JPS5968343A - Method for manufacturing breathable film - Google Patents

Method for manufacturing breathable film

Info

Publication number
JPS5968343A
JPS5968343A JP17950082A JP17950082A JPS5968343A JP S5968343 A JPS5968343 A JP S5968343A JP 17950082 A JP17950082 A JP 17950082A JP 17950082 A JP17950082 A JP 17950082A JP S5968343 A JPS5968343 A JP S5968343A
Authority
JP
Japan
Prior art keywords
vinyl chloride
plasticizer
chloride resin
film
breathable film
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.)
Granted
Application number
JP17950082A
Other languages
Japanese (ja)
Other versions
JPH0432857B2 (en
Inventor
Haruaki Kakiya
垣谷 晴昭
Kyoji Yoshida
吉田 恭二
Masakiyo Yuino
結野 正清
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.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Monsanto Chemical Co
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 Mitsubishi Monsanto Chemical Co filed Critical Mitsubishi Monsanto Chemical Co
Priority to JP17950082A priority Critical patent/JPS5968343A/en
Publication of JPS5968343A publication Critical patent/JPS5968343A/en
Publication of JPH0432857B2 publication Critical patent/JPH0432857B2/ja
Granted legal-status Critical Current

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  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Moulding By Coating Moulds (AREA)

Abstract

PURPOSE:To obtain an air-permeable film useful for clothing, packaging, sanitary supplies, etc., by dispersing a vinyl chloride resin obtd. by drying an emulsion-polymerized or a fine suspension-polymerized polymer emulsion or suspension, in water, melting, a coating film of the resulting aq. dispersion by heating and cooling the film. CONSTITUTION:A vinyl chloride resin having an average particle size of 50mu or below obtd. by drying an emulsion-polymerized or a fine suspension-polymerized polymer emulsion or suspension, and a plasticizer are dispersed in water. This dispersion is applied onto a subtrate having a surface release property to form a coating film. Then the film is molten by heating at a temp. not higher than that represented by the formula (wherein Tg is a glass transition point of vinyl chloride resin, and the number of parts of plasticizer added is that of the plasticizer to be added per 100pts.wt. vinyl chloride resin) and cooled to obtain an air-permeable film.

Description

【発明の詳細な説明】 本発明は、通気性フィルムの製造方法に関するものであ
り、更に詳しくは、塩化ビニル系樹脂を基体とした軟質
で通気性あるフィルムを製造する方法に関1゛ろもので
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a breathable film, and more particularly, to a method for producing a soft and breathable film based on a vinyl chloride resin. It is.

塩化ビニル系樹脂を基体として、蓄電池用微孔性セパレ
ーターや擬皮革等を製造1−る技術としては、特公昭、
?9−23g3g号公報、特公昭’IO−!i23乙号
公報、特公昭グ!−5g乙号公報、特公昭’l5−37
g77号公報、特公昭タ乙−25ng号公報、特公昭グ
アー/1.9g’1号公報、特公昭4/−7−グ59 
’% S号公報、特公昭6ユー3.5−703号公報、
特公昭33−//9g7号公報等に記載の方法が提案さ
れ、一部実用化されている。
Techniques for manufacturing microporous separators for storage batteries, pseudo-leather, etc. using vinyl chloride resin as a base include Tokkosho,
? Publication No. 9-23g3g, Special Publication Sho'IO-! i23 No. 2 Publication, Special Public Shogu! -5g Publication No. 1, Special Publication Sho'l5-37
G77 Publication, Special Publication Shota Otsu-25ng Publication, Special Publication Sho Guar/1.9g'1 Publication, Special Publication Showa 4/-7-G59
'% S Publication, Special Publication No. 6 U 3.5-703,
A method described in Japanese Patent Publication No. 33-/9g7 has been proposed, and some of the methods have been put into practical use.

これら既提案の方法のうちで、基体塩化ビニル系樹脂に
多元の可塑剤を配合した組成物を原料とする方法は、特
公昭39−23g!ig号公報、特公昭’70−、t2
3乙号公報に記載の方法がある。
Among these already proposed methods, a method using a composition containing a base vinyl chloride resin and a plurality of plasticizers as a raw material is disclosed in Japanese Patent Publication No. 39-23g! ig issue, special public show '70-, t2
3. There is a method described in Publication No. 3.

しかし、これら公報に記載の方法によって、厚さか0.
 / 111m前後の極めて薄く軟質であるフィルムを
製造することは困難である。
However, by the methods described in these publications, the thickness can be reduced to 0.
It is difficult to produce an extremely thin and flexible film with a thickness of around 111 m.

本発明者らシマ、かかる状況にあって、衣料用、包装用
、両生用品用等に用いられろ、厚さかo/mm前後で、
軟質の通気性フイJLrムを工業的有利に製造1−る方
法を提供することを目的として、鋭意倹訓した結果、本
発明を完成1−るに至ったものである。
In this situation, the inventors of the present invention believe that it can be used for clothing, packaging, household goods, etc., with a thickness of around 0/mm.
With the aim of providing an industrially advantageous method for producing a soft breathable film, the present invention has been completed as a result of intensive study.

