JPH0214888B2 - - Google Patents
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- JPH0214888B2 JPH0214888B2 JP57192661A JP19266182A JPH0214888B2 JP H0214888 B2 JPH0214888 B2 JP H0214888B2 JP 57192661 A JP57192661 A JP 57192661A JP 19266182 A JP19266182 A JP 19266182A JP H0214888 B2 JPH0214888 B2 JP H0214888B2
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Description
本発明は通気性複合材を製造する方法に関する
ものであり、更に詳しくは、布製基材の片面に塩
化ビニル系樹脂よりなる多数の通気性の小孔を有
むる樹脂層の形成された通気性複合材を、製造す
る方法の改良に関するものである。
合成樹脂よりなるフイルム又はシートは、広く
各種の製品に対する装飾用および耐摩耗性カバー
として広く使用されている。これらのフイルム又
はシートは、例えば壁、床および卓上カバー、ブ
ツクカバー、内張り、衣類および自動車内部用の
クロース用として広く使用されている。多くの場
合、合成樹脂よりなるフイルム又はシートは、繊
維品、紙、フエルト、金属、木等のような裏地上
に被覆される。これら裏地物質は多くの目的を有
し、その最も普通の目的は、製品の強度及び効用
を増加し、フイルム又はシートを固定する接着剤
を受け入れることにある。合成樹脂よりなるフイ
ルム又はシートとこれらを支持する裏地物質と
を、接着剤によつて接着すると、裏地物質の特徴
を損ない、接着剤使用による欠点が表われるとい
つた問題があつた。
本発明者らは、合成樹脂よりなるフイルム又は
シートと布製基材とよりなる複合材とする際に、
裏地となる布製基材の通気性、クツシヨン性、手
ざわりを余り犠牲にしない、工業的有利な製造方
法を提供することを目的として鋭意検討した結
果、本発明を完成するに至つたものである。
しかして本発明の要旨とするところは、乳化重
合法、又は微細懸濁重合法によつて得られた重合
体乳濁液を乾燥して得られた平均粒子径が5〜50
ミクロンの塩化ビニル系樹脂を、可塑剤とともに
水に分散し、この分散液を布製基材の片面に塗布
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+(150−可塑剤添加部数) …()
〔()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100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、溶融して樹脂粒子
表面同志を溶着させ、かつ、布製基材と付着させ
たのち、冷却することを特徴とする通気性複合材
の製造方法に存する。
以下、本発明を詳細に説明する。
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と
しては、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酸及びこれらのエ
ステル類、ならびに無水マレイン酸、芳香族ビニ
ル化合物、ハロゲン化ビニリデン化合物、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。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
たものであつてもよい。
上記塩化ビニル系樹脂は、乳化重合法又は微細
懸濁(マイクロサスペンジヨン)重合法によつて
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、布製基
材上に通気性樹脂層を形成するのに好適である。
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。乳化重合法によつて得られる樹脂
乳濁液を、例えば噴霧乾燥法により乾燥すると、
平均粒子径が2ミクロン以下の微小粒子が多数凝
集しあい、平均粒子径が5ミクロンないし40ミク
ロンの多孔質の粒子が形成される。微細懸濁重合
法によつて得られる樹脂は、平均粒子径が20ミク
ロンないし40ミクロンで、この樹脂も乾燥時に数
個の粒子が凝集し合うが、凝集する性質は乳化重
合法によつて製造したものほど強くはない。
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。平均粒子径が50ミクロン以上で
あると、最終的に得られる複合材の通気性樹脂層
の強度、通気性を好ましく調節するのが難かし
く、これら性質が均衡した樹脂層を安定して得る
ことができない。最終的に得られる樹脂層の通気
性は、使用する塩化ビニル系樹脂粒子の平均粒子
径によつて変わる。塩化ビニル系樹脂は、平均粒
子径が50ミクロン以下で5ミクロン以上のものか
ら選択使用可能であり、ほぼ均一な平均粒子径の
もの用いても、異なる平均粒子径のものを二種以
上組み合せて用いてもよい。なお、原料の塩化ビ
ニル系樹脂は、最終的に得られる通気性樹脂層の
通気量、強度、感触などによつて、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、種々選ぶことがで
きる。
本発明によるときは、上記塩化ビニル系樹脂粉
末を、可塑剤とともに水に分散し、可塑剤を塩化
ビニル系樹脂粉末に吸収させる。
