JPH083878A - Production of air permeable vinyl chloride leather and film - Google Patents

Production of air permeable vinyl chloride leather and film

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Publication number
JPH083878A
JPH083878A JP14495090A JP14495090A JPH083878A JP H083878 A JPH083878 A JP H083878A JP 14495090 A JP14495090 A JP 14495090A JP 14495090 A JP14495090 A JP 14495090A JP H083878 A JPH083878 A JP H083878A
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Japan
Prior art keywords
film
vinyl chloride
polyvinyl chloride
powder
seconds
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JP14495090A
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Japanese (ja)
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Takeshi Hiyama
健 桧山
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Individual
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Individual
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Abstract

PURPOSE:To provide a vinyl-coated leather having air permeability by heat- bonding a polyvinyl chloride film to a fiber base with a resin adhesive containing a foaming agent. CONSTITUTION:This method for producing a vinyl-coated leather and film having air permeability is to coat an interface between a fiber base (or a releasable sheet) and a polyvinyl chloride film with an aqueous emulsion (or a solvent type resin) containing a foamable inorganic salt capable of easily generating a gas (e.g. ammonium bicarbonate, ammonium chloride or sodium carbonate), scatter a hot-melt adhesive polymer selected from a polyamide, a polyester, a polyacetal and a polyolefin and having high crystallinity and a melting point with little difference from that of the polyvinyl chloride and press and bond the fiber base and the polyvinyl chloride film (at 140-100 deg.C for 10-40sec.).

Description

【発明の詳細な説明】 本発明は塩化ビニールフイルムから通気性のあ る塩化ビニールレザー、フイルムを製造する方法 に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a breathable vinyl chloride leather or film from a vinyl chloride film.

塩化ビニールは柔軟性あり、抗張力、引裂力強 く、防水力大で廉価のため、レインコート、レジ ャーウェア等その用途は多い。しかし通気性物品 という分野に於ては、その製造法が未だ解決され て居らない。従来フイルムに如何に孔をあけるか のみ研究されているが、耐水性、抗張力、柔軟性 の低下を招き、塩化ビニール特有の性質を失うた め実用化されて居らない。 Since vinyl chloride is flexible, has high tensile strength, strong tearing power, is highly waterproof, and is inexpensive, it has many uses such as raincoats and cashier wear. However, in the field of breathable articles, its manufacturing method has not been solved yet. Conventionally, only how to make holes in a film has been studied, but it has not been put to practical use because it causes deterioration of water resistance, tensile strength and flexibility and loses the properties peculiar to vinyl chloride.

従来被膜に通気性を与える方法としては、1、 機械的に孔をあける方法、2、超音波又は電子線 による方法、3、発泡剤を用いる方法、4、ポリ マー混合物から特殊の成分を抽出する方法、5、 水溶液中の凝固方法、6、延伸する方法、等が知 られている。現在市販されているスポーツ用品、 防水用品の大部分は繊維布地の表面に撥水加工或 いは発泡剤を含む合成樹脂溶液のコーチングによ って製造されているが、防水力は劣り、高度の防 水力を必要とする農作業合羽、通勤作業用レイン コート等にはビニール合羽が主として使われてい る。しかし、ムレる欠点を有し、通気性の解決は 多くの働く人々の切実に希望するところである、 塩化ビニール、ナイロン、ポリエステル、ポリア セタール、ポリオレフィン類のフイルムに直接通 気性を持たせることは未だ未解決である。それ故、 本発明の目的は塩化ビニールフイルムからその特 性を失わずに通気性を附与することにある。 本 発明は繊維基体と塩化ビニールフイルムとを接着 するに際し、その中間面に2種の接着剤を塗付す る。1種は熱熔融接着粉として、ポリアミド、ポ リエステル、ポリアセタール、ポリオレフィン類 中、高い結晶度を有し而もポリ塩化ビニールと大 差ない融点のポリマー粉末を、1種は炭酸水素ア ンモン、塩化アンモン、炭酸ナトリウム等ガス発 生無機塩の少くとも一つを含有する水性エマルジ ョン或いは溶剤タイプ接着剤を、個々別々に又は 混合分散液として塗付し、該熔融ポリマーの融点 以上の温度140℃〜100℃、10秒〜40秒 間加熱熔融し、両者を接着し通気性ある塩ビレザ ーを製造する方法にかかるものである。 Conventional methods for providing air permeability to coatings are: 1, mechanical perforation, 2, ultrasonic or electron beam method, 3, blowing agent, and 4, extraction of special components from polymer mixture. The following methods are known: 5, a method for coagulating in an aqueous solution, 6, a method for stretching, and the like. Most sports and waterproof products currently on the market are manufactured by water-repellent treatment on the surface of fiber cloth or by coating with a synthetic resin solution containing a foaming agent. Vinyl duck is mainly used for agricultural work duck and raincoat for commuting work which requires water proofing. However, it has a stuffy defect, and a breathable solution is a desperate hope of many workers. It is still not possible to directly give air permeability to a film of vinyl chloride, nylon, polyester, polyacetal, or polyolefin. It is unresolved. Therefore, it is an object of the present invention to provide breathability to a vinyl chloride film without losing its properties. According to the present invention, when the fiber substrate and the vinyl chloride film are adhered, two kinds of adhesives are applied to the intermediate surface thereof. One is a polymer powder having a high crystallinity and a melting point not much different from that of polyvinyl chloride among polyamides, polyesters, polyacetals, and polyolefins as hot-melt adhesive powders, and one is ammonium hydrogen carbonate, chloride. Aqueous emulsion or solvent type adhesive containing at least one gas generating inorganic salt such as ammonium or sodium carbonate is applied individually or as a mixed dispersion liquid, and the temperature is not lower than the melting point of the molten polymer. The present invention relates to a method for producing a breathable vinyl chloride sol by heating and melting the mixture at a temperature of 100 to 100 ° C. for 10 to 40 seconds and adhering the both.

