JPH0571058A - Production of fiber formed product - Google Patents

Production of fiber formed product

Info

Publication number
JPH0571058A
JPH0571058A JP3255959A JP25595991A JPH0571058A JP H0571058 A JPH0571058 A JP H0571058A JP 3255959 A JP3255959 A JP 3255959A JP 25595991 A JP25595991 A JP 25595991A JP H0571058 A JPH0571058 A JP H0571058A
Authority
JP
Japan
Prior art keywords
fiber
heating
fiber bundle
heat
microwave
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.)
Pending
Application number
JP3255959A
Other languages
Japanese (ja)
Inventor
Shizumoto Fujisaki
倭元 藤崎
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.)
UNIE POINTO KK
Original Assignee
UNIE POINTO KK
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 UNIE POINTO KK filed Critical UNIE POINTO KK
Priority to JP3255959A priority Critical patent/JPH0571058A/en
Publication of JPH0571058A publication Critical patent/JPH0571058A/en
Pending legal-status Critical Current

Links

Landscapes

  • Lining Or Joining Of Plastics Or The Like (AREA)
  • Nonwoven Fabrics (AREA)
  • Pens And Brushes (AREA)

Abstract

PURPOSE:To obtain a fiber formed product having uniform network structure and stabilized in quality by heating a fiber bundle obtained by mixing synthetic fibers having different melting point from the central part by microwave and further heating the peripheral part by hot air. CONSTITUTION:A fiber bundle obtained by mixing synthetic fibers having different melting point is passed through the interior of an applicator of microwave and heating from the fiber central part is carried out by the microwave. The fiber bundle is further heat-treated by passing the fiber bundle through a hot air heater and the peripheral part is heated to provide the fiber formed product suitable for ink occlusion body for marking pen, occlusion body of cosmetic solution, suction wick for aromatic, dental mouse piece, cigarette filter, etc.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、マーキングペン用イン
キ吸蔵体、化粧用溶液の吸蔵体、芳香剤用吸上げ芯、歯
科用マウスピース、シガレットフィルター及び各種フィ
ルター等に適用することができる繊維束を提供する繊維
成形物の製造方法に関する。
FIELD OF THE INVENTION The present invention can be applied to ink occluding bodies for marking pens, occlusion bodies for cosmetic solutions, wicks for fragrances, dental mouthpieces, cigarette filters and various fibers. The present invention relates to a method for manufacturing a fiber molded product that provides a bundle.

【0002】[0002]

