JPS6228225B2 - - Google Patents

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Publication number
JPS6228225B2
JPS6228225B2 JP53110608A JP11060878A JPS6228225B2 JP S6228225 B2 JPS6228225 B2 JP S6228225B2 JP 53110608 A JP53110608 A JP 53110608A JP 11060878 A JP11060878 A JP 11060878A JP S6228225 B2 JPS6228225 B2 JP S6228225B2
Authority
JP
Japan
Prior art keywords
heat treatment
molded article
contact heat
fibrous
fiber
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
Application number
JP53110608A
Other languages
Japanese (ja)
Other versions
JPS5540805A (en
Inventor
Susumu Norota
Tsutomu Kiryama
Tadashi Imoto
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Teijin Ltd
Original Assignee
Teijin Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Teijin Ltd filed Critical Teijin Ltd
Priority to JP11060878A priority Critical patent/JPS5540805A/en
Publication of JPS5540805A publication Critical patent/JPS5540805A/en
Publication of JPS6228225B2 publication Critical patent/JPS6228225B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

[産業上の利用分野] 本発明は、繊維ウエブを原料として、非直線状
で孔道長の長い貫通孔を有し通気性のある多孔性
成形物を工業的に製造する方法に関するものであ
る。 [従来技術] 従来、汎用の多孔性シートの成形加工は、熱可
塑性合成板の成形加工法の下記代表的方法によつ
てなされている。 (1) 雄雌型成形法、(2) スリツプ成形法、(3)
加圧成形法、(4) 真空成形法、 これらの中で、工業的にみて最も簡便で生産性
が高いのは、上記(4)の真空成形法である。しか
し、一般の多孔性シート、例えば発泡スチロール
等、の成形加工は、実際には真空成形法の一種で
あるプラグアシスト法で行なわれており、透気性
が良すぎるために直接法では成形困難というのが
実状である。 これに対し、汎用のフイルムシートは、主とし
て上記(3)、(4)の方法で成形加工され、真空成形で
は直接法でも成形容易である。すなわち、真空成
形には、 (A)直接法、(B)ドレイプ成形法、(C)エアスリツプ
法、(D)スナツプバツク法、(E)プラグアシスト法、
(F)エアクツシヨン、法等があるが、中でも直接法
は、操作が非常に簡便であり、コスト的にも安
く、生産性も高く最も有利な方法である。 [発明が解決しようとする問題点] かかる状況下で、フイルムシートと既存の多孔
性シートとの中間程度の透気性がありかつ直接法
で真空成形の可能な新規な素材シートがあれば、
工業的に非常に有利である。そこで、本発明者ら
は、直接法による真空成形が容易であつてかつ非
直接状貫通孔を有する多孔性シートを経て多孔性
成形物を製造する方法について鋭意研究を進めた
結果、本発明に至つたものである。 [問題を解決するための手段] すなわち、本発明は、熱可塑性繊維状ポリマー
を主体とする繊維ウエブの多層積層体を、その全
端を把持しつ、特定条件下で非接触熱処理して多
孔性シートを形成し、しかる後、該多孔性シート
を真空成形して見掛け密度が0.20〜0.99g/cm3
成形物とすることを特徴とする不織構造体よりな
る多孔性成形物の製造方法である。 以下、本発明の方法を詳細に説明する。 本発明方法における熱可塑性繊維状ポリマーを
形成するポリマーとは、ポリエチレン、ポリプロ
ピレン、ポリ塩化ビニル、ポリスチレン、ふつ素
樹脂、アクリル―スチレン共重合樹脂、ポリカー
ボネート、ポリアセタール、ナイロン、ポリエス
テル、ポリウレタン等の熱可塑性ポリマー単体ま
たはそれらの混合体を総称し、特に限定されない
が、ポリオレフイン系、ナイロン系のポリマーや
各種エラストマー等が熱融解後の強力低下が少な
いので望ましい。これらのポリマーには、必要に
応じ艶消剤、着色剤、安定剤等の添加剤を含んで
もよい。 また、本発明方法において使用する繊維ウエブ
としては、本発明者らが先に特公昭49−18508号
等で提案したバーストフアイバー法によるたて方
向に無数の非連続亀裂を有するフイルム状物から
の二次元的繊維構造物で、繊維径(μ)の分布が
6.0〜12.0の標準偏差を有するものであり、該繊
維の断面がランダムな異形状である繊維構造物を
含むウエブが適当であるが、短繊維または長繊維
フイラメントからなるウエブでもよい。ウエブは
出来るだけ均一である方が望ましく、後記する方
法によつて得られるたて方向に無数の非連続亀裂
を有するフイブリル化シートを積層し、幅方向に
延展してなる、異形断面を有する繊維からなる網
状繊維ウエブを使用したものが最も望ましい。 本発明方法における繊維ウエブ多層積層体と
は、前述の繊維ウエブを複数層重ね合わせて形成
される構造体であつて、均一な多孔性フイルムを
得るためには少くとも出来るだけ多く積層する方
が良い。本発明方法により得られる多孔性成形物
の非直線状貫通孔の孔径分布は、該積層体の繊維
の繊維径によつて左右され、繊維径10μm以下の
細い繊維のウエブを用いる場合には成形物におけ
る孔径は小さくなり、また繊維径10〜30μm程度
の繊維ウエブを用いる場合には該孔径は大きくな
る。このように、成形物中の孔径と多層積層体を
構成する繊維の太さとは密接に関係し、デニール
(繊度)の異なつた分布を持つ繊維集合体を用い
ると、成形品の孔径もランダムなものとなる。前
述した如く、本発明方法で用いられる繊維ウエブ
の主体となる繊維の繊維径(μm)分布は、標準
偏差(σ)が6.0〜12.0のものが適当である。 繊度の異なる繊維ウエブを、厚さ方向にデニー
ルが増大する傾向になるように積層すると、成形
物の厚さ方向に孔径の変化した多孔体成形物が得
られる。 さらに、軟化点の異なる繊維の多層積層体を熱
処理して成形すると、軟化点の低い繊維によつて
構成される部分は完全に溶解して繊維形態が全く
なくなり、一方高融点繊維で構成される部分は完
全には溶解せず、一部は繊維状のまま残り多孔性
成形物の強力低下を防ぐとともに、曲面熱変形性
を発現することになる。 本発明の方法によれば、デニールや軟化点の異
なる繊維の多層積層体を使用することによつて、
適当な孔径分布を有する多孔性成形物が得られ