水性エマルジョンの水蒸気或いは発生ガスが熔 融されたフイルムを突きぬけ、多孔性になること は考えられるが、フイルムを冷却し取出した場合、 ゆ着したり収縮して、その多孔性を保持されない から如何に多孔性を保持するかがポイントである。 It is conceivable that the water vapor or the generated gas of the aqueous emulsion penetrates the melted film and becomes porous, but when the film is cooled and taken out, it sticks or shrinks, and the porosity is not maintained. The point is to maintain the porosity.

特公昭38−26872、特公昭51−1899 1等に於て高い結晶性ポリマーを融点より10℃ 〜40℃高い温度で延伸して熱固定することによ り多孔性フイルムを得ることが記載している。高 重合ポリマーを高温で延伸することにより、フイ ルムの結晶の機械学的配置が乱れはじめ、大きな ひずみを受け、破損し易くなるが、結晶の高い重 合物はそのような方法で若干の通気性を得ること は知られている。今仮定として塩ビフイルムに高 度の不活性レジンを全面的に被膜した場合は延伸 のみで多孔性となる可能性はあるが、塩化ビニー ルフイルムの特有の柔軟性、風合、強度が失われ るばかりでなく経済的でない。本発明に於けるポ リアミド、ポリエステル、ポリアセタール、ポリ オレフィン類の高い結晶度を有するポリマーを点 熔融接着することにより、融点以上に熔融された 状体に於て、水蒸気或いはガスの突破により多孔 質となり又フイルムの癒着収縮を防止し又塩ビフ イルムの柔軟性を損なわないばかりでなく、塩ビ フイルムと基体との接着力は一般水溶性或いは溶 剤タイプ接着剤による接着力よりも熱熔融接着剤 を併用することに依り強化される。ポリアミド、 ポリオレフィン、ポリエステル、ポリアセタール 類の高い結晶度を有するポリマー粉末が塩化ビニ ールフイルムに熱熔着されることにより、柔軟な フイルムが固定化され冷却した場合収縮を防止し、 フイルム及びポリマーにあけられた通気孔の閉塞 を防ぐものと思われる。Japanese Patent Publication No. 38-26872 and Japanese Patent Publication No. 51-18991 describe that a highly crystalline polymer is stretched at a temperature 10 ° C. to 40 ° C. higher than the melting point and heat-set to obtain a porous film. ing. By stretching a highly polymerized polymer at high temperature, the mechanical arrangement of the crystal of the film begins to be disturbed, it is subject to large strain and is easily broken, but a polymer with a high crystal weight is slightly aerated by such a method. It is known to get sex. Assuming now, if a vinyl chloride film is entirely coated with a highly inert resin, it may become porous only by stretching, but the pliability, feel and strength peculiar to vinyl chloride film will be lost. Not only economical. By subjecting the polymer having high crystallinity such as polyamide, polyester, polyacetal, and polyolefins in the present invention to spot fusion bonding, in the state of being melted to a temperature higher than the melting point, the porous body is formed by the breakthrough of water vapor or gas. Not only does it prevent adhesion shrinkage of the film and does not impair the flexibility of the vinyl chloride film, but the adhesive strength between the vinyl chloride film and the substrate is generally higher than that of a water-soluble or solvent-type adhesive. It is strengthened by using together. Polymer powders of polyamide, polyolefin, polyester, and polyacetals with high crystallinity are heat-welded to vinyl chloride film to immobilize the flexible film and prevent it from shrinking when cooled, and it is opened in the film and polymer. It seems to prevent the blockage of the ventilation holes.