本発明の要旨と1−るところは、乳化重合法、又は微細
懸濁重合法によって得られた重合体乳濁液を乾燥して得
られプこ、平均粒子径が3−0ミクロン以下の塩化ビニ
ル系樹脂を、可塑剤ととも(・て水に分散し、この分散
液を、表面榮I]離性を有1−る基材(/コ塗布して塗
布11Qを形成し、ついでこの塗布1漢を次の(1)式
、すなわちTg−1−(/ 3O−jl]塑剤添加部数
)  ・・・・(1)〔(I)式において、Tg  は
塩化ヒニル系植脂のガラス転移点を、可塑剤添加部数は
塩化ビニル系材脂700重量部に対する可塑剤の添加部
数をそれぞれ意味する。〕 で表わされる温度以下で加熱、浴融させたのち冷却する
ことを特徴とする通気性フィルムの製造方法に存する。
The gist and first feature of the present invention is that a polymer emulsion obtained by an emulsion polymerization method or a fine suspension polymerization method is dried, and the average particle size is 3-0 microns or less. A vinyl resin is dispersed in water together with a plasticizer, and this dispersion is applied to a substrate (1) having release properties to form a coating 11Q. 1 kan is converted into the following formula (1), that is, Tg-1-(/3O-jl] number of parts of plasticizer added)... (1) [In formula (I), Tg is the glass transition of the hinyl chloride-based fat. The number of parts of plasticizer added means the number of parts of plasticizer added to 700 parts by weight of vinyl chloride-based material. The problem lies in the film manufacturing method.

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

本発明において塩化ビニル系樹脂とは。ポリ塩化ビニル
及び塩化ビニルを主体とする共重合体を意味する。塩化
ビニルと共重合しうるモノマートシてハ、ビニルエステ
ル類、ビニルエーテル類、アクリル酸又はメタクリル酸
及びこれらのエステル類、マレイン酸又はフマールは及
びこれらのエステル類、ならびに無水マレイン酸、芳香
族ビニル化合物、ハロゲン什ビニリチン化合物、アクリ
ロニトリル、メタクリロニトリル、エチレン、プロピレ
ンなどがあげられる。
What is vinyl chloride resin in the present invention? It means polyvinyl chloride and a copolymer mainly composed of vinyl chloride. Monomers copolymerizable with vinyl chloride, vinyl esters, vinyl ethers, acrylic acid or methacrylic acid and esters thereof, maleic acid or fumar and esters thereof, maleic anhydride, aromatic vinyl compounds, Examples include halogenated vinylitine compounds, acrylonitrile, methacrylonitrile, ethylene, and propylene.

これらモノマーに微量の多官能基含有化合物を添加し、
部分架橋させたものであってもよい。
Adding a trace amount of a compound containing a polyfunctional group to these monomers,
It may be partially crosslinked.

上記塩化ビニル系樹脂は、乳化重合法又は微細懸濁(マ
イクロサスペンション)重合法によって製造したものを
用いる。これら方法で製造した塩化ビニル系樹脂は、平
均粒子径が小さく、通気性フィルムを製造するのに好適
である。
The vinyl chloride resin used is one produced by emulsion polymerization or microsuspension polymerization. The vinyl chloride resins produced by these methods have small average particle diameters and are suitable for producing breathable films.

本発明によるときは、上記方法で製造した塩化ビニル系
樹脂の乳濁液を乾燥して粉末とし、この粉末を用いる。
According to the present invention, the vinyl chloride resin emulsion produced by the above method is dried to form a powder, and this powder is used.

乳化重合法によって得られろ樹脂乳濁液を、例えば噴霧
乾燥法(、(より乾燥すると、平均粒子径か2ミクロン
以下の微小粒子か多数凝集しあい、平均粒子径かSミク
ロンないしtioミクロンの多孔質の粒子が形成される
。微細懸濁重合法((よって得られろ仙脂は、平均粒子
径か20ミクロンないし40ミクロンて、この樹脂゛も
乾燥時に0個の粒子か凝集し合うか、凝集する性質は乳
化重合法(でよって製造したものほど強くはない。
When the resin emulsion obtained by the emulsion polymerization method is dried, for example, by spray drying, a large number of microparticles with an average particle size of 2 microns or less aggregate, and porous particles with an average particle size of S microns to 10 microns are formed. Fine suspension polymerization method (Thus, the average particle diameter of the Sensin resin obtained is 20 to 40 microns, and the resin is either 0 particles or aggregates together when dried. The agglomeration property is not as strong as that produced by the emulsion polymerization method.

本発明によるときは、上記乾燥した塩化ビニル系樹脂粉
末のうち、平均粒子径が50ミクロン以下のものを用い
る。平均粒子径かSOミクロン以上であると、最終的(
(得られるフィルムの強度、通気性を好ましく調節する
のが軸かしく、これら性質が均衡したフィルムを安定し
て得ることかできない。最終的に得られるフィルムの通
気性は、使用する塩化ビニル系8j脂の平均粒子径によ
って変わる。塩化ビニル系樹脂は、平均粒子径が50ミ
クロン以下でsミクロン以上のものから選択使用可能で
あり、はぼ均一な平均粒子径のもの用いても、異なる平
均前られる通気性フィルムの通気量、強度、感触なとに
よって、一種類としたり二種類としたり、単一樹脂(ホ
モポリマー)としたり、共重合樹脂としたり、種々選ぶ
ことかできろ。
According to the present invention, among the dried vinyl chloride resin powders, those having an average particle size of 50 microns or less are used. If the average particle size is SO micron or more, the final (
(It is important to properly adjust the strength and air permeability of the resulting film, and it is not possible to stably obtain a film with balanced properties.The air permeability of the final film depends on the vinyl chloride type 8J used. It varies depending on the average particle size of the fat.Vinyl chloride resins can be selected from those with an average particle size of 50 microns or less and s microns or more. Depending on the air permeability, strength, and feel of the breathable film, you can choose from a variety of options, such as one or two types, a single resin (homopolymer), or a copolymer resin.

