size distribution, resulting in a decrease in film stretchability and failure to make the film porous.

なお、本発明で使用する水酸化マグネシウムは、特開昭
60−176918号公報に記載された製造方法により
容易に製造され、この製造方法で製造されたものが好ま
しい。
Incidentally, the magnesium hydroxide used in the present invention can be easily manufactured by the manufacturing method described in JP-A-60-176918, and those manufactured by this manufacturing method are preferred.

本発明では上記した水酸化マグネシウムを表面処理して
おくことが必須であり、表面処理を施さない水酸化マグ
ネシウムを用いた場合は、水酸化マグネシウムの凝集が
生じ、分散性が劣る。そのため均一白化せず、また延伸
性が著しく低下する。
In the present invention, it is essential to surface-treat the above-mentioned magnesium hydroxide, and when magnesium hydroxide without surface treatment is used, agglomeration of magnesium hydroxide occurs, resulting in poor dispersibility. Therefore, uniform whitening is not achieved and the stretchability is significantly reduced.

表面処理を施した水酸化マグネシウムの使用量は、ポリ
オレフィン系樹脂100重量部当たり50〜400重量
部であり、好ましくは60〜200重量部である。この
使用量が50重量部未満では、多孔化が不充分で連通孔
が少なくなるため、充分な通気性及び透湿性が得られず
、400重量部を越えて用いた場合はフィルムの剛性が
増し、シート状物の成形および延伸性が低下する。
The amount of surface-treated magnesium hydroxide used is 50 to 400 parts by weight, preferably 60 to 200 parts by weight, per 100 parts by weight of the polyolefin resin. If the amount used is less than 50 parts by weight, the porosity will be insufficient and the number of communicating pores will be reduced, making it impossible to obtain sufficient air permeability and moisture permeability. If it is used in excess of 400 parts by weight, the rigidity of the film will increase. , the forming and stretching properties of the sheet-like material are reduced.

本発明で使用する表面処理剤としては、脂肪酸、脂肪酸
金属塩及び脂肪酸アミドが適当であり、特に常温で固体
状となるものが好ましい。脂肪酸、脂肪酸金属塩や脂肪
酸アミドとして、ステアリン酸、ステアリン酸ナトリウ
ム、ステアリン酸カルシウム、パルミチン酸、パルミチ
ン酸ナトリウム、パルミチン酸カルシウム、ミリスチン
酸、ミリスチン酸ナトリウム、ミリスチン酸カルシウム
、ラウリン酸、ラウリン酸ナトリウム、ラウリン酸カル
シウム、オレイン酸、オレイン酸ナトリウム、オレイン
酸カルシウム、ステアリン酸アミド、オレイン酸アミド
等が例示され、特に、ステアリン酸ナトリウム、パルミ
チン酸ナトリウム、ミリスチン酸ナトリウム、ラウリン
酸ナトリウム、オレイン酸ナトリウムが好適である。
As the surface treatment agent used in the present invention, fatty acids, fatty acid metal salts, and fatty acid amides are suitable, and those that are solid at room temperature are particularly preferred. Fatty acids, fatty acid metal salts, and fatty acid amides include stearic acid, sodium stearate, calcium stearate, palmitic acid, sodium palmitate, calcium palmitate, myristic acid, sodium myristate, calcium myristate, lauric acid, sodium laurate, and lauric acid. Examples include calcium phosphate, oleic acid, sodium oleate, calcium oleate, stearamide, oleic acid amide, and particularly preferred are sodium stearate, sodium palmitate, sodium myristate, sodium laurate, and sodium oleate. .

表面処理を施した水酸化マグネシウムは、例えば塩化マ
グネシウム水溶液に水酸化カルシウムを加えて反応させ
、生成物を熟成して水酸化マグネシウムを生成沈澱させ
る。次いで、濾過、水洗した沈澱物に、脂肪酸金属塩の
水溶液を加え、表面に展着した後、蒸発乾固し、微粉砕
することによって得られる。または、脂肪酸、脂肪酸金
属塩または脂肪酸アミドと水酸化マグネシウムを所定量
で配合し、ヘンシェルミキサーで混合し、水酸化マグネ
シウムの表面に展着させることによって得られる。
The surface-treated magnesium hydroxide is prepared by adding calcium hydroxide to an aqueous magnesium chloride solution and causing the reaction, and the product is aged to produce and precipitate magnesium hydroxide. Next, an aqueous solution of a fatty acid metal salt is added to the filtered and water-washed precipitate, spread on the surface, evaporated to dryness, and finely pulverized. Alternatively, it can be obtained by blending a predetermined amount of fatty acid, fatty acid metal salt, or fatty acid amide with magnesium hydroxide, mixing with a Henschel mixer, and spreading the mixture on the surface of magnesium hydroxide.