第1図によりその製造行程を説明する。繊維基 体1がタイコロール2の上辺を通り、耐熱ゴム無 限ベルト7に入る前に、先ず水性エマルジョン塗 付機3により水性エマルジョンを塗付され、次に 静電ロールで構成された熱熔融ポリマー粉末散布 機4によりパウダーを全面に散布する。一方塩化 ビニールフイルム6はタイコロール5を通り、前 記繊維基体と接合されながら無限ベルト7に入っ て行く。遠赤外線又は電熱7により140℃〜1 00℃に加熱された無限ベルト内に於て10秒〜 40秒通過し、塩化ビニールフイルム6と基体1 とは接合し一体となり、次にプレスロール11に 於て加圧圧着され水冷ロール12により若干延伸 固化され巻取りロール13によって巻取られる。 The manufacturing process will be described with reference to FIG. Before the fiber substrate 1 passes through the upper side of the Tyco roll 2 and enters the heat-resistant rubber endless belt 7, the aqueous emulsion is first coated with the aqueous emulsion coating machine 3, and then the heat-melting is performed by the electrostatic roll. The powder is sprayed on the entire surface by the polymer powder spraying machine 4. On the other hand, the vinyl chloride film 6 passes through the tyrocolor 5 and enters the infinite belt 7 while being bonded to the above-mentioned fiber substrate. After passing through an infinite belt heated to 140 ° C to 100 ° C by far infrared rays or electric heat 7 for 10 seconds to 40 seconds, the vinyl chloride film 6 and the substrate 1 are bonded and integrated, and then the press roll 11 is formed. Then, it is pressure-bonded, slightly stretched and solidified by a water-cooling roll 12, and wound by a winding roll 13.

その間一体となったフイルムと基体は無限ベルト 7に沿って走り、上部にある無限ベルト7との間 には空間10があり、水性エマルジョンから蒸発 した水蒸気やガスは熔融フイルムを突破して逃げ る外無く多孔性フイルムを製造することができる。In the meantime, the integrated film and substrate run along the infinite belt 7, and there is a space 10 between the infinite belt 7 and the upper part, and water vapor and gas evaporated from the aqueous emulsion break through the molten film and escape. It is possible to produce a porous film without exception.

此の加熱機械は、温度、スピード、接着剤の量、 散布の量を適宜調整が可能である。 With this heating machine, the temperature, speed, amount of adhesive, and amount of spraying can be adjusted appropriately.

第2図は顕微鏡で見た通気性塩化ビニールフイ ルムの平面図であって、岐阜県繊維工業試験所に 於て撮影したものである。フイルム16内に点在 する熱熔融粉末14と無数にあけられた通気孔1 5とを示す。電子顕微鏡45倍に於ては熱熔融粉 末14のみ見れるが1000倍の倍率に於ては熱 熔融粉末14間に無数の通気孔15が見れている。 Figure 2 is a plan view of the breathable vinyl chloride film as seen through a microscope, taken at the Gifu Prefectural Textile Industry Laboratory. The hot-melt powder 14 scattered in the film 16 and innumerable vent holes 15 are shown. Under the electron microscope 45 times, only the hot melt powder 14 can be seen, but at 1000 times magnification, numerous vent holes 15 are seen between the hot melt powder 14.

8000倍の倍率に於ては通気孔の周りが程々ふ くらみがあり奥に更に微細な孔を見出だすことが 出来る。At a magnification of 8000 times, there is a slight bulge around the ventilation holes, and it is possible to find finer holes in the back.

以下本発明を具体的に実施例にて説明する。 The present invention will be specifically described below with reference to examples.

実施例1、 三菱化成ビニール製品サンプレーン 厚さ0.08m/m 巾92cm 抗張力165kg/cm2 伸び350% 直角引裂力25kg/cm2 100%モジュラス55kg/cm2 基 布 30×20ナイロンハーフ 桐生トリコット製 接着剤 酢酸ビニール、エチレン、メチロールア クリル共重合エマルジョン50%液 1000g 接着熱熔融パウダー ポリアミドNo.12 30g 両接着剤を水中分散液として吹付け130℃15 秒熱処理する。Example 1, Mitsubishi Kasei vinyl product sunplane Thickness 0.08 m / m Width 92 cm Tensile strength 165 kg / cm 2 Elongation 350% Right angle tearing force 25 kg / cm 2 100% Modulus 55 kg / cm 2 Base cloth 30 × 20 Nylon half Kiryu tricot Adhesive made vinyl acetate, ethylene, methylol acrylate copolymer emulsion 50% liquid 1000 g Adhesive hot melt powder Polyamide No. 12 30 g Both adhesives are sprayed as dispersion in water and heat treated at 130 ° C for 15 seconds.