【従来の技術】従来より、マーキングペンにおけるイン
キ吸蔵体は、熱溶融性の捲縮状短繊維と、該繊維より融
点が高い捲縮状短繊維を混合して繊維束とし、これを熱
風、或いは遠赤外線等で加熱して作製されていた。
2. Description of the Related Art Conventionally, an ink occlusion body for a marking pen has a heat-meltable crimped short fiber and crimped short fiber having a melting point higher than that of the fiber to form a fiber bundle. Alternatively, it was manufactured by heating with far infrared rays or the like.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記し
た方法では、直径が小さい吸蔵体、例えば5mmφ以下
を製造する場合には問題が少ないが、それ以上の径の吸
蔵体、例えば20mmφ程度を製造する場合、以下のよ
うな問題がある。 (1)繊維束の外周部から加熱されるために、繊維束の
外周部においては熱溶融性の捲縮状短繊維が熱溶融し、
繊維同士を接着(点接着)させるが、繊維束の中心部に
おいては熱が充分に伝熱・供給されないために、上記し
た点接着が不十分となる。即ち、繊維束の外周部におい
ては比較的密な網状構造が形成され、中心部においては
比較的粗な構造となるために、浸透圧の不均一が生じ、
インキが外周部に移行する傾向がある。したがって、肝
心な中心部に接合しているペン先体からのインキのフロ
ーが不安定になるという欠点がある。また、繊維束の中
心部は、ほとんど無処理の状態であるため、外周部のよ
うに繊維が点接着することにより繊維同士で拘束し合う
こともないので、衝撃によるスリップ現象を起こす。 (2)繊維自体の伝熱性が低く、しかも空隙が存在する
ために、断熱効果が高く、熱上昇速度が低い。したがっ
て、加熱処理に要する時間が長く掛かり、生産性が悪
い。尚、加熱温度を上げると、幾分加熱時間を短縮する
ことができるが、他の繊維熱劣化(軟化)させるおそれ
があるために加熱温度の上昇限界があるため、大した効
果をあげることができない。 (3)加熱装置自体、例えば加熱炉をまず加熱する必要
があるため、無駄な(被加熱物を加熱する以外に消費さ
れる)エネルギーを必要とし、コスト高になり、ユーザ
の要望に応じ切れない面が多かった。
However, in the above-mentioned method, there are few problems when producing an occlusion body having a small diameter, for example, 5 mmφ or less, but an occlusion body having a diameter larger than that, for example, about 20 mmφ is produced. In this case, there are the following problems. (1) Since the heat is applied from the outer peripheral portion of the fiber bundle, the heat-meltable crimped short fibers are melted in the outer peripheral portion of the fiber bundle,
Although the fibers are bonded (spot-bonded) to each other, the above-described point-bonding is insufficient because heat is not sufficiently transferred / supplied in the central portion of the fiber bundle. That is, a relatively dense net-like structure is formed in the outer peripheral portion of the fiber bundle, and a relatively coarse structure is formed in the central portion, resulting in non-uniform osmotic pressure.
The ink tends to migrate to the outer periphery. Therefore, there is a drawback that the flow of ink from the pen tip that is joined to the essential center becomes unstable. In addition, since the central portion of the fiber bundle is almost untreated, the fibers are not constrained by the fibers due to point-bonding as in the outer peripheral portion, which causes a slip phenomenon due to impact. (2) The heat conductivity of the fiber itself is low, and since voids are present, the heat insulating effect is high and the rate of heat rise is low. Therefore, the heat treatment takes a long time and the productivity is poor. Incidentally, if the heating temperature is raised, the heating time can be shortened to some extent, but there is a limit to the heating temperature due to the possibility of heat deterioration (softening) of other fibers, so that a great effect can be obtained. Can not. (3) Since it is necessary to first heat the heating device itself, for example, the heating furnace, wasteful energy (consumed in addition to heating the object to be heated) is required, resulting in high cost and not meeting the user's request. There were many things that did not exist.

【0004】[0004]

【課題を解決するための手段】本発明は、上記に鑑み提
案されたもので、融点が異なる合成繊維を混合してなる
繊維束を、マイクロ波加熱工程で中心部から加熱し、そ
の後、熱風加熱工程で外周部を加熱することにより、繊
維同士を部分的に熱融着させるようにしたことを特徴と
する繊維成形物の製造方法に関するものである。
The present invention has been proposed in view of the above, and a fiber bundle formed by mixing synthetic fibers having different melting points is heated from the center in a microwave heating step, and then hot air is blown. The present invention relates to a method for producing a fiber molded product, characterized in that the fibers are partially heat-sealed by heating the outer peripheral portion in the heating step.

【0005】上記したように、本発明は融点が異なる合
成樹脂を混合してなる繊維束を加熱処理することによ
り、低融点の繊維を熱溶融させて繊維同士を熱融着(点
接着)させるものである。そして、その際、加熱手段と
してマイクロ波加熱を採用することにより、高速で、且
つ均一な点接着を施すようにしたものである。
As described above, according to the present invention, a fiber bundle formed by mixing synthetic resins having different melting points is heat-treated to heat-melt the low-melting-point fibers and heat-bond (fiber-bond) the fibers together. It is a thing. Then, at that time, by adopting microwave heating as the heating means, high-speed and uniform point bonding is performed.