この際用いることができる可塑剤としては、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、ジイソデシルフタレート、ジドデシルフタレ
ート、ジウンデシルフタレート等のフタル酸エス
テル類;アジピン酸ジオクチル、アジピン酸ジ−
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;ペンタエリスリトールエステ
ル、ジエチレングリコールジベンゾエート等のグ
リコールエステル類;アセチルリシノール酸メチ
ル等の脂肪酸エステル類;トリクレジルホスフエ
ート、トリフエニルホスフエート等のりん酸エス
テル類;エポキシ化大豆油、エポキシ化アマニ油
等のエポキシ化油;アセチルトリブチルシトレー
ト、アセチルトリオクチルシトレート、トリーn
−ブチルシトレート等のクエン酸エステル類;ト
リアルキルトリメリテート、テトラ−n−オクチ
ルピロメリテート、ポリプロピレンアジペート、
その他ポリエステル系等の種々の可塑剤があげら
れる。これら可塑剤は一種類でも、二種類以上を
組み合せて用いてもよい。可塑剤の量は、塩化ビ
ニル系樹脂100重量部に対して、20〜70重量部の
範囲内で選ぶことができる。
塩化ビニル系樹脂粉末と可塑剤とを水に分散さ
せるためには、分散剤を用いる。分散剤として使
用可能なものは、通常界面活性剤として知られて
いるものでよい。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ような両性界面活性
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。
上記分散剤は、塩化ビニル系樹脂と可塑剤との
合計量に対して、0.1〜5.0重量%の範囲で使用す
ればよい。
塩化ビニル系樹脂粉末と可塑剤とを、水に分散
させるには、これら二成分を分散剤を溶解した水
に加え、撹拌混合する。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20〜
80重量%の範囲とする。固形分の濃度が、この範
囲より低かつたり、逆に高いときは、得られる通
気性樹脂層の厚さを調節するのが困難であり、好
ましくない。固形分の濃度は、上記範囲のうち40
〜60重量%の範囲が、特に好ましい。
分散液の撹拌混合は、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。撹拌混合する
際の温度は、50〜80℃の温度とするのがよい。塩
化ビニル系樹脂粉末に、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樹
脂層表面に亀裂が生ずる。従つて、塩化ビニル系
樹脂粉末に吸収させる可塑剤量は、配合した可塑
剤の一部、望ましくは約半分とし、残りは吸収さ
れずに水に分散している状態とするのがよい。こ
のようにするには、水に可塑剤の全量を加えて撹
拌強度、撹拌時間等を変えて、塩化ビニル系樹脂
粉末へ吸収させる量を調節する方法、まず可塑剤
の約半分を加えてこれを塩化ビニル系樹脂粉末へ
ほぼ吸収させ、残りの可塑剤を水に加えて分散さ
せる方法等をとればよい。
水に塩化ビニル系樹脂と可塑剤を分散させる際
に使用しうる撹拌混合機は、液体に固体を分散す
る目的で従来から使用されている撹拌混合機であ
つてよい。
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、防カビ剤、
香料等を少量添加、混合することができる。
上記分散液を撹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があ
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、フイルターを用いて除去するの
が好ましい。
本発明によるときは、上記方法で調製した分散
液を、布製基材の片面に塗布する。布製基材は、
フエルト状シート、織つたり、編んだ繊維製品を
いう。織り方は、平織、あや織、朱子織、斜文
織、紗織、絽織等のいずれであつてもよい。編み
方は、メリヤス編み、レース編み等のいずれであ
つてもよい。繊維の原料は、植物性繊維のほか、
動物性繊維、合成繊維及びこれらの混合物であつ
てもよい。アスベストのような鉱物性繊維であつ
てもよい。特に好ましいのは、直径の細い糸によ
つて、平織、あや織、朱子織等によつて織つたも
のである。
分散液を布製基材に塗布して塗布膜を形成する
には、スプレイコート法、ロールコート法、グラ
ビアコート法、リバースコート法等のそれ自体公
知の各種塗布方法のいずれかによればよい。
布製基材の片面に形成する塗布膜の厚さは、次
の加熱、溶融工程終了後の通気性複合材の通気性
を犠牲にしないように、調節するのがよい。
本発明によるときは、上記方法で形成した塗布
膜を、加熱して塗布膜中に含まれる水分を揮散さ
せ、次いで樹脂粒子の表面を溶融させて粒子相互
を溶着させ、同時に布製基材にも付着させる。塗
布膜中の水分の揮散、樹脂粒子の表面付着を急激
に行なうと、最終的に得られる複合材の通気性樹
脂層表面に多数の小さな亀裂が生ずることが多
い。この小さな亀裂の生成を防止するために、樹
脂粒子表面を溶融させるための加熱を行なう前
に、40〜100℃の温度範囲で、5分以内の加熱を
行なう予備乾燥を行ない、塗布膜中の水分の可成
りの割合を、揮散させるのがよい。
塗布膜は、上記の予備乾燥を行ない、又は行な
わずに、加熱し、水分をほぼ完全に揮散し、樹脂
粒子表面を溶融させて、相隣り合う粒子同志を溶
着させ、更に布製基材にも付着させる。この際の
加熱温度は、余り低すぎると長時間加熱しても、
樹脂粒子表面が溶融しないので、強度の優れた通
気性樹脂層が得られず、好ましくない。
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