通気度 0.21cm3/cm2/sec JIS.L1096.6.27.1A法 耐水度 1000cm以上 JIS.L102.5.1.1A法 磨耗強さ 331回 JIS.L1096.6.17.1A法 浸透度 150g/m/24h JIS.Z0208 実施例2 同じフイルムと基体の接着に於て水性エマルジ ョンに炭酸水素アンモニウム重量比1%を含ませ 加工した。(エマルジョン50%液1000g・ 炭酸水素アンモン10g・水200g)にて吹付 けた。Air permeability 0.21 cm 3 / cm 2 / sec JIS. L1096.6.27.1A method Water resistance 1000 cm or more JIS. L102.5.1.1 A method Abrasion strength 331 times JIS. L1096.6.17.1A method Penetration 150 g / m 2 / 24h JIS. Z0208 Example 2 An aqueous emulsion containing 1% by weight of ammonium hydrogen carbonate was processed for adhesion of the same film and substrate. It was sprayed with (1000 g of 50% emulsion, 10 g of ammonium bicarbonate and 200 g of water).

通気度 0.58cm3/cm2/sec JIS.L1096.6.27A法 実施例1より通気性に於て約3倍増加した。Air permeability 0.58 cm 3 / cm 2 / sec JIS. L1096.6.27A method The air permeability was increased by about 3 times as compared with Example 1.

実施例3 実施例1に於ては両接着剤を同一分散液として 吹付けたが、熱熔融ポリマーの量に制限される為、 先ず水溶性エマルジョンを吹き付け次ぎに熱熔融 ポリマーを30g/m散布し、同様に130℃ 15秒加熱した。Example 3 In Example 1, both adhesives were sprayed as the same dispersion liquid, but since the amount of the hot-melt polymer is limited, first the water-soluble emulsion is sprayed and then the hot-melt polymer is added at 30 g / m 2 It was sprinkled and heated at 130 ° C. for 15 seconds in the same manner.

通気度0.42を示し実施例1より好結果を得た。The air permeability was 0.42, and the good result was obtained from Example 1.

実施例4 熱熔融ポリマーを酸ビエチレン共重合物にして 例3と同様の方法で実験した。Example 4 An experiment was conducted in the same manner as in Example 3 except that the hot-melt polymer was an acid-biethylene copolymer.

通気度0.39を示し大差が無かった。The air permeability was 0.39 and there was no great difference.

実施例5 熱熔融ポリマー、ポリアミド12のみにて相当 多く30g/m散布した場合、通気度は0であ った。Example 5 The air permeability was 0 when a large amount of 30 g / m 2 was sprayed with only the hot-melt polymer and polyamide 12.

実施例6 上記水性エマルジョン液はガス発生量を多くす るため炭酸水素アンモン50g水400gエマル ジョン50%液500gにて吹付け接着加熱した。Example 6 In order to increase the amount of gas generated, the above aqueous emulsion liquid was spray-bonded and heated with ammonium bicarbonate 50 g, water 400 g, emulsion 50% liquid 500 g.

通気度は0であった。単独接着剤では通気性は出 来ないことが判明した。The air permeability was 0. It was found that breathability does not appear with a single adhesive.

実施例7 実施例1以下と同じフイルムを使用し基布の代 りに離型紙を使用した。加熱室を通過し冷却後離 型紙を剥がしフイルムを作製した。Example 7 The same film as in Example 1 was used, and release paper was used instead of the base fabric. After passing through the heating chamber and cooling, the release paper was peeled off to prepare a film.

熱熔融ポリマーにエチレン酸ビ重合物30g/m2 水性エマルジョンとして、炭酸アンモン50g水 400g、エマルジョン50%液1000gを塗 付した。To the hot-melt polymer, 50 g of ammonium carbonate, 400 g of water, and 1000 g of 50% emulsion were applied as an aqueous emulsion of 30 g / m 2 of ethylene acid bipolymer.