不発叩圧よろときは、上記塩化ビニル系ml脂粉末を、
可塑剤ととも洒髭散し、可塑剤を環化ビニル系i栢脂粉
末に吸収させろ。
If the misfire occurs, use the vinyl chloride-based ml fat powder,
Sprinkle with a plasticizer to absorb the plasticizer into the cyclized vinyl powder.

この除用いることかできる可塑剤として(ま、ジオクチ
ルフタレート、ジベンジルフタレート、ブチルベンジル
フタレート、ジベンジルフタレート、ジオクチルフタレ
ート、ジオクチルフタレート、ジオクチルフタレート等
のフタル酸エステル知;アジピン酸ジオクチル、アノピ
ン酸ジーn−ブチル、セバシン酸ジブチル等の脂肪族二
塩基酸エステル類;ペンタエリスリトエステル =17つエチレングリコ−/l/ シヘンゾエート等の
グリコールエステル類;アセチルリンノール酸メチル等
の脂肪酸エステル類;トリクレジルホスフェート、トリ
フェニルホスフェート等)りん鍍エステル類;エポキ/
化大豆油、エポキ/化アマニ油等のエポキシ化油;アセ
テルトリフチルントレ−1・、アセチルトリオクチル/
トレー1・、トリーローブチル/l−1/−ト等のクエ
ン酸エステルガラ;トリアルキルトφ>  +−、テト
ラ−n−オクチルピロメリテート、ポリプロピレンア/
ぺ−1・、七〇曲ポリエステル系等のTi1]/zのb
丁”I]!’!lかあ(ザられる。これら可塑i11は
一種類でも、二陣胡シ、上を組み合せて用いてもよい。
Plasticizers that can be removed include phthalate esters such as dioctyl phthalate, dibenzyl phthalate, butylbenzyl phthalate, dibenzyl phthalate, dioctyl phthalate, dioctyl phthalate, dioctyl phthalate; dioctyl adipate, dianopinate -Aliphatic dibasic acid esters such as butyl and dibutyl sebacate; Pentaerythrite ester = 17 ethylene glycol/l/ Glycol esters such as shihenzoate; Fatty acid esters such as methyl acetyl linoleate; Tricresyl phosphate, triphenyl phosphate, etc.) phosphorus esters; epoxy/
Epoxidized oils such as oxidized soybean oil, epoxidized linseed oil;
Tray 1・, citric acid ester glass such as trilobyl/l-1/-; trialquilt φ> +-, tetra-n-octylpyromellitate, polypropylene a/
Pe-1・, 70 songs Ti1]/b of z
Ding"I]!'!lka (zareru. These plastic i11 may be used in one type or in combination of two types and two types.

可カ4削の量・1ま、塩化ビニル系樹脂700重搦゛部
に対して、20〜70重量部の範囲内で・選ぶことがで
きる。
The amount of scraping can be selected within the range of 20 to 70 parts by weight per 700 parts by weight of vinyl chloride resin.

塩化ビニル系樹脂粉末と可塑剤とを水に分散させるため
((は、分散剤を用いる。分散剤として使用可能なもの
シま、通常界面活囲剤として知られているものでよい。
In order to disperse the vinyl chloride resin powder and plasticizer in water, a dispersant is used.What can be used as a dispersant is one commonly known as a surfactant.

例えば、脂肪酸石けん、アルキル硫酸エステル塩、アル
キルスルホン酸塩のようなアニオン界面活性剤;第1級
アミン塩、第2級アミン塩、第3級アミン塩のようなカ
チオン界面活性剤;アルキルベタインのヨウナ両性界面
活性剤;ポリオキシエチレンアルキルエーテル、ポリオ
キシエチレンアルキルアミン等の非イオン界面活性剤が
あげられる。
For example, anionic surfactants such as fatty acid soaps, alkyl sulfates, and alkyl sulfonates; cationic surfactants such as primary amine salts, secondary amine salts, and tertiary amine salts; Ampholytic surfactants include nonionic surfactants such as polyoxyethylene alkyl ether and polyoxyethylene alkyl amine.

上記分散剤は、塩化ビニル系a脂と可・ψ剤とダ、0 の合計敬に対して、0/〜9.−重量%の範囲で使用す
れはよい。
The above-mentioned dispersant has a ratio of 0/ to 9. - It may be used within the range of % by weight.

塩化ヒニル系)yii脂粉米粉末塑剤とを、水に分散さ
せるには、これら二成分を分散剤を溶削′シた水に加え
、攪拌混合する。この際、水と固形分(塩化ビニル系樹
脂と可塑剤との和)との比率は、固形分の濃度を分散液
(水と固形分との和)のユ0〜go重量%の範囲とする
。固形分のa度が、この範囲より低かったり、逆に高い
ときは、最終的に得られるフィルムの厚さを調節するの
か困難であり、好凍しくない。固形分の濃度は、上記範
囲のうちグ0〜60重量%の範囲が、特に好ましい。
In order to disperse the (hinyl chloride-based) yii fat flour rice powder plasticizer in water, these two components are added to the water in which the dispersant has been melted and mixed by stirring. At this time, the ratio of water and solid content (sum of vinyl chloride resin and plasticizer) is determined by adjusting the concentration of solid content in the range of 0 to 0% by weight of the dispersion (sum of water and solid content). do. When the degree of solid content is lower than this range or conversely higher than this range, it is difficult to control the thickness of the final film, and the film does not freeze well. The solid content concentration is particularly preferably in the range of 0 to 60% by weight within the above range.