る可塑剤の量によつて変わることがわかつた。
すなわち、加熱、溶融する際の温度は、次の
()式、
Tg+(150−可塑剤添加部数) …()
〔()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100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とするのがよいことが分つ
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樹脂層が得られない。加
熱、溶融する際の下限温度は、上記()式で表
わされる温度より約50℃低い温度である。
加熱、溶融の操作は、上記()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、最終的に得られる通気性樹脂層に多
数の小さな亀裂が生ずることが多い。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
の操作を行なう前に、40〜80℃の温度で5分以内
加熱する予備乾燥操作を行なつて、塗布膜に含ま
れる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。
本発明によるときは、上記方法で得られる通気
性複合材を、常温付近まで冷却し、ロール状に巻
き取る。
なお、通気性複合材を冷却する途中で、又は冷
却したのちに、この複合材の片面又は両面に、シ
リコーンオイル、シリコーンエマルジヨン等の撥
水性物質を塗布すると、通気性複合材に撥水性を
付与することができる。
本発明方法によつて得られる通気性複合材の樹
脂層には、通常の軟質プラスチツクフイルムと同
様に、グラビア印刷、スクリーン印刷、フレキソ
印刷、発泡印刷、谷染め印刷等それ自体公知の各
種印刷法で印刷が可能である。本発明方法によつ
て得られる通気性複合材は、例えば卓上カバー、
ブツクカバー、物品収納箱内張り、椅子張り用ク
ロス、自動車内部用クロス、オムツカバー、雨具
等の用途に、好適である。
本発明は、次のように特別に顕著な効果を奏
し、その産業上の利用価値は、極めて大である。
(1) 本発明方法によるときは、0.01〜0.5mmの範
囲の厚さを通気性塩化ビニル系樹脂層をもつた
複合材を、容易に製造することができる。
(2) 本発明によつて得られた複合材は、通気性樹
脂層が布製基材に接着剤を介さずに一体に付着
されているので、製作が容易である。
(3) 本発明方法によつて得られる複合材は、樹脂
層が、軟質で、かつ、これを構成する樹脂粒子
が相隣り合う粒子との間で空隙を形成し、この
空隙が樹脂層の一方の側から布製基材の側に連
通している。よつて、このままオムツカバー、
雨具等の用途に使用しても湿気が飛散されやす
く、蒸れることがない。
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、
以下の例に限定されるものではない。
実施例 1
乳化重合法によつて製造し、噴霧乾燥法で乾燥
したポリ塩化ビニル粉末(平均重合度1100、ガラ
ス転移点約80℃、平均粒子径10ミクロンのもの)
を50重量%、水47重量%及びドデシルベンゼンス
ルホン酸ソーダ(DBS)3重量%の割合よりな
る三成分を混合し、混合液Aを調製した。
一方、ジオクチルフタレート65重量%、水32重
量%及びDBS3重量%の割合よりなる三成分を混
合し、混合液Bを調製した。
混合液Aと混合液Bとを重量比で2.6対1の割
合で混合し、分散液を得た。この分散液の固形分
は55.8重量%、ポリ塩化ビニル100重量部に対す
る可塑剤添加部数は、50重量部である。
上記分散液を、市販されているナイロン織布
(直径70ミクロンの糸で平織したもの。孔の大き
さ200ミクロン。)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。
この塗布膜を形成したナイロン織布を、80℃に
調節した熱風炉に3分間放置して、塗布膜の予備
乾燥を行なつた。続いて、この塗布膜付きのナイ
ロン織布を170℃に調節した熱風炉に1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、同時にナイロン織布表
面とも一体に付着させた。
上の加熱、溶融の操作終了後、冷却し、片面に
厚さ(布製基材の孔部分に浸透した部分は無視
し、基材の上に形成された樹脂層の厚さをいう。)
約0.1mmの通気性樹脂層の形成された通気性複合
材を得た。
得られた通気性複合材につき、樹脂層の平均孔
径、複合材の平均通気量、複合材の透湿度等を、
次の方法に従つて測定した。測定結果を、第1表
に示す。
樹脂層の平均孔径……電子顕微鏡により測定し
た。
複合材の平均通気量……複合材の一方の側から窒
素ガスを0.5Kg/cm2の圧力で送り、1平方セン
チメートル当り1分間の通気量を算出した。
300mm幅の複合材につき、幅方向に5カ所測定
し、平均したもの。
複合材の透湿度……JIS Z0208に準拠した。
実施例 2
実施例1に記載の例におけるポリ塩化ビニル
を、乳化重合法によつて製造し、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5重量%、ガラ
ス転移点約70℃、平均粒子径25ミクロン)に代え
たほかは、同例記載の方法と同様の手順で、分散
液を調製した。
得られた分散液を、実施例1で用いたと同種の
ナイロン織布に、同例に記載したと同様にして塗
布し、塗布膜の予備乾燥を行なつた。続いて、こ
の塗布膜付きのナイロン織布を、金属板上に載置
し、80℃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つた。続いて、この塗布膜