通気度 0.61cm3/cm2/sec JIS.L1096 耐水度 400cm以上 浸透度 800g/m/h JIS.Z0208 本発明による通気性塩化ビニールレザー、フイ ルムの製造法は高い結晶度を有する熱熔融ポリマ ー粉末とガス発生溶液とを同時に接着剤として作 用させ冷却後フイルム及びポリマーにあけられた 通気孔が癒着や収縮することが無い事が特徴であ って一部実施例を示したが固形粉末の種類、ガス 発生無機物の種類、フイルムの種類等、当業者が その変更修正または均等物を使用することが明ら かであるから、本発明の原則のなかの変更は特許 請求の範囲に含まれることを意図するものである。Air permeability 0.61 cm 3 / cm 2 / sec JIS. L1096 Water resistance 400 cm or more Penetration 800 g / m 2 / h JIS. Z0208 The method for producing a breathable vinyl chloride leather or film according to the present invention is a method in which a hot-melting polymer powder having a high crystallinity and a gas generating solution are simultaneously used as an adhesive agent, and after cooling, a vent hole is formed in the film and the polymer. Although some examples have been shown that there is no adhesion or contraction, those skilled in the art can use modifications or equivalents such as solid powder type, gas generating inorganic substance type, film type etc. Changes in the principles of the invention are intended to be within the scope of the following claims because it is obvious to do so.

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

第1図は本発明の方法で使用される装置の概略図 である。 第2図は電子顕微鏡で見た通気性塩化ビニールフ イルムの平面図である。 Aは倍率1000 Bは倍率8000 岐阜県繊維工業試験所撮影 FIG. 1 is a schematic diagram of an apparatus used in the method of the present invention. FIG. 2 is a plan view of the breathable vinyl chloride film as seen with an electron microscope. A is 1000 magnification B is 8000 magnification Taken by Gifu Textile Industry Laboratory

【手続補正書】[Procedure amendment]