分散液の攪拌混合は、可塑剤を塩化ビニル系樹脂粉末に
吸収させるために行なう。塩化ビニル系松脂粉末(7、
配合した可塑剤の全量を吸収させてしまうと、最終的に
得られる通気性フィルム表面に亀裂か生ずる。従って、
塩化ビニル系樹脂粉末((吸収させる可塑剤敏は、配合
した可塑剤の一部、望ましく!ま約半分とし、残りは水
((分散している状態と1−るのかよい。このように1
−る:〆こ(ま、水に可塑剤の余計を加えて攪イ1゛強
度、攪拌時[;」]等乞変えて、塩化ヒニル系樹脂粉末
へ吸収さぜる紹゛を肌面づ−る方法、丑ず可塑剤の約半
分を!i1;えでこれを塩化ヒニル系4fL1脂粉末へ
ほぼ吸収させ、残りを水に加えて分散させる方法等を、
とれはよい。
The dispersion is stirred and mixed in order to absorb the plasticizer into the vinyl chloride resin powder. Vinyl chloride pine resin powder (7,
If the entire amount of the blended plasticizer is absorbed, cracks will occur on the surface of the finally obtained breathable film. Therefore,
Vinyl chloride resin powder ((The plasticizer density to be absorbed is a part of the blended plasticizer, preferably! About half, and the rest is water ((It is good to be in a dispersed state.
- 〆(Well, add excess plasticizer to water and stir.) - a method in which approximately half of the Ushizu plasticizer is absorbed into hinyl chloride-based 4fL1 fat powder, and the remainder is added to water and dispersed.
The amount is good.

水に塩化ビニル系樹脂と可塑剤を分散させる際に使用し
つる攪拌混合機は、液体(に固体を分散1−る目的で従
来から使用されている1μs拌混押湯であってよい。
The vine stirring mixer used when dispersing the vinyl chloride resin and plasticizer in water may be a 1 μs stirring mixer conventionally used for the purpose of dispersing solids in liquids.

分散液を調製する際に、樹脂安定剤、紫外線吸収剤、充
填材、染料、顔料、難燃剤等を少量添加、混合すること
ができる。
When preparing the dispersion, small amounts of resin stabilizers, ultraviolet absorbers, fillers, dyes, pigments, flame retardants, etc. can be added and mixed.

上記分散液を攪拌混合機で調製する際に、分散液には、
気泡、ゲル、塊状物が含まれることかあるので、これら
を真空脱泡機、ホバートミキサー、ロールミル、フィル
ター等を用いて除去するのが好ましい。
When preparing the above dispersion using a stirring mixer, the dispersion contains
Since air bubbles, gels, and lumps may be included, it is preferable to remove these using a vacuum deaerator, a Hobart mixer, a roll mill, a filter, or the like.

本発明によるときは、上記方法で調製した分散液を、表
面剥離性を有する基材に塗布する。
According to the present invention, the dispersion prepared by the above method is applied to a substrate having surface releasability.

この基材は、分散液にもとつく塗布膜を支持する機能を
果すものである。基材(・マ、金属薄板、紙、耐熱樹脂
薄板より構成するのかよい。この基材の塗布膜を形成す
る面には、塗布膜を加熱溶融したのち得られる通気性フ
ィルムか、剥離しやすいように、離型剤に塗布するなど
により、表面剥離性を付与しておく。
This base material functions to support the coating film based on the dispersion liquid. The base material may be made of a thin metal plate, paper, or a thin heat-resistant resin plate.The surface of this base material on which the coating film will be formed may be a breathable film obtained after heating and melting the coating film, or a film that is easily peeled off. In this way, surface releasability is imparted by applying a mold release agent or the like.

分散液を基材に塗布して塗布膜を形成するには、スプレ
ィコート法、ロールコート法、グラビアコート法、リバ
ースコート法、ディップコート法、ナイフコート法等の
それ自体公知の各種塗布方法によればよい。
To form a coating film by applying the dispersion to a base material, various coating methods known per se such as spray coating, roll coating, gravure coating, reverse coating, dip coating, and knife coating can be used. It's fine.

基材の剥離性を付与した面に形成する塗布膜の厚さは、
次の加熱溶融工程終了後に得られる通気性フィルムの厚
さが005〜05印の範囲となるように、調節1−るり
かよい。塗布膜を加熱すると、水分が揮散するので、最
終的に得られる通気性フィルムの厚さは、もとの塗布膜
に較へてこれに含捷れている水分に相当てろ割合で薄く
なる。通気性フィルムは、余り薄すぎろと強度か充分で
なくて実用性か劣るので好ましくなく、逆((余り厚す
きろと充分な通気性を発揮しえなくなる。このため、厚
さ00/−09mmの範囲とfるのかよく、中で゛も0
.O3−〇、30Firmの範囲とするのがよ(・。
The thickness of the coating film formed on the releasable surface of the base material is:
Adjustment 1-Rurikai so that the thickness of the breathable film obtained after the next heating and melting step is in the range of 005 to 05 marks. When the coating film is heated, the moisture evaporates, so that the thickness of the breathable film finally obtained becomes thinner than the original coating film by a proportion corresponding to the moisture contained therein. If the breathable film is too thin, it will not have enough strength and will be less practical, so it is undesirable. It seems that the range of 09mm is f, and ゛ is also 0 in the range.
.. O3-〇, it is better to set it in the range of 30 Firm (・.