付きのナイロン織布を、金属板に載置したまま、
160℃に調節した熱風炉で1分間留めて、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、同時にナイロン織布表面とも一体に
付着させた。
上の加熱、溶融の操作終了後、冷却し、片面に
厚さ(定義は、実施例1の場合に同じ)約0.1mm
の通気性樹脂層の形成された通気性複合材を得
た。
得られた通気性複合材につき、実施例1に記載
の方法で、諸性質を測定した。結果を、第1表に
示す。
比較例 1
実施例1に記載の例において、塗布膜の加熱、
溶融の操作条件を、200℃の温度としたほかは、
同例に記載の方法と同様の操作手順で、複合材を
製造した。
得られた複合材につき、実施例1に記載の方法
で、諸性質を測定した。結果を、第1表に示す。
比較例 2
実施例2に記載の例において、塗布膜の加熱、
溶融の操作条件を、190℃としたほかは、同例に
記載の方法と同様の操作手順で、複合材を製造し
た。
得られた複合材につき、実施例1に記載の方法
で諸性質を測定した。結果を、第1表に示す。
The present invention relates to a method for producing a breathable composite material, and more specifically, the present invention relates to a method for producing a breathable composite material, and more specifically, a breathable composite material in which a resin layer made of vinyl chloride resin and having a large number of small breathable pores is formed on one side of a cloth base material. The present invention relates to improvements in methods for manufacturing composite materials. Films or sheets made of synthetic resins are widely used as decorative and wear-resistant covers for a wide variety of products. These films or sheets are widely used, for example, for wall, floor and tabletop coverings, book covers, linings, clothing and automotive interior coverings. Often, films or sheets of synthetic resin are coated onto backings such as textiles, paper, felt, metal, wood, and the like. These backing materials have many purposes, the most common being to increase the strength and utility of the product and to accommodate the adhesive that secures the film or sheet. When a synthetic resin film or sheet is bonded to a backing material that supports the film or sheet using an adhesive, there is a problem in that the characteristics of the backing material are impaired and disadvantages due to the use of the adhesive appear. The present inventors have discovered that when creating a composite material consisting of a film or sheet made of synthetic resin and a cloth base material,
The present invention was completed as a result of extensive research aimed at providing an industrially advantageous manufacturing method that does not significantly sacrifice the breathability, cushioning properties, and texture of the fabric base material that serves as the lining. However, the gist of the present invention is that the average particle size obtained by drying a polymer emulsion obtained by an emulsion polymerization method or a fine suspension polymerization method is 5 to 50.
