JPH0618921B2 - Method for forming W / O type emulsion and porosity - Google Patents
Method for forming W / O type emulsion and porosityInfo
- Publication number
- JPH0618921B2 JPH0618921B2 JP21505689A JP21505689A JPH0618921B2 JP H0618921 B2 JPH0618921 B2 JP H0618921B2 JP 21505689 A JP21505689 A JP 21505689A JP 21505689 A JP21505689 A JP 21505689A JP H0618921 B2 JPH0618921 B2 JP H0618921B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- organic solvent
- polymer
- emulsion
- type emulsion
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Treatment And Processing Of Natural Fur Or Leather (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Paints Or Removers (AREA)
- Synthetic Leather, Interior Materials Or Flexible Sheet Materials (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、合成皮革、人工皮革、天然皮革などの皮革類
の表面形成膜、各種セパレータ膜、医療分野などに用い
られる連通孔を有する多孔質(微多孔性膜)の形成方法
に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention relates to a surface forming film of leather such as synthetic leather, artificial leather, and natural leather, various separator films, and a porous material having communicating holes used in the medical field and the like. The present invention relates to a method for forming a quality (microporous film).
微多孔性膜の製造方法は、従来から多くの方法が提案さ
れ、実用化されている。その方法を大別すると、湿式法
で代表される抽出法と乾燥法があるが、これらの従来方
法では、薄膜形成時の孔の大きさの制御、生産スピード
が遅いなどの面から用途によっては未だ不満足な点が多
く、必要性がありながら実施されていないのが実情であ
る。As a method for producing a microporous membrane, many methods have been conventionally proposed and put into practical use. The methods are roughly classified into an extraction method and a drying method, which are typified by a wet method. However, in these conventional methods, it is possible to control the size of pores when forming a thin film, and the production speed is slow. There are still many unsatisfied points, and the reality is that they have not been implemented although they are necessary.
例えば、衣料、家具シート、車両シート、靴甲革などに
用いられる合成皮革、人工皮革、天然皮革などの皮革類
の表面仕上膜には、快適さの面から通気性、透湿性に富
む被膜が望まれているが、未だ満足すべき方法がなく実
施されていない。For example, the surface finishing film of synthetic leather, artificial leather, natural leather, and other leather used for clothing, furniture seats, vehicle seats, shoe uppers, etc., has a film that is highly breathable and breathable in terms of comfort. Although desired, there is still no satisfactory method and it is not implemented.
本発明は、前記従来技術の課題を背景になされたもの
で、用途毎に要求される機能や性能に適した孔径とする
ことができるという効果を奏しうる多孔質形成用のW/
O型エマルジョンおよびこれを用いた多孔質の形成方法
を提供することを目的とする。The present invention has been made against the background of the above-mentioned problems of the prior art, and W / for forming a porous material, which has an effect that a pore diameter suitable for a function or performance required for each application can be obtained
It is an object of the present invention to provide an O-type emulsion and a method for forming a porosity using the same.
本発明は、沸点が150℃以下であり、かつ水の溶解度
が100g当たり50g以下である有機溶剤と高分子重
合体とからなる、高分子重合体有機溶剤溶液または分散
液に、水溶性アミノ酸多量体の水溶液を乳化混合して得
られた多孔質成形用のW/O型エマルジョンおよびそれ
を支持体に被覆したのち、乾燥させることからなる多孔
質の形成方法を提供するものである。The present invention provides a high-molecular polymer organic solvent solution or dispersion comprising a high-molecular polymer and an organic solvent having a boiling point of 150 ° C. or lower and a water solubility of 50 g or lower per 100 g, and containing a large amount of a water-soluble amino acid. It is intended to provide a W / O type emulsion for porous molding, which is obtained by emulsifying and mixing an aqueous solution of a body, and a method for forming a porous body, which comprises coating the support with the W / O type emulsion and then drying.