る。 本発明の目的とする不織構造体よりなる多孔性
成形物は、熱可塑性繊維状ポリマーを主体とする
繊維ウエブの多層積層体を、その全端を挾持しつ
つ、該ポリマーの少くとも30重量%が融解するよ
う後述の条件で非接触熱処理し、しかる後、目的
とする成形物の型に当てがつて真空成形すること
によつて得られる。 従来、不織布を形成するにあたつて熱可塑性繊
維ウエブを加熱ローラー等で融着せしめることは
よく知られているが、本発明方法における融解と
は、不織布を形成する為の融着とは異なり、外部
圧力を加えることなく非接触熱処理し、繊維状ポ
リマーの少くとも30重量%以上を溶解せしめ、い
わゆる繊維形態を部分的に失わしめて多孔性シー
トを形成するともに見掛密度を高め、非直線状貫
通孔を著しく小さくせしめるものである。 このため本発明方法では、多層積層体の非接触
熱処理を下記式を満足する温度(T℃)と時間
(t分)の条件下で行うことが必要である。 [1/(T−Tm)]≦t≦[50/(T/Tm)] 〔但し、tは非接触熱処理時間(分)、Tは非接触
熱処理の雰囲気温度(℃)であつて、該繊維ポリ
マーの主たる成分の融点(Tm℃)よりも1〜30
℃高い温度とする。〕 かかる非接触熱処理を受けた積層ウエブ内の繊
維状ポリマーは融解粘度と表面張力のバランス状
態においてウエブ空間を流動し、高密度で複雑な
多孔構造を形成する。 本発明方法では、このような非接触熱処理によ
つて形成した多孔性シート状物を真空成形に賦し
て所望の形状を有する成形物とするが、本発明方
法において採用される真空成形法としては、直接
法、ドレイプ成形法、エアスリツプ法、スナツプ
バツク法、プラグアシスト法、エアクツシヨン法
のいずれも実施可能である。とりわけ、直接法
は、上記各種の真空成形法の中で最も簡便な基本
的方法であり、設備的にも生産性の上でも安価に
製造できる方法である。本発明方法ではかかる直
接法によつて問題なく十分に成形可能である。す
なわち前述した如く非接触熱処理を行つて得られ
た多孔性シート状物を該シート状物がまだ軟かい
状態のうちに、目的とする成形物の型の上で、真
空吸引して形造るものである。真空成形法の最も
重要な問題は、(イ)どの程度まで深絞りできるか、
および(ロ)側面部と底部とで肉厚の差はどの程度に
押えられるか、などの点である。本発明方法にお
いて用いられる前記条件で非接触熱処理された多
孔性シート状物は、完全には融解しておらず、ご
く一部分は軟化した繊維にとどまつているため、
曲面変形性が大きく、絞り深さ(H)と開口広さ
(W)との比が0.5近傍においても十分に良好な成
形物が直接法で得ることができる。一方、偏肉に
ついても実施例で後述する様にH/W比が0.3の
近傍では十分に小さく良好な成形物が得られる。
なお、本発明方法ではガーレイ式測定法よる透気
度が0.1〜200秒/100c.c.―airの範囲にある多孔性
シート状物は特に成形性が良好であるので望まし
い。 次に図面を参照しながら本発明の不織構造体よ
りなる多孔性成形物の製造法を具体例をもつて声
明する。 ポリプロピレンと6―ナイロンとの混合熱可塑
性ポリマーを、ベント型押出機を用いて窒素ガス
を圧入しながら溶融混練し、スリツトダイから押
出すとともに高ドラフト下で引取つて第1図に示
す如き亀裂シートを形成し、該亀裂シートを
500枚程度積層し、進行方向にオーバーフイード
しながら、両端を把持して幅方向に延展し、該延
展ウエブをベルト間に設置された予備プレスロー
ラーでプレスして形態保持せしめ、続いて非接触
式赤外線ヒーターで195〜200℃の範囲で20〜30秒
間非接触熱処理し、続いて、得られた多孔性シー
ト状物を直接法の真空成形機にかけると、絞り深
さ(H)/開口広さ(W)の比が0.3〜0.5の第2
図に示される如きカツプ状多孔性成形物が得られ
る。 そして、本発明者らの研究によれば、かくして
良好な成形性の下で真空成形して得られる成形物
は、0.20〜0.99g/cm3という高い見掛け密度を有
する。 なお、本発明の方法において、多層積層体の中
に金網、寒冷紗などの補強材、活性炭、香料、顔
料、ガラス繊維、難燃剤、金箔等の添加剤を付与
し、該非接触熱処理を行ない、真空成形を実施
し、これらを含む不織構造体よりなる多孔性成形
物としてもよい。 [発明の効果] 上述の如き本発明方法によれば、簡便な直接法
の真空成形によつて見掛け密度0.20〜0.99g/cm3
の良好な多孔性成形物を製造することができる。 そして、本発明の不織構造体よりなる多孔性成
形物の用途としては、例えば帽子、アートフラワ
ー、曲面性のある服地の芯、ブラジヤーカツプ等
の衣料用分野、菓子敷、皿、飲食用パツト、トレ
イ、弁当箱の内装材、食品包装材、生鮮物の包装
材等の食品用分野、植木鉢、苗入れの如き農園芸
用分野、スピーカーコーン、部品ケース、水槽の
空気透化内張材等の工業的分野等が挙げられる。 [実施例] 以下、本発明を実施例を挙げて詳述する。なお
実施例中“部”とあるのは“重量部”を意味す
る。 実施例 ポリプロピレン70部を6―ナイロン30部との混
合熱可塑性ポリマーをベント型押出機を用いて窒
素ガスを圧入しながら、スリツトダイから押出し
高ドラフトで引取つて亀裂シート(A)を得た。 同様にしてポリプロピレンの亀裂シート(B)
を得た。 次に、亀裂シート(A)、(B)を各々交互に同
方向に積層し、積層数の合計が500枚になるよう
にした繊維状物を、進行方向にはオーバーフイー
ドしつつ、幅方向には延展して均一な繊維ウエブ
を形成せしめ、熱プレスローラーにて形態保持を
行い、目付120g/m2の不織シートとして巻取つ
た。続いて、該不織シートを赤外線ヒーターの間
に移送し、195〜200℃の範囲で30秒間熱処理し
て、直ちに隣接する真空成形機にかけて直接法及
びドレイプ法によりカツプ状の多孔性成形物を得
た。該成形物の製品品質は次表の如く良好であつ
た。
[Industrial Field of Application] The present invention relates to a method for industrially producing a porous molded product having non-linear long through-holes and having air permeability using a fiber web as a raw material. [Prior Art] Conventionally, general-purpose porous sheets have been molded by the following representative method for molding thermoplastic composite boards. (1) Male and female molding method, (2) Slip molding method, (3)