Micron vinyl chloride resin is dispersed in water together with a plasticizer, this dispersion is applied to one side of a fabric base material to form a coating film, and this coating film is then calculated by the following formula (), that is, Tg + ( 150 - Number of parts of plasticizer added) ...() [In formula (), Tg means the glass transition point of the vinyl chloride resin, and number of parts of plasticizer added means the number of parts of plasticizer added to 100 parts by weight of the vinyl chloride resin. . ] The present invention relates to a method for producing a breathable composite material, which comprises heating and melting the resin particles at a temperature equal to or lower than the following to weld the surfaces of the resin particles together and adhering them to a cloth base material, and then cooling the resin particles. The present invention will be explained in detail below. In the present invention, the vinyl chloride resin refers to polyvinyl chloride and a copolymer mainly composed of vinyl chloride. Monomers that can be copolymerized with vinyl chloride include vinyl esters, vinyl ethers,
Examples include acrylic acid or methacrylic acid and their esters, maleic acid or fumaric acid and their esters, maleic anhydride, aromatic vinyl compounds, halogenated vinylidene compounds, acrylonitrile, methacrylonitrile, ethylene, propylene, etc. . These monomers may be partially crosslinked by adding a trace amount of a compound containing a polyfunctional group. The vinyl chloride resin used is one produced by an emulsion polymerization method or a microsuspension polymerization method. The vinyl chloride resins produced by these methods have a small average particle size and are suitable for forming an air-permeable resin layer on a fabric base material. 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. When a resin emulsion obtained by an emulsion polymerization method is dried, for example, by a spray drying method,
A large number of microparticles with an average particle diameter of 2 microns or less aggregate to form porous particles with an average particle diameter of 5 microns to 40 microns. The resin obtained by the micro-suspension polymerization method has an average particle size of 20 to 40 microns, and this resin also aggregates several particles together when dried, but the agglomeration property is different from that produced by the emulsion polymerization method. It's not as strong as what I did. 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 50 microns or more, it is difficult to properly adjust the strength and air permeability of the breathable resin layer of the final composite material, and it is difficult to stably obtain a resin layer with balanced properties. I can't. The air permeability of the resin layer finally obtained varies depending on the average particle diameter of the vinyl chloride resin particles used. Vinyl chloride resins can be selected from those with an average particle size of 50 microns or less and 5 microns or more, and those with an almost uniform average particle size can be used, or two or more types with different average particle sizes can be used in combination. May be used. In addition, the raw material vinyl chloride resin may be one or two types, a single resin (homopolymer), or A variety of materials can be selected, including a copolymer resin. According to the present invention, the vinyl chloride resin powder is dispersed in water together with a plasticizer, and the plasticizer is absorbed into the vinyl chloride resin powder. Plasticizers that can be used in this case include phthalate esters such as dioctyl phthalate, dibenzyl phthalate, butylbenzyl phthalate, dibenzyl phthalate, diisodecyl phthalate, didodecyl phthalate, and diundecyl phthalate; dioctyl adipate, diundecyl phthalate, etc.; −
Aliphatic dibasic acid esters such as n-butyl and dibutyl sebacate; glycol esters such as pentaerythritol ester and diethylene glycol dibenzoate; fatty acid esters such as methyl acetyl ricinolate; tricresyl phosphate and triphenyl phosphate. Phosphate esters such as; epoxidized oils such as epoxidized soybean oil and epoxidized linseed oil; acetyl tributyl citrate, acetyl trioctyl citrate, tri-n
- Citric acid esters such as butyl citrate; trialkyl trimellitate, tetra-n-octyl pyromellitate, polypropylene adipate,
Other examples include various plasticizers such as polyester plasticizers. These plasticizers may be used alone or in combination of two or more. The amount of plasticizer can be selected within the range of 20 to 70 parts by weight based on 100 parts by weight of the vinyl chloride resin. A dispersant is used to disperse the vinyl chloride resin powder and plasticizer in water. Dispersants that can be used include those commonly known as surfactants. 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; and nonionic surfactants such as polyoxyethylene alkyl ether and polyoxyethylene alkyl amine. The above-mentioned dispersant may be used in an amount of 0.1 to 5.0% by weight based on the total amount of vinyl chloride resin and plasticizer. To disperse the vinyl chloride resin powder and plasticizer in water, these two components are added to water in which the dispersant is dissolved and mixed by stirring. At this time, the ratio of water and solid content (sum of vinyl chloride resin and plasticizer) should be determined by adjusting the solid content concentration from 20 to 20 of the dispersion liquid (sum of water and solid content).