本発明においては、沸点が150℃以下であり、かつ水
の溶解度が100gあたり50g以下である有機溶剤を
使用する。本発明の多孔質形成機構は、支持体に被覆さ
れたW/O型エマルジョンを乾燥させる際、該エマルジ
ョン中の有機溶剤が、分散されている水よりも速く蒸発
して高分子重合体が分散水を安定維持した状態で凝固す
ることによるものであり、従って本発明の有機溶剤の沸
点は150℃以下、好ましくは120℃以下でなければ
ならない。沸点が150℃を超えた有機溶剤を使用する
と、乾燥の際、該W/O型エマルジョンを構成する有機
溶剤と分散水の蒸発が同時に進行するため本発明の目的
とする微多孔質は得られない。本発明の多孔化機構から
して、水の沸点である100℃以上の沸点を有する有機
溶剤でも本発明で使用できる理由は、本発明で使用する
水溶性アミノ酸多量体が分散水の表面に配向して分子状
被膜を形成しているため、高温の急激な乾燥条件下でも
水の分散は安定で、かつ蒸発が遅延されることによるも
のと考えられる。In the present invention, an organic solvent having a boiling point of 150 ° C. or less and a water solubility of 50 g or less per 100 g is used. The mechanism for forming the porosity of the present invention is that when the W / O type emulsion coated on the support is dried, the organic solvent in the emulsion evaporates faster than the dispersed water to disperse the high molecular weight polymer. This is because water solidifies in a stable state, and therefore the boiling point of the organic solvent of the present invention must be 150 ° C or lower, preferably 120 ° C or lower. When an organic solvent having a boiling point of more than 150 ° C. is used, the evaporation of the organic solvent constituting the W / O type emulsion and the dispersion water simultaneously proceed during drying, so that the target microporous material of the present invention can be obtained. Absent. The reason why the organic solvent having a boiling point of 100 ° C. or more, which is the boiling point of water, can be used in the present invention in view of the porosity mechanism of the present invention is that the water-soluble amino acid multimer used in the present invention is oriented on the surface of dispersed water. It is considered that the dispersion of water is stable and the evaporation is delayed even under the rapid drying condition at high temperature because the molecular coating is formed.
また、本発明の有機溶剤は、該有機溶剤100gあたり
の水の溶解度50g以下でなければならない。水の溶解
度が50gを超える有機溶剤を使用した場合は、アミノ
酸多量体の水溶液を高分子重合体有機溶剤溶液に添加す
る際、高分子重合体が凝固し、安定したエマルジョンが
得られない。Further, the organic solvent of the present invention must have a water solubility of 50 g or less per 100 g of the organic solvent. When an organic solvent having a water solubility of more than 50 g is used, when the aqueous solution of the amino acid polymer is added to the high molecular polymer organic solvent solution, the high molecular polymer coagulates and a stable emulsion cannot be obtained.
沸点が150℃以下であり、水の溶解度が100gあた
り50g以下である本発明の有機溶剤としては、ベンゼ
ン、トルエン、キシレン、メチルエチルケトン、ジエチ
ルケトン、エチルブチルケトン、ジブチルケトン、酢酸
エチル、酢酸ブチル、二塩化エタンなどがあり、場合に
よってはトルエン/テトラヒドロフラン、メチルエチル
ケトン/テトラヒドロフラン、トルエン/ジオキサンな
どの水と混和性の小さい有機溶剤と水と混和性の大きい
有機溶剤との混合溶剤であってもかまわない。As the organic solvent of the present invention having a boiling point of 150 ° C. or lower and a water solubility of 50 g or lower per 100 g, benzene, toluene, xylene, methyl ethyl ketone, diethyl ketone, ethyl butyl ketone, dibutyl ketone, ethyl acetate, butyl acetate, There is ethane dichloride, etc., and in some cases, it may be a mixed solvent of an organic solvent having a low miscibility with water and an organic solvent having a high miscibility with water, such as toluene / tetrahydrofuran, methyl ethyl ketone / tetrahydrofuran, and toluene / dioxane. .
本発明で使用する高分子重合体としては、天然ゴムなど
の天然樹脂、ポリ塩化ビニル、SBR(スチレン−ブタ
シエンゴム)、NBR(アクリロニトリル−ブタジエン
ゴム)、ポリウレタン、ポリスチレン、ポリアミノ酸、
ポリアミド、ポリエステルなどの従来公知の合成高分子
重合体が挙げられ、場合によってはこれらの混合重合体
であってもかまわない。The high molecular weight polymer used in the present invention includes natural resins such as natural rubber, polyvinyl chloride, SBR (styrene-butadiene rubber), NBR (acrylonitrile-butadiene rubber), polyurethane, polystyrene, polyamino acid,
Conventionally known synthetic high molecular weight polymers such as polyamide and polyester may be mentioned, and in some cases, a mixed polymer thereof may be used.
本発明で使用する高分子重合体有機溶剤溶液は、該高分
子重合体有機溶剤溶液中に該有機溶剤には不溶性の同種
あるいは異種の粒子が分散されている高分子重合体有機
溶剤分散溶液であってもかまわない。むしろ、このよう
な粒子が存在することにより、被覆された該W/O型エ
マルジョンを乾燥する際に、高分子重合体の収縮が抑え
られ多孔質が得られ易くなるため好ましい場合がある。The high molecular polymer organic solvent solution used in the present invention is a high molecular polymer organic solvent dispersion solution in which the same kind or different kinds of particles insoluble in the organic solvent are dispersed in the high molecular polymer organic solvent solution. It doesn't matter. Rather, the presence of such particles is preferred in some cases, since the shrinkage of the high molecular weight polymer is suppressed and the porosity is easily obtained when the coated W / O type emulsion is dried.