本発明によるとき(・ま、上記方法で形成した塗布膜を
、加熱、溶融する。加熱することにより、塗布膜に含ま
れる水分を揮散させ、続いて樹脂粒子表面を溶融して隣
接する粒子同志を接着させる。この際の加熱温度が余り
高いときは、加熱時間か短かくても、樹脂粒子が完全に
溶融し、粒子形状がくずれてしまうので、通気孔が形成
できない。本発明者らの実験によれば、加熱、溶融する
際の最適温度は、樹脂の二次転移点、樹脂に配合する可
塑剤の量によって変わることかわかった。すなわち、加
熱、溶融する際の温度は、次の(1)式、 Tg+(/so−可塑剤添加部数) ・・・・・・(1
)〔(1)弐において、Tg  は塩化ビニル系樹脂の
ガラス転移点を、可塑剤添加部数は塩化ビニル系樹脂7
00重量部に対する可塑剤添加部数をそれぞれ意味する
。〕 で表わされる温度以下とするのがよいことが分った。な
お、加熱する温度が余り低すぎるときは、長時間加熱し
ても樹脂粒子表面が溶融しないので、強度の優れた通気
性フィルムが得られない。加熱、溶融する際の下限温度
は、上記CI)式で表わされる温度より約Sθ℃低い温
度である。
According to the present invention, the coating film formed by the above method is heated and melted. By heating, the water contained in the coating film is evaporated, and then the surface of the resin particles is melted, and the adjacent particles are melted. At this time, if the heating temperature is too high, even if the heating time is short, the resin particles will completely melt and the particle shape will collapse, making it impossible to form vent holes. According to experiments, it was found that the optimum temperature for heating and melting varies depending on the secondary transition point of the resin and the amount of plasticizer added to the resin.In other words, the optimum temperature for heating and melting is as follows: Formula (1), Tg+(/so-number of plasticizer added)...(1
) [In (1) 2, Tg is the glass transition point of the vinyl chloride resin, and the number of parts of plasticizer added is the vinyl chloride resin 7
Each refers to the number of parts of plasticizer added per 00 parts by weight. ] It was found that it is best to keep the temperature below the following. Note that if the heating temperature is too low, the surface of the resin particles will not melt even if heated for a long time, and a breathable film with excellent strength will not be obtained. The lower limit temperature during heating and melting is about Sθ°C lower than the temperature expressed by the above formula CI).

加熱、溶融の操作は、上記(1)式で表わされる上限温
度より若干低い温度で、2〜3分間程度の短時間加熱す
るのがよいが、加熱を高温で急激に行なうと、最終的に
得られるフィルムに多数の小さな亀裂が生ずることか多
い。この小さな亀裂を生じないようにするためには、加
熱、溶融の操作を行なう前((、qO〜gocの温度で
5分以内加熱する予備乾:陛操作を行なって、塗布j換
に含゛まれろ水分の一部を揮散させたのち、加熱、溶融
の操作を行なうとよい。
For heating and melting operations, it is best to heat for a short time of about 2 to 3 minutes at a temperature slightly lower than the upper limit temperature expressed by equation (1) above, but if heating is performed rapidly at a high temperature, The resulting film often has many small cracks. In order to prevent these small cracks from forming, it is necessary to perform a pre-drying operation by heating within 5 minutes at a temperature of qO to GOC before heating and melting. After volatilizing some of the moisture, heating and melting may be performed.

本発明によるとき1ま、上記方法で得られる通気性フィ
ルムを、常温付近−まで冷却し、通気性フィルムのみ、
又はこれど基体と?−諸に、ロール状に巻き取る。
According to the present invention, first, the breathable film obtained by the above method is cooled to around room temperature, and only the breathable film is
Or is this the base? - Roll it up into rolls.

なお、通気性フィルムを冷却1−る途中で、又は冷却し
たのちに、このフィルムの片面又(・ま両面+C、シリ
コーンオイル、シリコーンエマルジョン等の撥水1生物
質を塗布すると、通気性フィルムに撥水性を付与するこ
とができる。
In addition, if you apply a water repellent material such as +C, silicone oil, silicone emulsion, etc. to one or both sides of the film during or after cooling the breathable film, the film will become Can impart water repellency.

本発明方法によって得られろ通気性フィルム(ま、通常
の軟質プラスチックフィルムと同様に印刷、接着等の二
次加工が可能である。本発明方法によって得られる通気
性フィルムシす、単独能である。
The breathable film obtained by the method of the present invention can be subjected to secondary processing such as printing and adhesion in the same way as ordinary soft plastic films.The breathable film obtained by the method of the present invention can be used independently. .

本発明方法は、次のように特別に顕蓄な効果を奏し、産
業上の利用価値は極めて犬である。
The method of the present invention has particularly remarkable effects as described below, and has extremely high industrial utility value.

(1)本発明方法によるときは、0.0 /〜Q、’ 
、5−111mの範囲の極めて薄く、しかも柔軟性のあ
る通気性フィルムを、容易に製造′1−ることができろ
(1) When using the method of the present invention, 0.0/~Q,'
, extremely thin and flexible breathable films in the range of 5-111 m can be easily produced.