The range shall be 80% by weight. If the solid content concentration is lower or higher than this range, it is difficult to control the thickness of the resulting breathable resin layer, which is not preferable. The solid content concentration is 40% of the above range.
A range of 60% by weight is particularly preferred. The dispersion is stirred and mixed in order to absorb the plasticizer into the vinyl chloride resin powder. The temperature during stirring and mixing is preferably 50 to 80°C. If the vinyl chloride resin powder absorbs the entire amount of the blended plasticizer, cracks will occur on the surface of the finally obtained breathable resin layer. Therefore, it is preferable that the amount of plasticizer absorbed into the vinyl chloride resin powder be a portion, preferably about half, of the blended plasticizer, with the remainder not being absorbed but being dispersed in water. To do this, add the entire amount of plasticizer to water and change the stirring intensity, stirring time, etc. to adjust the amount absorbed into the vinyl chloride resin powder.First, add about half of the plasticizer and then A method may be used in which most of the plasticizer is absorbed into the vinyl chloride resin powder, and the remaining plasticizer is added to water and dispersed. The stirring mixer that can be used to disperse the vinyl chloride resin and plasticizer in water may be a stirring mixer that has been conventionally used for the purpose of dispersing solids in liquids. When preparing the dispersion, resin stabilizers, ultraviolet absorbers, fillers, dyes, pigments, flame retardants, fungicides,
A small amount of fragrance etc. can be added and mixed. When preparing the above dispersion using a stirring mixer, the dispersion may contain bubbles, gels, and lumps, so these should be removed using a vacuum defoamer, Hobart mixer, roll mill, or filter. is preferable. According to the present invention, the dispersion prepared by the above method is applied to one side of a fabric substrate. The fabric base material is
Refers to felt-like sheets, woven or knitted textile products. The weaving method may be any of plain weave, twill weave, satin weave, twill weave, gauze weave, and rug weave. The knitting method may be stockinette knitting, lace knitting, etc. In addition to vegetable fiber, the raw materials for fiber include
It may be animal fiber, synthetic fiber, or a mixture thereof. It may also be a mineral fiber such as asbestos. Particularly preferred are those woven with threads having a small diameter in plain weave, twill weave, satin weave, or the like. In order to form a coating film by applying the dispersion liquid to a fabric base material, any of various coating methods known per se, such as a spray coating method, a roll coating method, a gravure coating method, and a reverse coating method, may be used. The thickness of the coating film formed on one side of the fabric base material is preferably adjusted so as not to sacrifice the breathability of the breathable composite material after the subsequent heating and melting process. According to the present invention, the coating film formed by the above method is heated to volatilize the water contained in the coating film, and then the surface of the resin particles is melted to weld the particles to each other, and at the same time, the coating film is also applied to the cloth base material. Make it adhere. If water in the coating film evaporates rapidly and resin particles adhere to the surface, many small cracks often occur on the surface of the breathable resin layer of the final composite material. In order to prevent the formation of these small cracks, before heating to melt the surface of the resin particles, pre-drying is carried out by heating within a temperature range of 40 to 100°C for 5 minutes or less, and the It is advisable to volatilize a significant proportion of the water. The coating film is heated with or without the above pre-drying to volatilize the moisture almost completely, melt the surface of the resin particles, weld the adjacent particles together, and also coat the cloth substrate. Make it adhere. If the heating temperature at this time is too low, even if heated for a long time,
Since the surface of the resin particles does not melt, a breathable resin layer with excellent strength cannot be obtained, which is not preferable. According to experiments conducted by the present inventors, it has been 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 temperature during heating and melting is determined by the following formula (): Tg + (150 - number of parts of plasticizer added) ... () [In formula (), Tg is the glass transition point of the vinyl chloride resin, The number of parts means the number of parts of the plasticizer added to 100 parts by weight of the vinyl chloride resin. ] It was found that it is best to keep the temperature below the following. In addition, if the heating temperature is too low,