このような不溶性粒子としては、例えばベンゾクアナミ
ン樹脂粉末、シリコーン粉末、ポリアミノ酸粉末、ポリ
エステル粉末、ポリアミド粉末など従来公知の重合体粉
末が挙げられ、これらは使用される有機溶剤の種類によ
って適宜選択される。Examples of such insoluble particles include conventionally known polymer powders such as benzoquanamine resin powder, silicone powder, polyamino acid powder, polyester powder, and polyamide powder, which are appropriately selected depending on the type of organic solvent used. .
本発明の水溶性アミノ酸多量体とは、蛋白質、例えばコ
ラーゲンなどの分解によって得られる天然ポリアミノ酸
多量体、あるいはグリシン、プロリン、アスパラギン
酸、セリン、アラニン、アルギニン、グルタミン酸、イ
ソロイシン、ヒドロキシプロリン、バリン、リジン、フ
ェニルアラニン、ロイシン、チロシン、スレオニン、ヒ
ステジン、メチオニン、ヒドロキリジンなどアミノ酸の
合成多量体である。安定したエマルジョンを形成させる
に適当な分子量は、200〜3,000であり、またこ
の範囲の分子量のアミノ酸多量体は水の保持力が強いた
め、W/O型エマルジョンを乾燥させる際に分散水の蒸
発を遅延させ、本発明の目的とする微多孔質が得られ易
い。The water-soluble amino acid multimer of the present invention is a protein, for example, a natural polyamino acid multimer obtained by degrading collagen or the like, or glycine, proline, aspartic acid, serine, alanine, arginine, glutamic acid, isoleucine, hydroxyproline, valine, It is a synthetic multimer of amino acids such as lysine, phenylalanine, leucine, tyrosine, threonine, histidine, methionine, and hydrokyridine. A suitable molecular weight for forming a stable emulsion is 200 to 3,000, and an amino acid multimer having a molecular weight in this range has a strong water retention property. It is easy to obtain the microporous material that is the object of the present invention by delaying the evaporation of.
本発明で使用される高分子重合体有機溶剤溶液の高分子
重合体の濃度は、高濃度から低濃度まで広い範囲で使用
できる。例えば、高濃度で使用すれば、得られる多孔質
は孔径が大きく数が少なくなる傾向となり、低濃度で使
用すれば、得られる多孔質は孔径が小さく数が多くなる
傾向となるため、目的とする用途によって濃度は選定す
べきである。さらに、孔径を大きく左右させる要因とし
ては、添加させる水の量がある。高分子重合体の固形重
量に対する添加される水の量の比率が大きくなるほど、
得られる多孔質は孔径が小さくなる。The concentration of the high molecular polymer in the high molecular polymer organic solvent solution used in the present invention can be used in a wide range from high concentration to low concentration. For example, when used at a high concentration, the resulting porous material tends to have a large pore size and a small number, and when used at a low concentration, the resulting porous material tends to have a small pore size and a large number, and thus the purpose is The concentration should be selected according to the intended use. Further, the factor that greatly affects the pore size is the amount of water added. The larger the ratio of the amount of water added to the solid weight of the high molecular weight polymer,
The resulting porous material has a small pore size.
一般的な範囲としては、高分子重合体固形重量100重
量部に対し、添加される水の量は30〜600重量部で
ある。しかし、この範囲は、本発明を限定するものでは
ない。As a general range, the amount of water to be added is 30 to 600 parts by weight with respect to 100 parts by weight of the solid polymer. However, this range does not limit the invention.
エマルジョンを構成するアミノ酸多量体の量も、広い範
囲で選ぶことができる。高分子重合体固形重量100重
量部に対するアミノ酸多量体の添加重量が15重量部以
上では、得られる多孔質の孔径はほとんど変化せず、上
記で述べた高分子重合体の濃度、添加水の量の影響が大
きく孔径に影響を与える。The amount of the amino acid multimer constituting the emulsion can be selected within a wide range. When the added weight of the amino acid multimer is 15 parts by weight or more based on 100 parts by weight of the high molecular weight polymer solid, the pore size of the obtained porous material hardly changes, and the concentration of the high molecular weight polymer and the amount of the added water described above. Greatly affects the pore size.