【0006】熱溶融する繊維(誘導体)をマイクロ波の
電界中に通過させると、双極子がマイクロ波の電場によ
り激しく振動回転し、その摩擦熱のために誘導体自身を
発熱させる。上記したマイクロ波を利用した加熱処理
は、以下のような特徴を有するものである。 高速加熱 マイクロ波は、瞬間的に被加熱物の中に浸透し、熱エネ
ルギーを変換するため熱伝導に要する時間が極めて短
く、数秒から数分で発熱する。 高速応答性能 マイクロ波エネルギーは、光速度(3×108 m/se
c)で伝導する高速応答性能を有しているので、瞬時の
起動・停止及び出力調整のコントロールを簡単に行なう
ことができる。 均一加熱 被加熱物の中心部より発熱するので、その内部まで均一
に加熱することができる。 高い熱効率 被加熱物自体が発熱体となるため、周囲の空気や加熱炉
を熱する必要がないためエネルギーロスがない。したが
って、高い熱効率が得られ、省エネルギー化を計ること
ができる。
When a heat-melting fiber (derivative) is passed through an electric field of microwaves, the dipole vibrates and vibrates violently due to the electric field of microwaves, and the friction itself causes the dielectric itself to generate heat. The heat treatment using microwaves described above has the following features. The high-speed heating microwave instantaneously penetrates into the object to be heated and converts heat energy, so that the time required for heat conduction is extremely short and heat is generated in a few seconds to a few minutes. High-speed response performance Microwave energy has a light velocity (3 × 10 8 m /
Since it has a high-speed response performance conducted in c), it is possible to easily control instantaneous start / stop and output adjustment. Uniform heating Since heat is generated from the central part of the object to be heated, it is possible to uniformly heat the inside thereof. High thermal efficiency Since the object to be heated itself becomes a heating element, there is no need to heat the surrounding air or heating furnace, so there is no energy loss. Therefore, high thermal efficiency can be obtained and energy saving can be achieved.

【0007】本発明の製造方法においては、まず、マイ
クロ波のアプリケーターに入る前にジェット熱風予熱装
置(80〜100℃)にて繊維を予熱する。次に、マイ
クロ波のアプリケータ内を通過させ、マイクロ波により
繊維の中心部より加熱させる。加熱状況は、マイクロ波
の出力により調整される。その後、熱風(110℃前
後)加熱装置内を通過させ、熱処理を行なう。得られた
繊維束は、インキ吸蔵体として使用する際における外周
面からのインキの流出を防ぐために、ポリエステルフィ
ルム、また不織布からなる外被を被着して製品とする。
In the manufacturing method of the present invention, first, the fibers are preheated by a jet hot air preheating device (80 to 100 ° C.) before entering the microwave applicator. Next, it is passed through a microwave applicator and heated from the center of the fiber by microwaves. The heating status is adjusted by the microwave output. After that, heat treatment is performed by passing hot air (around 110 ° C.) through a heating device. The obtained fiber bundle is coated with a polyester film or an outer cover made of a non-woven fabric in order to prevent the ink from flowing out from the outer peripheral surface when it is used as an ink absorber.

【0008】上記したように、繊維束の外周面を保護す
るフィルムなどを外被として被着するようにしても良い
し、繊維束の外周面を樹脂成形体が覆うように一体状に
成形させても良い。この場合、前記と同様に、予熱、マ
イクロ波加熱、熱風加熱した繊維束を押し出し機に供給
し、外被成形する。
As described above, a film or the like for protecting the outer peripheral surface of the fiber bundle may be applied as the outer cover, or the outer peripheral surface of the fiber bundle may be integrally molded so as to cover it. May be. In this case, in the same manner as described above, the preheated, microwave heated, and hot air heated fiber bundles are supplied to the extruder to form the outer cover.

【0009】このように、本発明の繊維成形物の製造方
法は、融点の低い繊維がマイクロ波加熱により繊維束の
中心部から加熱され、熱風加熱により外部成形され、熱
溶融した融点の低い繊維が繊維同士を点接着し、繊維束
に均一な網状構造を形成させる。そして、このような繊
維成形物をインキ吸蔵体として使用すると、均一な網目
構造によりインキの局在化(外周部への移行)を防止す
ることができる。また、衝撃による繊維のスリップ現象
が防止され、インキが外周面から流出することもない。
As described above, according to the method for producing a fiber molded product of the present invention, the fiber having a low melting point is heated from the center of the fiber bundle by microwave heating and externally molded by hot air heating, and the heat-melted fiber having a low melting point is used. Point-bonds the fibers to each other, forming a uniform network structure in the fiber bundle. When such a fiber molded product is used as an ink occlusion body, it is possible to prevent the localization of the ink (migration to the outer peripheral portion) due to the uniform mesh structure. Further, the fiber slip phenomenon due to impact is prevented, and the ink does not flow out from the outer peripheral surface.