Pressure forming method (4) Vacuum forming method Among these, the vacuum forming method (4) above is the simplest and most productive from an industrial perspective. However, the molding of general porous sheets such as Styrofoam is actually done by the plug-assist method, which is a type of vacuum forming method, and the direct method is difficult to mold because the air permeability is so good. is the actual situation. On the other hand, general-purpose film sheets are mainly formed by the methods (3) and (4) above, and can be easily formed by direct vacuum forming. In other words, vacuum forming methods include (A) direct method, (B) drape molding method, (C) air slip method, (D) snapback method, (E) plug assist method,
(F) There are air action methods, methods, etc., but among them, the direct method is the most advantageous method because it is very simple to operate, low in cost, and has high productivity. [Problems to be solved by the invention] Under such circumstances, if there is a new material sheet that has an air permeability that is intermediate between a film sheet and an existing porous sheet and can be vacuum formed by a direct method,
It is industrially very advantageous. Therefore, the present inventors conducted extensive research on a method for producing porous molded products through a porous sheet that is easy to vacuum form using a direct method and has non-direct through holes, and as a result, the present invention was developed. It has been reached. [Means for Solving the Problem] That is, the present invention involves gripping all ends of a multilayer laminate of fibrous webs mainly composed of thermoplastic fibrous polymers and subjecting them to non-contact heat treatment under specific conditions to form pores. Production of a porous molded product made of a nonwoven structure, characterized by forming a porous sheet and then vacuum forming the porous sheet to obtain a molded product with an apparent density of 0.20 to 0.99 g/cm 3 It's a method. The method of the present invention will be explained in detail below. Polymers forming the thermoplastic fibrous polymer in the method of the present invention include thermoplastics such as polyethylene, polypropylene, polyvinyl chloride, polystyrene, fluorine resin, acrylic-styrene copolymer resin, polycarbonate, polyacetal, nylon, polyester, and polyurethane. It is a general term for single polymers or mixtures thereof, and is not particularly limited, but polyolefin-based, nylon-based polymers, various elastomers, etc. are preferable because they have less strength loss after thermal melting. These polymers may contain additives such as matting agents, colorants, stabilizers, etc., if necessary. Furthermore, the fiber web used in the method of the present invention is made from a film-like material having numerous discontinuous cracks in the longitudinal direction by the burst fiber method previously proposed by the present inventors in Japanese Patent Publication No. 49-18508. In a two-dimensional fiber structure, the distribution of fiber diameter (μ) is