脂肪酸、脂肪酸金属塩または脂肪酸アミドは水酸化マグ
ネシウムに対して10重量%以下使用するのが好ましく
、さらに2〜5重量%が好ましい。
The fatty acid, fatty acid metal salt, or fatty acid amide is preferably used in an amount of 10% by weight or less, more preferably 2 to 5% by weight, based on magnesium hydroxide.

また、本発明の効果を妨げない範囲で、M機充填剤とし
て表面処理を施した水酸化マグネシウムの他に硫酸バリ
ウム、炭酸カルシウム等の他の無機充填剤を添加しても
よい。
Furthermore, other inorganic fillers such as barium sulfate and calcium carbonate may be added as the M filler in addition to the surface-treated magnesium hydroxide, within a range that does not impede the effects of the present invention.

なお、ポリオレフィン系樹脂には常法に従い熱安定剤、
紫外線安定剤、帯電防止剤、顔料、螢光剤等を添加して
も差し支えない。
In addition, heat stabilizers, heat stabilizers, and
There is no problem in adding ultraviolet stabilizers, antistatic agents, pigments, fluorescent agents, etc.

次に、本発明の多孔性フィルムの製造方法を説明する。Next, a method for manufacturing a porous film of the present invention will be explained.

まず、ポリオレフィン系樹脂に表面処理を施した水酸化
マグネシウムを他の添加剤と共に添加した後、ヘンシェ
ルミキサー、スーパーミキサー、タンブラ−型混合機を
用いて混合し、その後通常の一軸あるいは二軸スクリュ
ー押出機によって混練し、ペレット化する。
First, surface-treated magnesium hydroxide is added to polyolefin resin along with other additives, and then mixed using a Henschel mixer, super mixer, or tumbler type mixer, and then subjected to conventional single or twin screw extrusion. Knead and pelletize using a machine.

次いで、これらのペレットをインフレーション成形機ま
たは、Tダイ成形機を用いて製膜する。
Next, these pellets are formed into a film using an inflation molding machine or a T-die molding machine.

この際に、ペレット化せず直接押出機で成形することも
できる。
At this time, it is also possible to directly mold using an extruder without pelletizing.

その後、少なくとも一軸方向に、1.1倍以上延伸を行
う。延伸は多段階に分けて行ってもよいし、二軸方向に
延伸してもよい。
Thereafter, stretching is performed at least 1.1 times in at least one axis direction. Stretching may be performed in multiple stages or biaxially.

延伸倍率が1.1倍未満の場合は、フィルムの多孔化が
不充分となる。
If the stretching ratio is less than 1.1 times, the film will not be sufficiently porous.

また、延伸後、孔の形態安定性を増すために熱固定を行
ってもよい。
Further, after stretching, heat setting may be performed to increase the morphological stability of the holes.

上記多孔性フィルムの印刷性や接着性を改良する目的の
ために、コロナ放電処理等の表面処理を行うこともでき
る。
In order to improve the printability and adhesion of the porous film, surface treatment such as corona discharge treatment can also be performed.

通気性は、表面処理を施した水酸化マグネシウムの使用
量、粒径、延伸倍率等によって決まるが、水酸化マグネ
シウムは酸化マグネシウムと水に熱分解されるので、得
られたシート状物には溶融製膜時生成した水の発泡によ
る微小な空洞ができ、延伸による多孔化、連通化が助長
され通気性および透湿性がよ(なる特徴を有している。
Air permeability is determined by the amount of surface-treated magnesium hydroxide used, particle size, stretching ratio, etc., but since magnesium hydroxide is thermally decomposed into magnesium oxide and water, the resulting sheet material has no melting properties. Microscopic cavities are created by the foaming of water generated during membrane formation, and the stretching facilitates porosity and communication, resulting in improved air permeability and moisture permeability.

〔実施例〕〔Example〕

以下、実施例により本発明を説明する。 The present invention will be explained below with reference to Examples.

なお、この実施例で用いたフィルムの物性評価方法は以
下の通りである。
The method for evaluating the physical properties of the film used in this example is as follows.

(1)強度:25mm(巾) x 100mm (長さ
)のフィルムを引張りスピード200ma+/sinで
テンシロン引張り試験機にて破断時強度 をMD(流れ方向)、TD(流れに垂 直な方向)について各々測定した。
(1) Strength: A film of 25 mm (width) x 100 mm (length) was pulled at a tensile speed of 200 ma+/sin using a Tensilon tensile tester, and the strength at break was measured in MD (machine direction) and TD (perpendicular to the flow direction), respectively. It was measured.