【提出日】平3.8.13 (別紙1、第5頁19行と20行の間に挿入) 本発明に於ける熱熔融パウダーは1インチ平方に400
個〜4900個の範囲で撒布する。撒布量は概算式、2
5.4−ax=bx′により算定する。xは1インチに
於けるパウダーの数、aはパウダーの直径、bは要求す
る通気孔の直径である。上式に於ける25.4−axは
1インチ内に撒布されたパウダー内の空間の總計、b
x′のx′は空間の数でx=x′と見倣す。例へば50
μの通気孔を要求する場合パウダーの直径が0.5mmと
すれば上式により25.4−0.5x=0.05xとな
るからx=46インチ当り46の二乗となる。25.4
=x(2a+0.05)、現在市場で一般に使用されて
いるパウダー1インチ当り38コ×38コ=1444コ
を例にとれば、b=0との接点は0.67mmとなる。
0.67mmのパウダーを融着した場合0.05mmの孔を
形成しようかと思へば0.67−0.05=0.62と
なり圧力と加熱によってパウダーの高さが0.1mmとな
るとすればパウダーの底辺面積は約2倍となるから0.
62÷2=0.31となり0.05mmの孔形成には0.
31mmのパウダー径を必要とすることになる。このよう
にしてパウダーの直径を計算することが出来る。パウダ
ーの量及び直径が既存製品を使用する場合は例へば1イ
ンチ38コパウダーの直径0.25の場合は通気孔b=
25.4−2axの式から計算してb=0.17とな
る。170Uの孔は耐水性に缺ける為塩化ビニールフィ
ルムとしては適切でないからいかにして10ミクロン以
下の孔にすべきかが問題となる。その点に関して以下説
明する。計算されたパウダー量及び直径に於いては加熱
温度及び時間に余り関係なく、後述するフィルム破損線
以上に於いても通気孔の形成は容易である。又いつでも
安心して一定の通気孔を得ることが出来る。フィルムに
融着されたパウダーの部分はフィルムの厚さより厚く、
フィルムの部分は加熱により早く熔融されて表面張力の
作用により収縮しようとして無数の孔を発生するのであ
る。正確に計算されたb即ち空間は高温により完全に熔
融されても通気孔が10U以上にはならないので目的の
達成はコンスタントで而も容易である。フィルムの耐水
性を無視して唯単に多孔性にすることは加熱と圧力によ
ってフィルム破損線内に於いては可能であるがあくまで
塩化ビニールの本命は耐水力であるから如何にして水の
透らないしかも通気性のあるフィルムを作るかが問題な
のである。破壊点はフィルムの軟化点、種類特に可ソ剤
の量、厚さ、繊維基体の種類特にメッシュの状体、プレ
ス圧力、接着剤の種類量、ガス発生無機塩の種類量等に
より千差万別である。一例を示したのがある条件のある
フィルムのものである。170℃で10秒、160℃で
18秒、150℃で25秒、140℃で40秒、130
℃で55秒、120℃で75秒、110℃で100秒と
なりその点を連結したのがそのフィルムの破損線であ
る。その線の左側に於いてはフィルムは破壊せず、その
内側に於いては10U孔形成線5U形成線等を実験によ
り選定することが出来る。しかし破損線の選定は一般の
機械では殆んど不可能である。加熱温度と時間の正確な
サーモスタット、ON.OFF時のオーバーシュート、
アンダーシュートによる温度の不安定要素を払出したと
ころの最近のエレクトロニクスとメカトロニクスをとり
入れた装置でなければ困難で一般のラミネートマシン、
コーチングマシンは適切でない。離型ベルトに入った当
初の水分を含んだ塩ビフィルムと基体が進行後乾燥して
加熱温度が変化するようでは一定のデータは出て来な
い。いつでもどこでも一定のデータを必要とするのであ
る。フィルム破損線の選定が出来れば、5μ形成線の選
定を行い、高温低時間がよいか、低温長時間がよいか、
適切なる点を選定すべきで、各種条件により種々の結果
が出るから、この線と点の選定は加工段階に於いて重要
なることである。実験の結果によればパウダー量及び径
が計算通りの場合は低温長時間がよいが、一般には高温
短時間で加工すれば加熱後つまり孔形成後の収縮を防止
することになる。孔の大きさが250μとなった場合如
何にして10μ以下にすべきかであるが先づプレス圧力
を減らすこと。基布を平滑なものに代へること等を試験
して、最も大切なことは温度と時間の減少により数回の
実験をして希望の通気孔を定むべきである。たとへ25
0μの大孔であってもパウダーにより固定された空間は
破壊点の内部に於いてはある温度時間に於いて無数の通
気孔を形成することが出来るのである。次に熱熔融パウ
ダーを使用しない場合に就いて簡単に説明する。基布が
平坦な紙の場合は10μ以下の通気孔形成は殆ど不可能
で、一般の繊維布地、不織布等に於いても困難である。
しかし繊維基体或いはエンボスロールに対して、パウダ
ーの場合の1インチ平方400コ内至4900コの而も
凹凸が直径0.6mm内至0.15mmに構成した場合に
は、通気孔の形成は可能であるが一般に孔が大きくなり
易いのは凸部分の接着力がパウダーに比べて弱く、フィ
ルムが収縮し易く、孔が閉塞するため小孔の形成が難し
いから、高温で処理さぜるを得ないことによる。しかし
本質的に25.4=x(a+b)、b=0.05の凹凸
ロールに於ては50μの孔を形成することが出来るの
で、本発明と本質的に同意であるから実施例に数例を示
した。塩化ビニールフィルム或いは他の熱可ソ性フィル
ムと基体とを接着した一般のフィルムシートを上記エン
ボスロールにより加圧して通気性フィルムを製造する事
が出来る。又孔径の大きすぎたフィルムに対して、フィ
ルム面にウレタン発砲樹脂溶液をコーチングしたり或い
は塩化ビニール樹脂溶液を通気孔をまったく閉塞しない
程度の薄い液状で吹付したりコーチングする事により通
気孔塩化ビニールを製造する事も可能である。耐洗濯性
を特に要求されるような塩化ビニールシートの加工に於
いてはm平方50g以上の接着剤を必要とするから接着
剤に炭酸アンモン等のガス発生剤を混入することは緊要
である。 別紙2 第10頁17行と18行の間に挿入 以下実施例8より実施例16迄表にして比較できるよう
にした。塩化ビニールフィルムは商品名アキレス、厚さ
80ミクロン可ソ剤50%、基材ナイロンハーフ30デ
ニール、固形粉末ポリアミド直径0.3mmインチ平方6
444コ、接着剤アクリル酷酸ビニール共重合エマルジ
ョン50%水溶液、ガス発生剤炭酸水素アンモン2%重
[Date of submission] Flat 3.8.13 (Attachment 1, page 5, inserted between lines 19 and 20) The hot-melt powder in the present invention is 400 in 1 inch square.
Spread in the range of 4900 pieces. The spread amount is an approximate formula, 2
Calculated according to 5.4-ax = bx '. x is the number of powders per inch, a is the powder diameter, and b is the required vent hole diameter. In the above formula, 25.4-ax is the total amount of space in the powder scattered within 1 inch, b
x'of x'is the number of spaces and is imitated as x = x '. Example 50
In the case of requesting a ventilation hole of μ, if the diameter of the powder is 0.5 mm, 25.4-0.5x = 0.05x is obtained from the above equation, so that x = 46 squared per 46 inches. 25.4
= X (2a + 0.05), for example, 38 x 38 x 1444 per 1 inch of powder that is generally used in the market today, the contact point with b = 0 is 0.67 mm.
When fusing 0.67 mm powder, it is necessary to form a 0.05 mm hole. If it becomes 0.67-0.05 = 0.62, and if the powder height becomes 0.1 mm due to pressure and heating, The bottom area of the powder is about double, so
62 ÷ 2 = 0.31, which is 0.
You will need a powder diameter of 31mm. In this way the diameter of the powder can be calculated. If the amount and diameter of the powder used is an existing product, for example, if 1 inch 38 co-powder has a diameter of 0.25, the ventilation hole b =
Calculated from the formula of 25.4-2ax, b = 0.17. Since the 170 U hole is water resistant, it is not suitable as a vinyl chloride film, so there is a problem how to make a hole of 10 μm or less. This point will be described below. In the calculated powder amount and diameter, there is no relation to the heating temperature and time, and it is easy to form the ventilation holes above the film break line described later. Also, you can always get a certain amount of ventilation holes with peace of mind. The part of the powder fused to the film is thicker than the thickness of the film,
The film portion is rapidly melted by heating, and countless holes are generated to shrink due to the effect of surface tension. Even if the accurately calculated b, that is, the space is completely melted at a high temperature, the number of ventilation holes does not exceed 10 U, so that the achievement of the object is constant and easy. It is possible to make the film porous by ignoring the water resistance of the film within the line of damage of the film by heating and pressure, but since the favorite of vinyl chloride is the water resistance, it is difficult to see how water can pass through. The problem is how to make a film that is not breathable. The breaking point varies depending on the softening point of the film, the type, particularly the amount and thickness of the solvent, the type of the fiber substrate, especially the mesh body, the pressing pressure, the type of the adhesive, the amount of the gas generating inorganic salt, etc. It's another. An example is for a film with certain conditions. 170 ° C for 10 seconds, 160 ° C for 18 seconds, 150 ° C for 25 seconds, 140 ° C for 40 seconds, 130
The film was broken at 55 ° C., at 120 ° C. for 75 seconds, at 110 ° C. for 100 seconds, and the points are connected to each other, and the broken line of the film is obtained. On the left side of the line, the film does not break, and on the inside, a 10U hole forming line and a 5U forming line can be selected by experiments. However, the selection of the broken line is almost impossible with general machines. An accurate thermostat of heating temperature and time, ON. Overshoot when off,
A general laminating machine, which is difficult unless it is a device that incorporates recent electronics and mechatronics where the unstable element of temperature due to undershoot is taken out,
Coaching machine is not suitable. If the initial PVC film containing water and the substrate that entered the release belt are dried and the heating temperature changes, certain data cannot be obtained. It requires constant data anytime, anywhere. If the film damage line can be selected, select the 5μ forming line, and whether the high temperature and low time are good, or the low temperature and long time are good,
The selection of this line and point is important at the processing stage, because appropriate points should be selected and various results will be obtained under various conditions. According to the result of the experiment, when the powder amount and diameter are as calculated, low temperature and long time are preferable, but generally, high temperature and short time processing can prevent shrinkage after heating, that is, after hole formation. When the size of the hole becomes 250μ, how to make it less than 10μ is to reduce the pressing pressure first. It should be tested to replace the base cloth with a smooth one, and most importantly, several experiments should be conducted by decreasing the temperature and time to determine the desired ventilation hole. Tato 25
Even if the pore size is 0 μ, the space fixed by the powder can form innumerable vent holes inside the breaking point at a certain temperature and time. Next, a brief description will be given of the case where the hot-melt powder is not used. When the base cloth is a flat paper, it is almost impossible to form air holes having a diameter of 10 μm or less, and it is also difficult to use general fiber cloth, non-woven cloth and the like.
However, it is possible to form ventilation holes on the fiber substrate or embossing roll when the powder is 1 inch square 400 to 4900 indentations with a diameter of 0.6 mm to 0.15 mm. Generally, however, pores tend to be large because the adhesive strength of the convex part is weaker than that of powder, the film tends to shrink, and it is difficult to form small holes because the pores are blocked, so it is necessary to treat at high temperature. It depends. However, since it is possible to form a hole of 50 μ in an uneven roll of 25.4 = x (a + b) and b = 0.05, it is essentially the same as the present invention, and therefore, it is not included in the examples. An example was given. A general film sheet in which a vinyl chloride film or another thermosetting film and a substrate are adhered can be pressed by the embossing roll to produce a breathable film. For a film with too large a hole diameter, a urethane foam resin solution is coated on the film surface, or a vinyl chloride resin solution is sprayed or coated as a thin liquid that does not block the air holes. It is also possible to manufacture When processing a vinyl chloride sheet which is particularly required to have washing resistance, it is necessary to mix an adhesive with a gas generating agent such as ammonium carbonate, since an adhesive of m square 50 g or more is required. Attachment 2 Inserted between page 17, lines 17 and 18 The following examples 8 to 16 are tabulated for comparison. The vinyl chloride film is trade name Achilles, thickness 80 micron, 50% softener, base nylon half 30 denier, solid powder polyamide diameter 0.3 mm inch square 6
444, adhesive 50% acrylic acid vinyl acrylate copolymer aqueous solution, gas generating agent ammonium hydrogen carbonate 2% weight