【0010】また、特に前記したようなフィルムや不織
布、或いは樹脂成形体などの外被を存在させないように
することもできる。この場合、前記した方法と同様に、
均一な網目構造を有する繊維束を作製し、これを成形し
ようとする寸法の筒型ヒーター(超耐熱性樹脂)に通
す。筒形ヒーターの温度を高く設定することにより、適
度な固さと不透水性を表面層を形成することができ、こ
の繊維成形物を必要とする寸法に切断して製品とすれば
良い。
Further, it is possible to prevent the film, the non-woven fabric, the resin molding or the like as described above from existing. In this case, similar to the method described above,
A fiber bundle having a uniform mesh structure is produced and passed through a tubular heater (super heat resistant resin) of a size to be formed. By setting the temperature of the tubular heater to be high, the surface layer can be formed with appropriate hardness and water impermeability, and this fiber molded product can be cut into a required size to obtain a product.

【0011】[0011]

【実施例】【Example】

実施例1 (繊維成形物にポリエステルフィルムによるラッピング
を施した製造例) A.試料 1)特殊繊維スライバー; 目付量6.8g/m ポリエステルスライバー(2.5d ,融点245℃) …70% 編成ポリエステルスライバー(2.5d ,融点110℃)…30% 2)外被;ポリエステルフィルム(巾23mm) 3)製品の規格、寸法; 直径6.6mmφ 長さ75.5mm B.各セクションの設定温度、及び条件 1)予熱装置; 温度80〜100℃ ジェット熱風量5.0m3 /min 2)マイクロウェーブ加熱装置; 出力パワー0.8kW 3)ユニジェット加熱装置; 温度110〜115℃ ジェット熱風量5.0m3 /min 4)冷却装置; 温度10〜15℃ ジェット風圧3kg/cm2
Example 1 (Production example in which a fiber molded product is wrapped with a polyester film) A. Sample 1) Special fiber sliver; Basis weight 6.8 g / m Polyester sliver (2.5 d , melting point 245 ° C) 70% Knitted polyester sliver (2.5 d , melting point 110 ° C) 30% 2) Jacket; Polyester film (width 23 mm) 3) Product specifications and dimensions; Diameter 6.6 mm φ Length 75.5 mm B. Set temperature and conditions of each section 1) Preheating device; Temperature 80 to 100 ° C. Jet hot air volume 5.0 m 3 / min 2) Microwave heating device; Output power 0.8 kW 3) Unijet heating device; Temperature 110 to 115 ℃ Jet hot air volume 5.0 m 3 / min 4) Cooling device; Temperature 10-15 ℃ Jet wind pressure 3 kg / cm 2

【0012】まず、特殊繊維スライバーを予熱装置の入
口より挿入する。次に、マイクロウェーブ加熱装置の入
口インレットアタッチメント(口径10mmφ)の中を
通過させ、同装置出口アウトレットアタッチメント(口
径8mmφ)を通過させる。さらに、ユニジェット加熱
装置入口(口径7mmφ)の中に入れ、出口側の成形用
サイジングヒーター(6.7mmφ)を通って、冷却装
置を通過させる。そして、巻上機巻管部に、予め装填し
たポリエステルフィルムと一緒に挿入し、巻管部におい
て、棒状になった特殊繊維をフィルムでラッピングしな
がら引出し、さらにラッピングヒーターで押えてラッピ
ングを施し、切断部で所定の長さに切断した。
First, the special fiber sliver is inserted from the inlet of the preheating device. Next, the mixture is passed through the inlet inlet attachment (diameter 10 mmφ) of the microwave heating device and the outlet outlet attachment (diameter 8 mmφ) of the device. Further, it is put into the inlet of the unijet heating device (diameter 7 mmφ), passed through the molding sizing heater (6.7 mmφ) on the outlet side and passed through the cooling device. Then, in the winding machine winding tube portion, inserted together with the polyester film loaded in advance, in the winding tube portion, draw out while wrapping the rod-shaped special fiber with the film, and further press the lapping heater to perform the wrapping, It cut | disconnected to the predetermined length in the cutting part.