(2)透湿度: ASTM E96−66(D)に準じ
て測定した。
(2) Moisture permeability: Measured according to ASTM E96-66(D).

(3)穴:孔径が0.1.cIm以上の孔数を測定した
(3) Hole: Hole diameter is 0.1. The number of pores of cIm or more was measured.

実施例1〜6、比較例1〜9 旧=2.0、ρ= 0.92の線状低密度ポリエチレン
(し−シ叶E) 100重量部に表−1に示す充填剤を
表−1に示す量を添加し、ヘンシェルミキサーで混合し
、二輪スクリュー押出機を用いてペレット化した後、T
ダイ成形機によって押し出し、表−2に示す延伸倍率で
延伸した後の多孔性フィルムの厚みになるように、それ
ぞれ製膜した。
Examples 1 to 6, Comparative Examples 1 to 9 100 parts by weight of linear low density polyethylene with old = 2.0 and ρ = 0.92 (Shishiko E) was added with the fillers shown in Table 1. T
Each of the porous films was extruded using a die molding machine and stretched at the stretching ratio shown in Table 2 to have the thickness of the porous film.

次いで、80°Cで、表−2に示す延伸倍率で、−軸ま
たは二輪方向に延伸し、多孔性フィルムを得た。
Next, the film was stretched at 80°C in the -axis or two-wheel direction at the stretching ratio shown in Table 2 to obtain a porous film.

得られたフィルムについて上記に示す物性を測定し、そ
の結果を表−2に示した。
The physical properties shown above were measured for the obtained film, and the results are shown in Table 2.

なお、比較例7ではペレット化ができず、また、比較例
2.6.8および9では延伸を試みたが延伸切れが多く
、多孔性フィルムが得られなかった。
In Comparative Example 7, it was not possible to pelletize, and in Comparative Examples 2, 6, 8, and 9, stretching was attempted, but there were many stretching breaks, and a porous film could not be obtained.

実施例7.8 線状低密度ポリエチレン(L−LDPE)の代わりに、
実施例7では、MI= 2.0、ρ= 0.92の低密
度ポリエチレン(LDPE)と、MI= 2.0、ρ=
 0.96の高密度ポリエチレン(HOPE)を、実施
例8では、旧=2.0、ρ= 0.92の線状低密度ポ
リエチレン(L−LDPEりと、III= 1.5、ρ
= 0.90のポリプロピレン(PP)をそれぞれ3ニ
アの割合で用いた以外は、実施例2と同様の方法で多孔
性フィルムを得た。
Example 7.8 Instead of linear low density polyethylene (L-LDPE),
In Example 7, low density polyethylene (LDPE) with MI = 2.0, ρ = 0.92 and low density polyethylene (LDPE) with MI = 2.0, ρ =
In Example 8, high-density polyethylene (HOPE) of 0.96 was replaced with linear low-density polyethylene (L-LDPE Rito, III = 1.5, ρ) of
A porous film was obtained in the same manner as in Example 2, except that polypropylene (PP) of 0.90 was used at a ratio of 3 nia.

得られたフィルムの物性測定結果を表−2に示〔発明の
効果〕 実施例からも明らかなように、充填剤として平均粒径が
0.3〜2.0μm、比表面積がIOm/g以下である
表面処理を施した水酸化マグネシウムを使用することに
より下記のような効果が得られる。
The results of measuring the physical properties of the obtained film are shown in Table 2. [Effects of the invention] As is clear from the examples, the filler has an average particle diameter of 0.3 to 2.0 μm and a specific surface area of IOm/g or less. By using magnesium hydroxide that has undergone surface treatment, the following effects can be obtained.

(1)硫酸バリウムに比べ、二次凝集が少なく、分散性
が良好であるため、添加量が少なくても、高い透湿性と
均一な孔径分布が得られる。
(1) Compared to barium sulfate, it causes less secondary aggregation and has better dispersibility, so even if the amount added is small, high moisture permeability and uniform pore size distribution can be obtained.

(2)延伸性に優れ、比重も硫酸バリウムに比べ小さい
ために、薄く、かつ坪量の小さい10g/rrf以下の
多孔性フィルムが工業的に安定して得られる。
(2) Since it has excellent stretchability and has a lower specific gravity than barium sulfate, a thin porous film with a basis weight of 10 g/rrf or less can be stably obtained industrially.