A web containing a fiber structure having a standard deviation of 6.0 to 12.0 and having a randomly irregular cross-section of the fibers is suitable, but a web consisting of short fibers or long fiber filaments may also be used. It is desirable for the web to be as uniform as possible, and fibers with irregular cross sections are obtained by laminating fibrillated sheets with numerous discontinuous cracks in the longitudinal direction and extending them in the width direction, which are obtained by the method described later. It is most desirable to use a reticulated fiber web consisting of: The fiber web multilayer laminate in the method of the present invention is a structure formed by laminating multiple layers of the aforementioned fiber webs, and in order to obtain a uniform porous film, it is better to laminate at least as many layers as possible. good. The pore size distribution of the non-linear through-holes of the porous molded product obtained by the method of the present invention depends on the fiber diameter of the fibers of the laminate, and when using a web of thin fibers with a fiber diameter of 10 μm or less, the The pore size in the product becomes small, and when a fiber web having a fiber diameter of about 10 to 30 μm is used, the pore size becomes large. In this way, the pore size in the molded product is closely related to the thickness of the fibers that make up the multilayer laminate, and if fiber aggregates with different denier distributions are used, the pore size of the molded product will also be random. Become something. As mentioned above, the fiber diameter (μm) distribution of the main fibers of the fiber web used in the method of the present invention is suitably one with a standard deviation (σ) of 6.0 to 12.0. When fiber webs with different finenesses are laminated so that the denier tends to increase in the thickness direction, a porous molded article with pore diameters varying in the thickness direction of the molded article can be obtained. Furthermore, when a multilayer laminate of fibers with different softening points is heat-treated and molded, the part made up of fibers with a low softening point completely dissolves and loses its fiber form, while the part made up of fibers with a high melting point disappears. Some portions do not completely dissolve, and some remain in the form of fibers, which prevents the strength of the porous molded product from deteriorating and exhibits curved heat deformability. According to the method of the present invention, by using a multilayer laminate of fibers having different deniers and softening points,
A porous molded article with a suitable pore size distribution is obtained. The porous molded article made of a nonwoven structure, which is an object of the present invention, holds a multilayer laminate of fiber webs mainly composed of a thermoplastic fibrous polymer, while sandwiching all the ends thereof, and at least 30% by weight of the polymer. % is melted by non-contact heat treatment under the conditions described below, and then applied to a mold for the desired molded product and vacuum-formed. Conventionally, it is well known that thermoplastic fiber webs are fused using heated rollers etc. to form non-woven fabrics, but the melting in the method of the present invention is different from fusion for forming non-woven fabrics. , a non-contact heat treatment is performed without applying external pressure to dissolve at least 30% by weight of the fibrous polymer, partially losing the so-called fiber morphology, forming a porous