アミノ酸多量体の添加量が15重量部未満では、添加量
が少なくなるにつれて得られる多孔質の孔径は大きくな
る傾向となるが、やはり高分子重合体の濃度、添加水の
量の影響も同時に受ける。If the amount of the amino acid polymer added is less than 15 parts by weight, the pore size of the porous material obtained tends to increase as the amount added decreases, but the concentration of the polymer and the amount of added water are also affected. .
従って、ポリアミノ酸多量体の量は、エマルジョンの安
定性から決定されるべきである。一般的に、高分子重合
体固形重量100重量部に対してアミノ酸多量体の添加
重量は、0.5〜150重量部の広い範囲でエマルジョン
は安定化が可能であるが、ポットライフの長い安定化さ
れたエマルジョンを得るのに、該添加重量は5重量部以
上が好ましく、さらに好ましくは10〜80重量部であ
る。Therefore, the amount of polyamino acid multimer should be determined from the stability of the emulsion. Generally, the addition weight of the amino acid multimer to 100 parts by weight of the high molecular weight polymer is 0.5 to 150 parts by weight, and the emulsion can be stabilized in a wide range, but it is stable for a long pot life. In order to obtain such an emulsion, the added weight is preferably 5 parts by weight or more, more preferably 10 to 80 parts by weight.
以上に説明したように、本発明は、エマルジョンを構成
する高分子重合体、有機溶剤、水、水溶性アミノ酸多量
体の比率を選ぶことによって広い範囲の孔径を設定出来
る従来には無いものである。As described above, the present invention does not exist in the prior art in which a wide range of pore diameters can be set by selecting the ratio of a high molecular polymer, an organic solvent, water, and a water-soluble amino acid multimer constituting an emulsion. .
このように、広範囲の孔径を設定できれば、通気性被膜
を得る場合は、通気、透湿、耐水度のバランスを任意に
設定でき、またフィルター用被膜を得る場合は、目的物
によって任意に孔径を設定できるという効果が得られ
る。In this way, if a wide range of pore diameters can be set, in the case of obtaining a breathable coating, the balance of ventilation, moisture permeability, and water resistance can be set arbitrarily, and in the case of obtaining a coating for a filter, the pore diameter can be arbitrarily set depending on the target substance. The effect that it can be set is obtained.
本発明のエマルジョンは、高分子重合体有機溶剤溶液ま
たは分散液に、水溶性アミノ酸多量体の水溶液を乳化混
合して得られる。その具体的な製法としては、水溶性ア
ミノ酸多量体と任意の濃度に溶解した水溶液をあらかじ
め調製し、これを任意濃度の高分子重合体有機溶剤溶
液、または分散液中にかきまぜながら少量ずつ添加し、
W/O型エマルジョンを形成させる方法が一般的であ
る。The emulsion of the present invention can be obtained by emulsifying and mixing an aqueous solution of a water-soluble amino acid multimer with an organic solvent solution or dispersion of a polymer. As a specific production method, a water-soluble amino acid multimer and an aqueous solution dissolved at an arbitrary concentration are prepared in advance, and this is added little by little to a high-molecular polymer organic solvent solution of an arbitrary concentration or a dispersion while stirring. ,
A general method is to form a W / O type emulsion.
本発明のエマルジョンは、離型紙、ポリエステルフィル
ム、織布、編布、不織布、合成皮革、人工皮革、天然皮
革などの支持体に被覆して乾燥すると多孔質が得られ
る。支持体に被覆する方法としては、ナイフコーティン
グ、ロールコーティング、グラビアコーティングなど通
常の被覆方法が採用できる。When the emulsion of the present invention is coated on a support such as release paper, polyester film, woven fabric, knitted fabric, non-woven fabric, synthetic leather, artificial leather, natural leather, etc. and dried, it is porous. As a method for coating the support, a usual coating method such as knife coating, roll coating, and gravure coating can be adopted.
また、この時の乾燥温度は室温から150℃以上の高温
まで適用できるが、エマルジョンを構成する高分子重合
体の軟化温度以下の温度が好ましく、また乾燥スピード
を速めて生産性を高めるためには出来るだけ高温が好ま
しい。従って、乾燥温度としては100℃〜150℃が
一般的には好ましい。例えば、支持体上に該エマルジョ
ンを100g/m2の量を被覆して乾燥する場合は、12
0℃の乾燥温度で約1分で目標とする多孔質が得られる
ので、一般的な20mの長さの乾燥機であれば、ライン
スピードは約20m/分と高生産性が得られる。Further, the drying temperature at this time can be applied from room temperature to a high temperature of 150 ° C. or higher, but a temperature not higher than the softening temperature of the polymer constituting the emulsion is preferable, and in order to accelerate the drying speed and improve productivity. The highest temperature possible is preferable. Therefore, a drying temperature of 100 ° C. to 150 ° C. is generally preferable. For example, when the emulsion is coated on the support in an amount of 100 g / m 2 and dried, 12
Since a target porosity can be obtained in about 1 minute at a drying temperature of 0 ° C., a general dryer having a length of 20 m can achieve high productivity with a line speed of about 20 m / min.