(2)本発明方法によるときは、通気性フィルムの通気
量を、樹脂粉末の平均粒子径、可塑剤の量、塗布膜の厚
さ、塗布膜を加熱、溶融するl黒度、時間等を選ぶこと
により、容易に変更することができる。
(2) When using the method of the present invention, the amount of air permeable in the breathable film, the average particle diameter of the resin powder, the amount of plasticizer, the thickness of the coating film, the blackness of heating and melting the coating film, the time, etc. You can easily change it by selecting it.

(3)本発明方法によるときは、最終的に得られる通気
性フィルムへの着色が容易であり、撥水性を付与するこ
とも容易である。
(3) When using the method of the present invention, it is easy to color the breathable film finally obtained, and it is also easy to impart water repellency to it.

(4)本発明方法によつC得られろ通気性フィルムは、
隣り合う樹脂粒子の間に空隙が形成され、これがフィル
ムの一方の側から他方の側に連通している。よって、布
とはり合わせて雨具、オシメカバー等の用途に便用する
際、水分が透過されやすく、蒸れることかない。
(4) The breathable film obtained by the method of the present invention is:
A void is formed between adjacent resin particles, and this void communicates from one side of the film to the other side. Therefore, when it is attached to cloth and used for purposes such as rain gear or diaper covers, moisture easily permeates through it and it does not get stuffy.

以下、本発明を実施例にもとづいて更に詳細に説明する
が、本発明はその要旨を超えない限り、以下の列に限定
さjするものではなし・。
Hereinafter, the present invention will be explained in more detail based on Examples, but the present invention is not limited to the following columns unless it exceeds the gist thereof.

実施例/ 、7L化重合法してよって、製造し、噴霧乾燥法で乾燥
したポリ塩化ビニル粉末(平均重合度/100、ガラス
転移点f′1gO℃、平均粒子径10ミクロンのもの)
をSO0重量%水q7重量索条びトチ/ルベンセノスル
ホン酸7−1−(D 13 S ) 3重量%の割合よ
りなる三成分を混合し、混合?lkAを調製した。
Example/ Polyvinyl chloride powder produced by 7L polymerization method and dried by spray drying method (average degree of polymerization/100, glass transition point f'1 gO ℃, average particle size 10 microns)
Mix the three components consisting of SO 0 wt % water q 7 wt % and horse chestnut/rubensenosulfonic acid 7-1-(D 13 S ) 3 wt %, and mix? lkA was prepared.

一方、ジオクチルフタL/−トbj!;重量%、水32
重量%及びDBSJ電量係の索条よりなる三成分を混合
し、混合液Bを調製した。
On the other hand, dioctyl phthalate L/-t bj! ;wt%, water 32
Mixture B was prepared by mixing three components consisting of weight percent and DBSJ coulometric ratio.

形分はssg重量係索条リ塩化ビニルioo重量部罠対
する可塑剤添加部数は、!iO重量部である。
Shape is ssg weight rope PVVC ioo weight part number of plasticizer added to the trap is! iO parts by weight.

上記分散液を、市販されて(・る離型紙(紙の表面に離
型剤が塗布されている紙)の表面に、ナイフコート法に
より塗布し、塗布膜を形成した。
The above dispersion was applied onto the surface of commercially available release paper (paper whose surface is coated with a release agent) by a knife coating method to form a coating film.

この塗布膜を形成した離型紙を、gθ℃に調節した熱風
炉に3分間放置して、塗布膜の予備乾燥を行なった。続
いて、この塗布膜付きの離型紙を/ ’)OCに調節し
た熱風炉に7分間放置して、水分をほぼ完全に揮散させ
たのち、ポリ塩化ビニル粉末の粒子表面を溶融させて、
隣接する粒子表面同志を付着させた。
The release paper on which the coating film was formed was left in a hot air oven adjusted to gθ°C for 3 minutes to pre-dry the coating film. Subsequently, the release paper with the coated film was left in a hot air oven adjusted to /') OC for 7 minutes to volatilize the moisture almost completely, and then the surface of the polyvinyl chloride powder particles was melted.
Adjacent particle surfaces were attached to each other.

上の加熱、溶融の操作終了後、フィルムを冷却し、厚さ
Q、 / l+1mの通気性フィルムを得た。この通気
性フィルムを「フィルム/」という。
After the above heating and melting operations were completed, the film was cooled to obtain a breathable film with a thickness of Q, /l+1 m. This breathable film is called "film/".

「フィルム/」の表面に、反応性シリコーンエマルジョ
゛ン(トーレシリコーン社g 、S Mg7os)をグ
ラビアコート法により塗布し、塗布後gθ℃に調節した
熱風炉中で30秒間加熱し、水分を揮散させた。このフ
ィルムを「フィルムコ」という。
A reactive silicone emulsion (manufactured by Toray Silicone Co., Ltd., S Mg7os) was applied to the surface of "Film/" by the gravure coating method, and after application, it was heated for 30 seconds in a hot air oven adjusted to gθ℃ to remove moisture. It was vaporized. This film is called ``Filmco''.

「フィルム/」及び「フィルムコ」につき、通気性、撥
水性、引張り強さ及び平均孔径等を、次の方法((従っ
て測定した。測定結果を第1表に記す。
The air permeability, water repellency, tensile strength, average pore diameter, etc. of "Film/" and "Filmco" were measured by the following methods. The measurement results are shown in Table 1.