sheet, increasing the apparent density, and forming a non-linear This makes the through hole significantly smaller. Therefore, in the method of the present invention, it is necessary to perform the non-contact heat treatment of the multilayer laminate under conditions of temperature (T° C.) and time (t minutes) that satisfy the following formula. [1/(T-Tm)]≦t≦[50/(T/Tm)] [However, t is the non-contact heat treatment time (minutes), T is the ambient temperature of the non-contact heat treatment (°C), and 1 to 30 higher than the melting point (Tm℃) of the main component of the fiber polymer
℃ higher temperature. ] The fibrous polymer in the laminated web subjected to such non-contact heat treatment flows through the web space in a state of balance between melt viscosity and surface tension, forming a dense and complex porous structure. In the method of the present invention, the porous sheet material formed by such non-contact heat treatment is subjected to vacuum forming to form a molded product having a desired shape. Any of the direct method, drape molding method, air slip method, snap back method, plug assist method, and air action method can be used. In particular, the direct method is the simplest basic method among the various vacuum forming methods mentioned above, and is a method that can be manufactured at low cost in terms of equipment and productivity. In the method of the present invention, sufficient molding is possible without problems by such a direct method. That is, a porous sheet-like material obtained by non-contact heat treatment as described above is formed by vacuum suction on a mold for the desired molded product while the sheet-like material is still in a soft state. It is. The most important issue with the vacuum forming method is (a) how deep it can be drawn;
and (b) how much difference in wall thickness can be suppressed between the side and bottom parts. The porous sheet-like material subjected to the non-contact heat treatment under the above conditions used in the method of the present invention is not completely melted, and a small portion remains as softened fibers.
A sufficiently good molded product with large curved surface deformability and a ratio of drawing depth (H) to opening width (W) of around 0.5 can be obtained by the direct method. On the other hand, as will be described later in Examples, thickness deviation is sufficiently small and a good molded product can be obtained when the H/W ratio is around 0.3.
In addition, in the method of the present invention, a porous sheet material having an air permeability in the range of 0.1 to 200 seconds/100 c.c.-air as measured by the Gurley method is particularly desirable because it has good moldability. Next, with reference to the drawings, a method for producing a porous molded article made of the nonwoven structure of the present invention will be described using a specific example. A mixed thermoplastic polymer of polypropylene and 6-nylon is melt-kneaded using a vent-type extruder while nitrogen gas is pressurized, extruded from a slit die, and taken under high draft to form a cracked sheet 1 as shown in FIG. form the crack sheet