本発明の多孔質形成機構は、次の原理に基づくものであ
る。すなわち、該エマルジョンを構成する分散水の球表
面は、水溶性アミノ酸多量体によって覆われ、その界面
活性効果によって該エマルジョンは安定化される。すな
わち、親油基は高分子重合体有機溶剤溶液側に配向し、
親水基は水粒子側に配向することによって、該エマルジ
ョンは安定化され、支持体への被覆後の乾燥の際にも水
粒子は凝集を生ずることなく、有機溶剤の蒸発とともに
高分子重合体の凝固が生ずる。このとき、分散水粒子は
表面を覆っている水溶性アミノ酸多量体による保水効果
のため、有機溶剤の蒸発よりも蒸発が遅れることとな
る。該エマルジョンにおいて、有機溶剤の蒸発の際の収
縮が大きい高分子重合体を使用する場合は、前述した不
溶性粒子を併用すると収縮が抑えられ効果的に多孔質が
得られ易い。The porosity forming mechanism of the present invention is based on the following principle. That is, the spherical surface of the dispersed water that constitutes the emulsion is covered with the water-soluble amino acid multimer, and the emulsion is stabilized by the surface-active effect. That is, the lipophilic group is oriented to the high molecular weight polymer organic solvent solution side,
By orienting the hydrophilic groups on the water particle side, the emulsion is stabilized, the water particles do not agglomerate during drying after coating on the support, and the water-soluble polymer of the high molecular weight polymer evaporates as the organic solvent evaporates. Coagulation occurs. At this time, the water dispersion particles have a water-retaining effect due to the water-soluble amino acid multimers covering the surfaces thereof, so that the evaporation is delayed as compared with the evaporation of the organic solvent. In the emulsion, when a high-molecular polymer having a large shrinkage upon evaporation of an organic solvent is used, the use of the above-mentioned insoluble particles together suppresses the shrinkage, and it is easy to effectively obtain a porous structure.
以上の方法で得られた多孔質は、支持体から剥離して、
各種のセパレータ膜、医療分野の通気膜、撥水処理と併
用して医療分野の耐水通気膜、合成皮革、人工皮革、天
然皮革などの表面化粧通気被膜などとして広範囲に利用
できる。そのほか、織布、編布、不織布などの繊維集合
体に直接被覆したものも防水通気布などとして、医療、
衣料等多くの分野で利用することができる。The porous obtained by the above method is peeled from the support,
It can be widely used as various separator membranes, breathable membranes in the medical field, water-resistant breathable membranes in the medical field, surface makeup breathable coatings for synthetic leather, artificial leather, natural leather, etc. In addition, those that are coated directly on fiber aggregates such as woven fabric, knitted fabric, and non-woven fabric can also be used as medical ventilation, etc.
It can be used in many fields such as clothing.
以下、具体的に実施例によって本発明を詳細に説明す
る。なお、実施例中「部」、「%」とあるのは、いずれ
も重量基準であり、特性測定値は下記の方法で得られた
ものである。Hereinafter, the present invention will be described in detail with reference to specific examples. In the examples, "parts" and "%" are based on weight, and the characteristic measurement values were obtained by the following methods.
(イ)通気度 JIS P8117の方法に準じ、ガーレのデンソメー
タを使用して測定した値で、50mlの空気が通過するの
に要する時間(秒)で表す。(A) Air permeability This is a value measured using a Gurley densometer according to the method of JIS P8117, and is expressed as the time (seconds) required for 50 ml of air to pass.
(ロ)透湿度 JIS L1099 A−1法の方法に準じ、透湿度
(g/m2・day)で表す。(B) Moisture permeability According to the method of JIS L1099 A-1, it is expressed by moisture permeability (g / m 2 · day).
(ハ)耐水圧 JIS L1092 A法の方法に準じ、耐水圧を水柱
(mm)で表す。(C) Water pressure resistance According to the method of JIS L1092 A method, the water pressure resistance is expressed by a water column (mm).