通気性・・鴛素ガスをo、 s kg、/ cnrの圧
力で送り、/平方センチメートル当り、7分間 の透過量として表示(’ cc / mrn / に尻
)。
Air permeability: Slow gas is sent at a pressure of o, s kg, / cnr, and expressed as the permeation amount per square centimeter for 7 minutes (in 'cc/mrn/).

撥水江・・JIS L−1092スプレー法に準拠した
Water repellent: Conforms to JIS L-1092 spray method.

引張り強さ JIS K−A732に準拠した。Tensile strength: Based on JIS K-A732.

平均孔径・電子顕微鏡による。Average pore diameter by electron microscopy.

実施例コ 実施例/((記載の例におけろポリ塩化ビニル粉末を、
乳化重合法によって製造し、噴霧乾燥法で乾燥した平均
重合度/り0Q、ガラス転移点的gθ℃、平均粒子径5
ミクロンのポリ塩化ビニル粉末て代えたほかは、同側記
載の方法と同様の操作手順で、通気性フィルムを製造し
た。
Example/Example/((In the example described, polyvinyl chloride powder was
Produced by emulsion polymerization method and dried by spray drying method, average degree of polymerization / 0Q, glass transition point gθ℃, average particle size 5
A breathable film was produced using the same procedure as described above, except that micron polyvinyl chloride powder was used instead.

得られた通気性フィルムの表面に、「フィルム2」を調
製したと同様にして反応性シリコーンエマルジョンを塗
布し、乾燥した。こうして得られた通気性フィルムを、
「フィルム3」という。
A reactive silicone emulsion was applied to the surface of the obtained breathable film in the same manner as in preparing "Film 2" and dried. The breathable film thus obtained is
It's called "Film 3."

「フィルム3」について、「フィルム/」ヲ評価したと
同様の方法で、諸性質を評価した。
Regarding "Film 3", various properties were evaluated in the same manner as in the evaluation of "Film/".

結果を第1表に記す。The results are shown in Table 1.

実施例3 実施例/に記載の例((おけるポリ塩化ビニルを、乳化
重合法によって製造し、噴霧乾燥法で乾燥した塩化ビニ
ルと酢酸ビニルとの共重合体(平均重合度1000、酢
酸ビニル含有量3重量%、ガラス転移点的70℃、平均
粒子径25ミクロン)に代えたほかは、同側記載の方法
と同様の手順で、分散液を調製した。
Example 3 Example described in Example/ A dispersion liquid was prepared in the same manner as described on the same side, except that the amount was 3% by weight, the glass transition temperature was 70° C., and the average particle size was 25 μm.

得られた分散液を、実施例/に記載したと同、錘にして
離型紙表面に塗布し、塗布膜の予備乾燥を行なった。続
いて、この塗布膜付きの離型紙を/bO’Qvc調節し
た熱風炉で1分間加熱、溶融した。
The obtained dispersion was applied as a weight to the surface of a release paper in the same manner as described in Examples, and the coating film was pre-dried. Subsequently, the release paper with the coated film was heated and melted for 1 minute in a hot air oven adjusted to /bO'Qvc.

これを冷却したのち、得られた通気性フィルムの表面に
、「フィルムコ」を調製したと同、峰にして反応性シリ
コーンエマルジョンを塗布し、乾燥した。こうして得ら
れた通気性フィルムを、「フィルムq」という。
After cooling, the surface of the obtained breathable film was coated with a reactive silicone emulsion in the same manner as in the preparation of "Filmco" and dried. The breathable film thus obtained is referred to as "film q".

「フィルムク」ニついて、「フィルム/」ヲ評価したと
同様の方法で、諸性質を評価した。
The various properties of "Filmku" were evaluated in the same manner as "Film/" was evaluated.

結果を47表に記す。The results are shown in Table 47.

比般例/ 実施例/に記載の方法において、塗布、嘆の加熱、溶融
の操作条l/1:な、1qoCvc調節した熱風炉で7
分間としたほか(ま、回倒に記載の方法と同様の操作手
順で、通気性フィルムを製造した。
In the method described in Comparative Example/Example/, the operating conditions of coating, heating, and melting were 1/1: 7 in a hot air oven adjusted to 1 qoCvc.
In addition, a breathable film was manufactured using the same operating procedure as described in ``Returning''.

得られた通気性フィルムの表面に、「フィルムコ」を調
製したと同様にして反応性シリコーンエマルジョンを塗
布し、乾燥した。こうして得られたフィルムを、「フィ
ルムs」という。
A reactive silicone emulsion was applied to the surface of the obtained breathable film in the same manner as in preparing "Filmco" and dried. The film thus obtained is called "film s".

「フィルムク」について、「フィルム/Jを評価したと
同様の方法で、諸性質を評価した。
Regarding "Filmku", various properties were evaluated in the same manner as "Film/J" was evaluated.

結果を框/表に記す。Record the results in the box/table.

第1表 ( ( 第1表より、次のことが明らかとなる。Table 1 ( ( From Table 1, the following becomes clear.

(1)本発明方法によって得られるフィルムは、平均孔
径が犬きく、従って通気性も優れている。
(1) The film obtained by the method of the present invention has a large average pore diameter and therefore has excellent air permeability.

(2)平均粒子径の大きい塩化ビニル系樹脂を用いると
、平均孔径が犬となり、通気性も優れたものか得られる
か強度は若干低下′1″る傾向が認められる(「フィル
ム3」と「フィルムク」との比較。)。
(2) When a vinyl chloride resin with a large average particle size is used, the average pore size becomes small, and there is a tendency for the strength to be slightly lowered (“Film 3” and “Film 3”). Comparison with "Filmku").