(3)押出性についても、水酸化マグネシウムのモース
硬度は2.0〜3.0と小さいので、押出機のシリンダ
ーの摩耗が少なく、装置の長期使用が可能となり、生産
性が向上する。
(3) As for extrudability, since magnesium hydroxide has a small Mohs hardness of 2.0 to 3.0, there is little wear on the cylinder of the extruder, allowing long-term use of the device and improving productivity.

本発明の多孔性フィルムは、透湿性、通気性に富み、か
つ耐水性、柔軟性にも優れており、雨具等の防水衣料、
使い捨てオムツ、衛生材料の防漏フィルム、包装材料、
電池用セパレーター、濾過材料等の用途に適している・ また、その通気性及び透湿性により結露現象ヲ生じない
ため、壁紙及び建材用シートにも適している。
The porous film of the present invention has excellent moisture permeability, air permeability, water resistance, and flexibility, and can be used for waterproof clothing such as rain gear, etc.
Disposable diapers, leak-proof films for sanitary materials, packaging materials,
Suitable for use as battery separators, filtration materials, etc. Also, due to its air permeability and moisture permeability, no condensation occurs, making it suitable for wallpaper and sheets for building materials.

Claims (1)

【特許請求の範囲】 1、ポリオレフィン系樹脂100重量部と、平均粒径が
0.3〜2.0μm、比表面積が10m^2/g以下で
あり、かつ表面処理を施した水酸化マグネシウム50〜
400重量部とからなる樹脂組成物を溶融製膜した後、
少なくとも一軸方向に1.1倍以上延伸したものである
ことを特徴とする多孔性フィルム。 2、表面処理が、脂肪酸、脂肪酸金属塩または脂肪酸ア
ミドによる表面処理である特許請求の範囲第1項記載の
多孔性フィルム。 3、ポリオレフィン系樹脂100重量部と平均粒径が0
.3〜2.0μm、比表面積が10m^2/gであり、
かつ表面処理を施した水酸化マグネシウム50〜400
重量部とを配合し、次いで溶融製膜した後、少なくとも
一軸方向に1.1倍以上延伸することを特徴とする多孔
性フィルムの製造方法。 4、表面処理が、脂肪酸、脂肪酸金属塩または脂肪酸ア
ミドによる表面処理である特許請求の範囲第3項記載の
多孔性フィルムの製造方法。
[Claims] 1. 100 parts by weight of polyolefin resin, 50% magnesium hydroxide having an average particle size of 0.3 to 2.0 μm, a specific surface area of 10 m^2/g or less, and surface-treated. ~
After melting and film-forming a resin composition consisting of 400 parts by weight,
A porous film characterized by being stretched at least 1.1 times in one direction. 2. The porous film according to claim 1, wherein the surface treatment is with a fatty acid, a fatty acid metal salt, or a fatty acid amide. 3. 100 parts by weight of polyolefin resin and an average particle size of 0
.. 3 to 2.0 μm, specific surface area is 10 m^2/g,
and surface-treated magnesium hydroxide 50-400
1. A method for producing a porous film, which comprises blending parts by weight, then melting and forming the film, and then stretching the film by a factor of 1.1 or more in at least one axis. 4. The method for producing a porous film according to claim 3, wherein the surface treatment is surface treatment with a fatty acid, a fatty acid metal salt, or a fatty acid amide.
JP2653088A 1988-02-09 1988-02-09 Porous film and production thereof Pending JPH01203439A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2653088A JPH01203439A (en) 1988-02-09 1988-02-09 Porous film and production thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2653088A JPH01203439A (en) 1988-02-09 1988-02-09 Porous film and production thereof

Publications (1)

Publication Number Publication Date
JPH01203439A true JPH01203439A (en) 1989-08-16

Family

ID=12196037

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2653088A Pending JPH01203439A (en) 1988-02-09 1988-02-09 Porous film and production thereof

Country Status (1)

Country Link
JP (1) JPH01203439A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002030169A (en) * 2000-07-17 2002-01-31 Mitsui Chemicals Inc Porous film
JP2010195898A (en) * 2009-02-24 2010-09-09 Sumitomo Chemical Co Ltd Polyolefin-based resin composition, method for producing porous film by using the composition, porous film, method for producing laminated porous film, laminated porous film, and separator for battery

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002030169A (en) * 2000-07-17 2002-01-31 Mitsui Chemicals Inc Porous film
JP2010195898A (en) * 2009-02-24 2010-09-09 Sumitomo Chemical Co Ltd Polyolefin-based resin composition, method for producing porous film by using the composition, porous film, method for producing laminated porous film, laminated porous film, and separator for battery

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