実施例1(W/O型エマルジョンの作製) ポリウレタン−ポリ塩化ビニル共重合体(東亜合成化学
(株)製)の15%メチルエチルケトン/トルエン(重
量比)=60/40溶液100部に、分子量800のポ
リグルタミン酸の10%水溶液70部を攪拌しながら添
加してW/O型エマルジョンを得た。Example 1 (Production of W / O type emulsion) 100 parts of a 15% methyl ethyl ketone / toluene (weight ratio) = 60/40 solution of a polyurethane-polyvinyl chloride copolymer (manufactured by Toagosei Kagaku Co., Ltd.) in 100 parts of a molecular weight of 800 70 parts of a 10% aqueous solution of polyglutamic acid was added with stirring to obtain a W / O type emulsion.
実施例2(W/O型エマルジョンの作製) ポリアミノ酸を主体とする重合体のエチレンジクロライ
ド8%溶液(セイコー化成(株)製、ラックスキンXB
−900)100部に、水溶性ポリアミノ酸多量体(住
友化学工業(株)製、ハイマージュ)の10%水溶液5
0部を攪拌しながら添加してW/O型エマルジョンを得
た。Example 2 (Preparation of W / O type emulsion) 8% ethylene dichloride solution of a polymer mainly composed of polyamino acid (manufactured by Seiko Kasei Co., Ltd., Luck Skin XB)
-900) 100 parts of a 10% aqueous solution of a water-soluble polyamino acid multimer (Sumitomo Chemical Co., Ltd., Hiimage) 5
0 part was added with stirring to obtain a W / O type emulsion.
実施例3(W/O型エマルジョンの作製) 15%ポリウレタン−メチルエチルケトン/トルエン
(70/30)溶液100部に、水溶性ポリアミノ酸多
量体(住友化学工業(株)製ハイマージュ)の10%水
溶液25部を攪拌しながら添加してW/O型エマルジョ
ンを得た。Example 3 (Preparation of W / O type emulsion) A 100% solution of a 15% polyurethane-methylethylketone / toluene (70/30) solution was added to a 10% aqueous solution of a water-soluble polyamino acid multimer (Sumitomo Chemical Co., Ltd., Hiimage). 25 parts were added with stirring to obtain a W / O type emulsion.
実施例4(多孔質の形成) 離型紙上に、実施例1で得られたエマルジョンを100
g/m2の目付量でコーティングし、110℃で30秒間
の乾燥直後にポリエステル繊維からなる編み物を貼り合
わせ、さらに120℃で2分間乾燥させた。その後、離
型紙を剥離してシート状多孔質被覆編み物を得た。Example 4 (Formation of Porous Material) 100 μm of the emulsion obtained in Example 1 was placed on a release paper.
Coating was carried out at a basis weight of g / m 2 , and immediately after drying at 110 ° C. for 30 seconds, a knitted fabric made of polyester fibers was bonded and further dried at 120 ° C. for 2 minutes. Then, the release paper was peeled off to obtain a sheet-like porous coated knit.
撥水処理して得られたシート状多孔質被覆編み物は、通
気性、透湿性があり、かつ耐水性のあるもので耐水防寒
衣料して最適なものであった。The sheet-like porous coated knitted fabric obtained by the water-repellent treatment has breathability, moisture permeability, and water resistance, and is optimal as a water-resistant cold-wearing garment.
実施例5(多孔質の形成) 表面がポリウレタン多孔質からなる通気性のある人工皮
革未仕上基体の表面に、実施例1で得られたエマルジョ
ンに着色顔料を混合した液を100g/m2の目付量でコ
ーティングし、120℃で1分間乾燥させた。得られた
シート状着色人工皮革は通気性を有するものであり、靴
甲革用、衣料用、手袋用、家具車両シート用などとして
快適なものであった。Example 5 (Formation of Porosity) 100 g / m 2 of a liquid prepared by mixing the emulsion obtained in Example 1 with a color pigment was applied to the surface of a breathable artificial leather unfinished substrate having a polyurethane porous surface. The coating was carried out at a basis weight and dried at 120 ° C. for 1 minute. The obtained sheet-like colored artificial leather was breathable and was comfortable for shoe uppers, clothing, gloves, furniture vehicle seats, and the like.