Since the surfaces of the resin particles do not melt even if heated for a long time, a breathable resin layer with excellent strength cannot be obtained. The lower limit temperature for heating and melting is approximately 50°C lower than the temperature expressed by the above formula (). 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 the above formula (), but if heating is performed rapidly at a high temperature, the final result will be Many small cracks often occur in the breathable resin layer. In order to prevent the formation of small cracks, before heating and melting, it is necessary to perform a pre-drying operation by heating at a temperature of 40 to 80°C for less than 5 minutes to remove the moisture contained in the coating film. After volatilizing a portion, heating and melting operations may be performed. According to the present invention, the breathable composite material obtained by the above method is cooled to around room temperature and wound into a roll. In addition, if a water-repellent substance such as silicone oil or silicone emulsion is applied to one or both sides of the composite material during or after cooling the composite material, the breathable composite material will become water-repellent. can be granted. The resin layer of the breathable composite material obtained by the method of the present invention can be formed by various printing methods known per se, such as gravure printing, screen printing, flexo printing, foam printing, and valley dyeing printing, as well as ordinary soft plastic films. It is possible to print with . The breathable composite material obtained by the method of the present invention can be used, for example, as a tabletop cover,
Suitable for uses such as book covers, linings for storage boxes, upholstery cloths, automobile interior cloths, diaper covers, rain gear, etc. The present invention has particularly remarkable effects as described below, and its industrial utility value is extremely large. (1) When the method of the present invention is used, a composite material having an air-permeable vinyl chloride resin layer with a thickness in the range of 0.01 to 0.5 mm can be easily produced. (2) The composite material obtained by the present invention is easy to manufacture because the breathable resin layer is integrally attached to the fabric base material without using an adhesive. (3) In the composite material obtained by the method of the present invention, the resin layer is soft, and the resin particles constituting the resin layer form voids between adjacent particles, and these voids form in the resin layer. One side communicates with the fabric base material side. So, leave the diaper cover as it is,
Even when used as rain gear, moisture is easily dispersed and it does not get stuffy. Hereinafter, the present invention will be explained in more detail based on Examples, but the present invention will not exceed the gist thereof.
It is not limited to the following examples. Example 1 Polyvinyl chloride powder produced by emulsion polymerization and dried by spray drying (average degree of polymerization 1100, glass transition point approximately 80°C, average particle size 10 microns)
A mixed solution A was prepared by mixing three components consisting of 50% by weight of DBS, 47% by weight of water, and 3% by weight of sodium dodecylbenzenesulfonate (DBS). On the other hand, a mixture B was prepared by mixing three components consisting of 65% by weight of dioctyl phthalate, 32% by weight of water, and 3% by weight of DBS. Mixed liquid A and mixed liquid B were mixed at a weight ratio of 2.6:1 to obtain a dispersion liquid. The solid content of this dispersion was 55.8% by weight, and the amount of plasticizer added was 50 parts by weight per 100 parts by weight of polyvinyl chloride. The above dispersion was applied to the surface of a commercially available nylon woven fabric (plain-woven with threads of 70 microns in diameter, pore size 200 microns) by a knife coating method to form a coating film. The nylon woven fabric on which the coating film was formed was left in a hot air oven adjusted to 80° C. for 3 minutes to pre-dry the coating film. Next, this coated nylon woven fabric was left in a hot air oven adjusted to 170°C for 1 minute to volatilize the moisture almost completely, and then the surface of the polyvinyl chloride powder particles was melted and the adjacent The particle surfaces were attached to each other, and at the same time, they were also attached integrally to the surface of the nylon fabric. After the above heating and melting operations are completed, it is cooled and one side is thickened (this refers to the thickness of the resin layer formed on the base material, ignoring the part that has penetrated into the pores of the fabric base material).
A breathable composite material having a breathable resin layer of about 0.1 mm was obtained. For the obtained breathable composite material, the average pore diameter of the resin layer, the average air permeability of the composite material, the moisture permeability of the composite material, etc.
It was measured according to the following method. The measurement results are shown in Table 1. Average pore diameter of resin layer: Measured using an electron microscope. Average airflow rate of the composite material: Nitrogen gas was sent from one side of the composite material at a pressure of 0.5 kg/cm 2 and the airflow rate per minute per square centimeter was calculated.