3)ソリコーンエマルジョンを塗布乾燥すると、通気性
フィルムの撥水性は飛躍的に向上1−ろ([フィルム/
Jと「フィルムス」との比較。)。
3) When the soricone emulsion is applied and dried, the water repellency of the breathable film increases dramatically.
Comparison between J and "Films". ).

4)塗布膜を加熱、溶融1−ろ温度が、前記f1)式で
表わされろ上限温度以上であると、粒子が完全((浴融
し形かくずれろために、平均孔径(・ま小さくなり、通
気性も低下する(「フィルム/」と「フィルムS」との
比収。) 出願人  三菱モンサント化成株式会社代理人  弁理
士 長谷用   − (、□・1か7名)
4) When the coating film is heated and the melting temperature is equal to or higher than the upper limit temperature expressed by the formula f1), the particles are completely melted (because the bath melts and collapses, the average pore size (・) becomes smaller, Air permeability also decreases (relative yield between "Film/" and "Film S".) Applicant Mitsubishi Monsanto Chemicals Co., Ltd. Representative Patent Attorney Hase - (, □・1 or 7 people)

Claims (1)

【特許請求の範囲】 (1)乳化重合法、又は微細懸濁重合法によって得られ
た重合体乳懸濁液を乾燥して得られた、平均粒子径がs
oミクロン以下の塩化ビニル系樹脂を、可塑剤とともに
水に分散し、この分散液を、表面剥離性を有する基材に
塗布して塗布膜を形成し、ついでこの塗布膜を次の([
)式、すなわち Tg + (tso−可塑剤添加部数) ・・・(1)
〔(I)式において、Tg  は塩化ビニル系樹脂のガ
ラス転移点を、可塑剤添加部数は塩化ビニル系樹脂io
o重量部に対する可塑剤の添加部数をそれぞれ意味する
。〕 で表わされる温度以下で加熱、浴融させたのち冷却する
ことを特徴とする通気性フィルムの製造方法。 (2)塩化ビニル系樹脂を、可塑剤とともに水に分散さ
せる際、温度を塩化ビニル系樹脂のガラス転移温度付近
とし、固形分(塩化ビニル系樹脂と可塑剤)濃度を、分
散液の20〜g。 重量%の範囲とすることを特徴とする特許請求の範囲第
(1)項記載の通気性フィルムの製造方法。 (31可塑剤を塩化ビニル系樹脂とともに水に分散させ
る際((、全可塑剤量の約半分を塩化ビニル系樹脂に吸
収させ、残りの可塑剤は塩化ビニル系樹脂に吸収させな
見・状態の分散液とづ−ることを特徴とする特許請求の
範囲第(1)項ないし第(2)項記載の通気性フィルム
の製造方法。 (4)  基材に塗布する塗布膜の厚さを、0.0 /
〜0、 S mmの範囲とすることを特徴とする特許請
求の範囲第(1)項ないし第(2)項記載の通気性フィ
ルムの製造方法。
[Scope of Claims] (1) Polymer milk suspension obtained by emulsion polymerization method or fine suspension polymerization method is dried, and the average particle size is s.
A vinyl chloride resin with a size of 0 microns or less is dispersed in water together with a plasticizer, and this dispersion is applied to a base material with surface releasability to form a coating film.
) formula, that is, Tg + (tso - number of parts of plasticizer added)...(1)
[In formula (I), Tg is the glass transition point of the vinyl chloride resin, and the number of plasticizer added is the vinyl chloride resin io
o Each refers to the number of parts of plasticizer added to parts by weight. ] A method for producing a breathable film, which comprises heating and bath-melting the film at a temperature below the temperature expressed by the formula, followed by cooling. (2) When dispersing vinyl chloride resin in water together with a plasticizer, the temperature should be set near the glass transition temperature of the vinyl chloride resin, and the solid content (vinyl chloride resin and plasticizer) concentration should be 20 to 20% of the dispersion. g. The method for producing a breathable film according to claim 1, wherein the amount is within a range of % by weight. (31 When dispersing a plasticizer in water together with a vinyl chloride resin, approximately half of the total amount of plasticizer is absorbed into the vinyl chloride resin, and the remaining plasticizer is not absorbed into the vinyl chloride resin.) A method for producing a breathable film according to claims (1) to (2), characterized in that a dispersion of ,0.0/
A method for producing a breathable film according to claims (1) to (2), characterized in that the thickness is in the range of 0.0, S mm.
JP17950082A 1982-10-13 1982-10-13 Method for manufacturing breathable film Granted JPS5968343A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17950082A JPS5968343A (en) 1982-10-13 1982-10-13 Method for manufacturing breathable film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17950082A JPS5968343A (en) 1982-10-13 1982-10-13 Method for manufacturing breathable film

Publications (2)

Publication Number Publication Date
JPS5968343A true JPS5968343A (en) 1984-04-18
JPH0432857B2 JPH0432857B2 (en) 1992-06-01

Family

ID=16066901

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17950082A Granted JPS5968343A (en) 1982-10-13 1982-10-13 Method for manufacturing breathable film

Country Status (1)

Country Link
JP (1) JPS5968343A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4967952A (en) * 1972-11-04 1974-07-02

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4967952A (en) * 1972-11-04 1974-07-02

Also Published As

Publication number Publication date
JPH0432857B2 (en) 1992-06-01

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