実施例6(多孔質の形成) 表面がポリウレタン多孔質からなる実施例5で使用した
人工皮革未仕上基体の表面に、実施例2で得られたエマ
ルジョンに着色顔料を混合した液を110メッシュのグ
ラビアロールを用いて塗布し、110℃で20秒間乾燥
させた。得られたシート状着色人工皮革は、通気性、透
湿性が大であり、靴用、衣料用、家具車両シート用とし
て快適なものであった。Example 6 (Formation of Porous Material) On the surface of the unfinished artificial leather substrate used in Example 5 whose surface is made of polyurethane porous material, a liquid obtained by mixing the emulsion obtained in Example 2 with a color pigment is used to form a 110 mesh liquid. It was applied using a gravure roll and dried at 110 ° C. for 20 seconds. The obtained sheet-like colored artificial leather was highly breathable and breathable, and was comfortable for shoes, clothing, and furniture vehicle seats.
実施例7(多孔質の形成) ポリエステルフィルム上に実施例3で得られたエマルジ
ョンを150g/m2の目付量でコーティングし、110
℃で2分間乾燥した。撥水処理したのち、ポリエステル
フィルムから剥離して得られたシート状多孔質膜は通気
性を有し、見掛け密度が0.32g/cm3であり各種セ
パレータ膜、医療用膜として有用なものであった。Example 7 (Formation of Porosity) A polyester film was coated with the emulsion obtained in Example 3 at a basis weight of 150 g / m 2 , and 110
It was dried at 0 ° C for 2 minutes. The sheet-like porous film obtained by peeling from the polyester film after water repellent treatment has air permeability and an apparent density of 0.32 g / cm 3 and is useful as various separator films and medical films. there were.
実施例8(多孔質の形成) 離型紙上に、実施例2で得られたエマルジョンを100
g/m2の目付量でコーティングし、110℃で40秒間
乾燥させたのち、次いで二液タイプのポリウレタン接着
剤液を150g/m2の目付量でコーティングし120℃
で40秒乾燥させ、その上にポリエステル繊維からなる
編み物をポリウレタン−ジメチルホルムアミド溶液を含
浸、コートして湿式凝固処理を施した基体を貼り合わせ
50℃で3日間放置した。離型紙を剥離して得られたシ
ート状人工皮革は、表面がポリアミノ酸樹脂の多孔質に
よって形成されているため、吸汗性、放湿性などが優
れ、ベトツキが無く、天然皮革の素上調外観を有し、家
具用シート、車両用シートとして有用なものであった。Example 8 (Formation of Porous Material) 100 μm of the emulsion obtained in Example 2 was placed on a release paper.
After coating with a basis weight of g / m 2 and drying at 110 ° C for 40 seconds, then a two-component type polyurethane adhesive solution is coated with a basis weight of 150 g / m 2 and 120 ° C.
After drying for 40 seconds, a knitted fabric made of polyester fiber was impregnated with a polyurethane-dimethylformamide solution, coated and wet-coagulated on the substrate, and the substrate was left at 50 ° C. for 3 days. The sheet-shaped artificial leather obtained by peeling off the release paper has a surface formed by the porosity of the polyamino acid resin, so it has excellent sweat absorption, moisture release, etc., is not sticky, and has a natural-looking appearance of natural leather. It has a usefulness as a furniture seat and a vehicle seat.
比較例1 離型紙上に、15%ポリウレタン−メチルエチルケトン
/トルエン(70/30)溶液100部にポリオキシエ
チレンセグメントを有する非イオン系界面活性剤(トー
レ・シリコーン(株)製、SH28PA)を1部添加し
たのち、攪拌しながら30部の水を添加して得たW/O
型エマルジョンを100g/m2の目付量でコーティング
し、110℃で2分間乾燥させた。離型紙から剥離して
得られたフィルムは、多孔質とはならず通気性はなかっ
た。Comparative Example 1 1 part of a nonionic surfactant (SH28PA manufactured by Toray Silicone Co., Ltd.) having a polyoxyethylene segment in 100 parts of a 15% polyurethane-methyl ethyl ketone / toluene (70/30) solution on release paper. After addition, 30 parts of water was added with stirring to obtain W / O
The type emulsion was coated at a basis weight of 100 g / m 2 and dried at 110 ° C. for 2 minutes. The film obtained by peeling from the release paper was not porous and was not breathable.
実施例4〜8および比較例1で得られた多孔質シート状
物の特性を、第1表に示す。The characteristics of the porous sheet materials obtained in Examples 4 to 8 and Comparative Example 1 are shown in Table 1.
〔発明の効果〕 本発明は、一般的乾式ラミネート装置、一般的なグラビ
ア塗布装置を用いて、従来と同じ乾燥速度で、従来法で
は得られない通気性、透湿性あるいは通気・耐水性、透
湿・耐水性に優れた多孔質を形成させる方法であり、得
られる多孔質は、例えば合成皮革、人工皮革、天然皮革
などの表面形成膜、各種セパレーター膜、医療分野など
の広い用途に有効に使用できるものである。 [Advantages of the Invention] The present invention uses a general dry laminating apparatus and a general gravure coating apparatus at the same drying speed as the conventional one, and has breathability, moisture permeability or ventilation / water resistance, which is not obtained by the conventional method. It is a method of forming a porous material with excellent wet and water resistance, and the obtained porous material is effective for a wide range of applications such as surface forming films of synthetic leather, artificial leather, natural leather, various separator films, medical fields, etc. It can be used.