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】通気性塩化ビニールレザー及びフイルムを 製造するために、直接フイルムに孔をあける方法 ではなく、繊維基体との接着行程に於て通気性を 附与する方法であって、繊維基体又は塩化ビニー ルフイルムの中間面に2種の接着剤を塗付する、 1種は熱熔融接着粉末、ポリアミド、ポリエステ ル、ポリアセタール、ポリオレフィン類中高い結 晶度を有し而もポリ塩化ビニールと大差無い融点 のポリマー粉末を、1種は炭酸水素アンモン、塩 化アンモン、炭酸ナトリウム等ガスを発生し易い 無機塩の少くとも一つを含有する水性エマルジョ ン或いは溶剤タイプ接着剤とを、個々別々に又は 混合分散液として塗付し、該熔融ポリマーの融点 以上の温度140℃〜100℃、10秒〜40秒、 加熱熔融し両者を接着して塩化ビニールレザーを 製造する方法。1. A method for providing breathability in a bonding process with a fiber substrate, not a method of directly making holes in the film for producing breathable vinyl chloride leather and film, the method comprising: Or, apply two kinds of adhesives on the intermediate surface of vinyl chloride film. One kind has a high crystallinity in hot-melt adhesive powder, polyamide, polyester, polyacetal, and polyolefins, and is very different from polyvinyl chloride. Polymer powders with no melting point, one with water-based emulsion containing at least one inorganic salt that easily generates gas such as ammonium hydrogen carbonate, ammonium chloride, and sodium carbonate, or solvent-type adhesive, separately. Alternatively, it is applied as a mixed dispersion liquid, and the temperature is not lower than the melting point of the molten polymer 140 ° C. to 100 ° C. for 10 seconds to 40 seconds. A method of manufacturing the Rureza. 【請求項2】繊維基体の代りに離型性シートを用い冷却
後 該シートを離脱して通気性フイルムを製造する方 法
2. A method for producing a breathable film by using a releasable sheet instead of a fibrous substrate and cooling the sheet to release the sheet.
JP14495090A 1990-06-01 1990-06-01 Production of air permeable vinyl chloride leather and film Pending JPH083878A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14495090A JPH083878A (en) 1990-06-01 1990-06-01 Production of air permeable vinyl chloride leather and film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14495090A JPH083878A (en) 1990-06-01 1990-06-01 Production of air permeable vinyl chloride leather and film