Measured at 5 points in the width direction for a 300mm wide composite material and averaged. Moisture permeability of composite material: Compliant with JIS Z0208. Example 2 A copolymer of vinyl chloride and vinyl acetate (average degree of polymerization 1000, containing vinyl acetate) was prepared by using an emulsion polymerization method to produce the polyvinyl chloride in the example described in Example 1, and dried by a spray drying method. A dispersion liquid was prepared in the same manner as described in the same example except that the amount of 5% by weight, the glass transition point of about 70° C., and the average particle size of 25 μm was used. The resulting dispersion was applied to the same type of nylon fabric as used in Example 1 in the same manner as described in Example 1, and the coated film was pre-dried. Subsequently, the nylon woven fabric with the coated film was placed on a metal plate and left in a hot air oven adjusted to 80°C for 3 minutes to pre-dry the coated film. Next, the nylon woven fabric with the coated film was placed on the metal plate,
After leaving it in a hot air oven adjusted to 160℃ for 1 minute to volatilize the moisture almost completely, the surface of the polyvinyl chloride powder particles is melted, adhering adjacent particle surfaces to each other, and at the same time adhering to the surface of the nylon fabric. Attached together. After the above heating and melting operations are completed, cool and coat one side with a thickness of approximately 0.1 mm (definition is the same as in Example 1).
A breathable composite material having a breathable resin layer formed thereon was obtained. Various properties of the obtained breathable composite material were measured by the method described in Example 1. The results are shown in Table 1. Comparative Example 1 In the example described in Example 1, heating the coating film,
The operating conditions for melting were a temperature of 200℃.
A composite material was produced using a similar operating procedure to that described in the same example. Various properties of the obtained composite material were measured by the method described in Example 1. The results are shown in Table 1. Comparative Example 2 In the example described in Example 2, heating the coating film,
A composite material was produced using the same procedure as described in the same example, except that the melting operation conditions were 190°C. Various properties of the obtained composite material were measured by the method described in Example 1. The results are shown in Table 1.
【表】
第1表より、本発明方法によつて得られた複合
材は、通気量、透湿度ともに大きな値を示すが、
加熱、溶融の操作条件を前記()式で表わされ
る上限温度以上とすると、得られる複合材は、通
気性、透湿度ともに小さな値を示すことが、明ら
かである。[Table] From Table 1, the composite material obtained by the method of the present invention shows large values for both air permeability and moisture permeability.
It is clear that when the operating conditions for heating and melting are set to above the upper limit temperature expressed by the above formula (), the resulting composite material exhibits small values for both air permeability and water vapor permeability.
Claims (1)
られた重合体乳濁液を乾燥して得られた平均粒子
径が5〜50ミクロンの塩化ビニル系樹脂を、可塑
剤とともに水に分散し、この分散液を布製基材の
片面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+(150−可塑剤添加部数) …() 〔()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100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、溶融して樹脂粒子
表面同志を溶着させ、かつ、布製基材と付着させ
たのち、冷却することを特徴とする通気性複合材
の製造方法。[Scope of Claims] 1. A vinyl chloride resin with an average particle size of 5 to 50 microns obtained by drying a polymer emulsion obtained by an emulsion polymerization method or a fine suspension polymerization method, It is dispersed in water together with a plasticizer, and this dispersion is applied to one side of a fabric base material to form a coating film, and then this coating film is calculated by the following formula (), that is, Tg + (150 - number of parts added of plasticizer)... () [In formula (), Tg means the glass transition point of the vinyl chloride resin, and the number of parts of plasticizer added means the number of parts of the plasticizer added to 100 parts by weight of the vinyl chloride resin. ] A method for producing an air-permeable composite material, which comprises heating and melting the resin particles at a temperature below the temperature expressed by the formula to weld the surfaces of the resin particles to each other and adhering them to a fabric base material, and then cooling the resin particles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57192661A JPS5981171A (en) | 1982-11-02 | 1982-11-02 | Manufacture of air permeable composite material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57192661A JPS5981171A (en) | 1982-11-02 | 1982-11-02 | Manufacture of air permeable composite material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5981171A JPS5981171A (en) | 1984-05-10 |
| JPH0214888B2 true JPH0214888B2 (en) | 1990-04-10 |
Family
ID=16294938
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57192661A Granted JPS5981171A (en) | 1982-11-02 | 1982-11-02 | Manufacture of air permeable composite material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5981171A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0639148B2 (en) * | 1989-02-09 | 1994-05-25 | 平岡織染株式会社 | Waterproof sheet manufacturing method |
-
1982
- 1982-11-02 JP JP57192661A patent/JPS5981171A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5981171A (en) | 1984-05-10 |
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