Approximately 500 sheets are laminated, and while overfeeding in the advancing direction, both ends are gripped and stretched in the width direction. The stretched web is pressed with a preliminary press roller installed between the belts to maintain its shape, and then non-contact. Non-contact heat treatment is performed for 20 to 30 seconds in the range of 195 to 200℃ using an infrared heater, and then the resulting porous sheet is applied to a direct vacuum forming machine. The second one with a width (W) ratio of 0.3 to 0.5
A cup-shaped porous molded product as shown in the figure is obtained. According to the research conducted by the present inventors, the molded product obtained by vacuum forming with good moldability has a high apparent density of 0.20 to 0.99 g/cm 3 . In addition, in the method of the present invention, reinforcing materials such as wire mesh and cheesecloth, additives such as activated carbon, fragrances, pigments, glass fibers, flame retardants, and gold foil are added to the multilayer laminate, and the non-contact heat treatment is performed. Molding may be performed to produce a porous molded product made of a nonwoven structure containing these materials. [Effects of the Invention] According to the method of the present invention as described above, an apparent density of 0.20 to 0.99 g/cm 3 can be obtained by simple direct vacuum forming.
It is possible to produce a porous molded product with good quality. The porous molded product made of the nonwoven structure of the present invention can be used, for example, in the field of clothing such as hats, art flowers, curved cores for clothing, brassiere cups, confectionery mats, plates, eating and drinking pads, etc. Food products such as trays, interior materials for lunch boxes, food packaging materials, packaging materials for fresh produce, agricultural and horticultural products such as flowerpots and seedling containers, speaker cones, parts cases, air-permeable lining materials for aquariums, etc. Examples include the industrial field. [Example] Hereinafter, the present invention will be described in detail by giving examples. In the examples, "parts" means "parts by weight." Example A thermoplastic polymer mixture of 70 parts of polypropylene and 30 parts of 6-nylon was extruded from a slit die using a vented extruder while nitrogen gas was being pressurized and taken off at a high draft to obtain a cracked sheet (A). Similarly cracked polypropylene sheet (B)
I got it. Next, the cracked sheets (A) and (B) were laminated alternately in the same direction so that the total number of laminated sheets was 500, and the fibrous material was overfed in the direction of travel while being overfed in the width direction. The fiber web was spread to form a uniform fiber web, the shape was maintained using a hot press roller, and the fiber web was wound up as a nonwoven sheet with a basis weight of 120 g/m 2 . Subsequently, the nonwoven sheet is transferred between an infrared heater, heat-treated at a temperature of 195 to 200°C for 30 seconds, and immediately placed in an adjacent vacuum forming machine to form a cup-shaped porous molded product by direct method and drape method. Obtained. The product quality of the molded product was good as shown in the table below.