第1図は、実施例4で得られた多孔質被覆編み物の表面
(粒子構造)の電子顕微鏡写真、第2図は、実施例5で
得られた着色人工皮革の表面(粒子構造)の電子顕微鏡
写真、第3図は、実施例6で得られた着色人工皮革の表
面(粒子構造)の電子顕微鏡写真、第4図は、実施例7
で得られた多孔質膜の表面(粒子構造)の電子顕微鏡写
真、第5図は、実施例8で得られた人工皮革の表面(粒
子構造)電子顕微鏡写真、第6図は、比較例1で得られ
たフィルムの表面(粒子構造)の電子顕微鏡写真をそれ
ぞれ示す。電子顕微鏡写真の倍率は、それぞれ500倍
である。1 is an electron micrograph of the surface (particle structure) of the porous coated knitted fabric obtained in Example 4, and FIG. 2 is an electron of the surface (particle structure) of the colored artificial leather obtained in Example 5. Micrograph, FIG. 3 is an electron micrograph of the surface (particle structure) of the colored artificial leather obtained in Example 6, and FIG. 4 is Example 7.
An electron micrograph of the surface (particle structure) of the porous film obtained in Example 5, FIG. 5 is an electron micrograph of the surface (particle structure) of the artificial leather obtained in Example 8, and FIG. 6 is Comparative Example 1. The electron micrographs of the surface (particle structure) of the film obtained in 1. are shown respectively. The electron micrographs have a magnification of 500 times, respectively.
Claims (2)
度が100gあたり50g以下である有機溶剤と高分子
重合体とからなる、高分子重合体有機溶剤溶液または分
散液に、水溶性アミノ酸多量体の水溶液を乳化混合して
得られるW/O型エマルジョン。1. A water-soluble amino acid in a polymer polymer organic solvent solution or dispersion, which comprises a polymer and an organic solvent having a boiling point of 150 ° C. or less and a water solubility of 50 g or less per 100 g. A W / O type emulsion obtained by emulsifying and mixing an aqueous solution of a multimer.
持体に被覆したのち、乾燥させることよりなる多孔質の
形成方法。2. A method for forming a porous structure, which comprises coating a support with the W / O type emulsion according to claim 1 and then drying the support.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21505689A JPH0618921B2 (en) | 1989-08-23 | 1989-08-23 | Method for forming W / O type emulsion and porosity |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21505689A JPH0618921B2 (en) | 1989-08-23 | 1989-08-23 | Method for forming W / O type emulsion and porosity |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0379643A JPH0379643A (en) | 1991-04-04 |
JPH0618921B2 true JPH0618921B2 (en) | 1994-03-16 |
Family
ID=16666030
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP21505689A Expired - Fee Related JPH0618921B2 (en) | 1989-08-23 | 1989-08-23 | Method for forming W / O type emulsion and porosity |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0618921B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012026361A1 (en) * | 2010-08-23 | 2012-03-01 | 日東電工株式会社 | Composite sheet |
CN103080230A (en) * | 2010-08-31 | 2013-05-01 | 日东电工株式会社 | Foam, production method for foam, and functional foam |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5518800A (en) * | 1993-03-10 | 1996-05-21 | Teijin Limited | Grained artificial leather, process for making same and fabricated articles |
JP4505109B2 (en) * | 2000-06-02 | 2010-07-21 | 株式会社フジ医療器 | Massage device |
JP2006188773A (en) * | 2004-12-28 | 2006-07-20 | Delta Tooling Co Ltd | Synthetic leather and solid knit |
JP5023261B2 (en) * | 2005-09-08 | 2012-09-12 | フジコピアン株式会社 | Lithium secondary battery separator and lithium secondary battery using the same |
-
1989
- 1989-08-23 JP JP21505689A patent/JPH0618921B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012026361A1 (en) * | 2010-08-23 | 2012-03-01 | 日東電工株式会社 | Composite sheet |
CN103080230A (en) * | 2010-08-31 | 2013-05-01 | 日东电工株式会社 | Foam, production method for foam, and functional foam |
Also Published As
Publication number | Publication date |
---|---|
JPH0379643A (en) | 1991-04-04 |
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