Publications (1)

Publication Number Publication Date
JPH083878A true JPH083878A (en) 1996-01-09

Family

ID=15373963

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14495090A Pending JPH083878A (en) 1990-06-01 1990-06-01 Production of air permeable vinyl chloride leather and film

Country Status (1)

Country Link
JP (1) JPH083878A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6333211B1 (en) 1998-08-26 2001-12-25 Shinko Electric Industries, Co., Ltd. Process for manufacturing a premold type semiconductor package using support pins in the mold and external connector bumps
US6489668B1 (en) 1997-03-24 2002-12-03 Seiko Epson Corporation Semiconductor device and method for manufacturing the same
CN104746355A (en) * 2015-03-31 2015-07-01 无锡市曼优丽新型复合材料有限公司 Method for producing double-sided leather and special compound equipment thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6489668B1 (en) 1997-03-24 2002-12-03 Seiko Epson Corporation Semiconductor device and method for manufacturing the same
US6333211B1 (en) 1998-08-26 2001-12-25 Shinko Electric Industries, Co., Ltd. Process for manufacturing a premold type semiconductor package using support pins in the mold and external connector bumps
US6577000B2 (en) 1998-08-26 2003-06-10 Shinko Electric Industries Co., Ld. Premold type semiconductor package
CN104746355A (en) * 2015-03-31 2015-07-01 无锡市曼优丽新型复合材料有限公司 Method for producing double-sided leather and special compound equipment thereof

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