【表】【table】

【表】【table】 【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明方法の原料の一例であるたて
方向に無数の非連続の亀裂を有するシートの概略
図である。第2図は本発明方法による多孔性成形
物の一例を示す概略断面図であり、は成形物、
は非直線状貫通口の断面口、は非直線状貫通
口の側面亀裂を示す。
FIG. 1 is a schematic diagram of a sheet having numerous discontinuous cracks in the longitudinal direction, which is an example of the raw material for the method of the present invention. FIG. 2 is a schematic cross-sectional view showing an example of a porous molded product produced by the method of the present invention, and 2 is a molded product;
3 shows the cross-sectional opening of the non-linear through hole, and 4 shows the side crack of the non-linear through hole.

Claims (1)

【特許請求の範囲】 1 熱可塑性繊維状ポリマーを主体とする繊維ウ
エブの多層積層体を、その全端を把持しつつ、該
ポリマーの少くとも30重量%が融解するよう下記
式を満足する条件で非接触熱処理し、しかる後真
空成形することにより、見掛け密度が0.20〜0.99
g/cm3である成形物とすることを特徴とする不織
構造体よりなる多孔性成形物の製造方法。 [1/(T−Tm)]≦t≦[50/(T−Tm)] 〔但し、tは非接触熱処理時間(分)、Tは非接触
熱処理の雰囲気温度(℃)であつて、該繊維状ポ
リマーの主たる成分の融点(Tm℃)よりも1〜
30℃高い温度とする。〕 2 繊維ウエブの多層積層体がデニールおよび/
または軟化点の異なる2種以上の繊維ウエブを積
層せしめたものである特許請求の範囲第1項記載
の不織構造体よりなる多孔性成形物の製造方法。 3 繊維ウエブが融点の異なる2種以上の熱可塑
性ポリマーの混合物からなる特許請求の範囲第1
項記載の不織構造体よりなる多孔性成形物の製造
方法。
[Claims] 1. Conditions that satisfy the following formula so that at least 30% by weight of the polymer melts while gripping all ends of a multilayer laminate of fibrous webs mainly composed of thermoplastic fibrous polymers: By non-contact heat treatment and then vacuum forming, the apparent density is 0.20 to 0.99.
A method for producing a porous molded article made of a non-woven structure, characterized in that the molded article has a particle size of 3 g/cm 3 . [1/(T-Tm)]≦t≦[50/(T-Tm)] [However, t is the non-contact heat treatment time (minutes), T is the ambient temperature of the non-contact heat treatment (℃), and 1~ than the melting point (Tm℃) of the main component of the fibrous polymer
The temperature will be 30℃ higher. ] 2 The multilayer laminate of the fiber web has a denier and/or
Alternatively, the method for producing a porous molded article made of a nonwoven structure according to claim 1, which is obtained by laminating two or more types of fiber webs having different softening points. 3. Claim 1, in which the fibrous web is made of a mixture of two or more thermoplastic polymers having different melting points.
A method for producing a porous molded article comprising the nonwoven structure described in 1.
JP11060878A 1978-09-11 1978-09-11 Porous molded article comprising nonwoven fabric structure and production Granted JPS5540805A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11060878A JPS5540805A (en) 1978-09-11 1978-09-11 Porous molded article comprising nonwoven fabric structure and production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11060878A JPS5540805A (en) 1978-09-11 1978-09-11 Porous molded article comprising nonwoven fabric structure and production

Publications (2)

Publication Number Publication Date
JPS5540805A JPS5540805A (en) 1980-03-22
JPS6228225B2 true JPS6228225B2 (en) 1987-06-18

Family

ID=14540136

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11060878A Granted JPS5540805A (en) 1978-09-11 1978-09-11 Porous molded article comprising nonwoven fabric structure and production

Country Status (1)

Country Link
JP (1) JPS5540805A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63135551A (en) * 1986-11-20 1988-06-07 茂呂 尚浩 Production of nonwoven fabric

Also Published As

Publication number Publication date
JPS5540805A (en) 1980-03-22

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