【0013】実施例2 (繊維成形物にポリエステル不織布によるラッピングを
施した製造例)繊維成形物本体(繊維束)の製造方法に
ついては実施例1と殆ど変わりはないが、問題点はポリ
エステル不織布のラッピング融着温度が高いため、ラッ
ピングヒーター前部に熱風(温度200℃)吹出し装置
を取付け、ラッピングして製造した。
Example 2 (Production Example in which Fiber Molded Product is Wrapped with Polyester Nonwoven Fabric) The manufacturing method of the fiber molded product main body (fiber bundle) is almost the same as in Example 1, but the problem is that the polyester nonwoven fabric is used. Since the lapping fusion temperature is high, a hot air (temperature 200 ° C.) blowing device was attached to the front part of the lapping heater and lapping was performed.

【0014】上記した実施例1及び2で得られたインキ
吸蔵体は、繊維の融着具合、硬度、径の不同、繊維充填
量、インク吸上げ,保持,排出等テストの結果、ユーザ
の要求に応えられるものとなった。
The ink occlusion bodies obtained in Examples 1 and 2 described above were tested by the user according to the results of tests such as fusion of fibers, hardness, non-uniformity in diameter, fiber filling amount, ink absorption, retention, and ejection. It was able to meet.

【0015】実施例3 (繊維成形物に外被を設けないストリップタイプの製造
例) A.試料 1)特殊繊維スライバー; 目付量18g/m ポリエステルスライバー(2.5d ,融点245℃) …70% 編成ポリエステルスライバー(2.5d ,融点110℃)…30% 2)外被…なし 3)製品の規格、寸法; 直径12mmφ 長さ100mm B.各セクションの設定温度、及び条件 1)予熱装置; 温度80〜100℃ ジェット熱風量5.0m3 /min 2)マイクロウェーブ加熱装置; 出力パワー1.2kW 3)ユニジェット加熱装置; ジェット熱風量1.0〜1.2m3 /min 4)筒形成形伝熱ヒーター; 口径12mmφ 電圧220V,350W 設定温度200℃ 5)冷却装置; 温度10〜15℃ ジェット風圧3kg/cm2 6)巻上引取機; 引取速度5m/min 7)切断部回転数;50RPM
Example 3 (Strip type manufacturing example in which a fiber molded product is not provided with a jacket) A. Sample 1) Special fiber sliver; Unit weight 18 g / m Polyester sliver (2.5 d , melting point 245 ° C) ... 70% Knitted polyester sliver (2.5 d , melting point 110 ° C) ... 30% 2) Jacket ... None 3 ) Product specifications and dimensions; Diameter 12 mm φ Length 100 mm B. Set temperature and conditions of each section 1) Preheating device; Temperature 80 to 100 ° C Jet hot air flow rate 5.0 m 3 / min 2) Microwave heating device; Output power 1.2 kW 3) Unijet heating device; Jet hot air flow rate 1 0 to 1.2 m 3 / min 4) Tube-shaped heat transfer heater; Diameter 12 mmφ Voltage 220 V, 350 W Set temperature 200 ° C. 5) Cooling device; Temperature 10 to 15 ° C. Jet wind pressure 3 kg / cm 2 6) Winding take-up machine ; Drawing speed 5m / min 7) Cutting part rotation speed; 50RPM

【0016】このストリップタイプの棒状繊維成形物の
製造方法は、繊維成形物本体(繊維束)の製造について
は実施例1と変わらないが、この場合は外被がないの
で、ユニジェット加熱装置と冷却装置との中間に筒形成
形電熱ヒーターを設置する。そして、ユニジェット加熱
装置で中心部及び外周部とも均一に熱接着された棒状の
特殊繊維を同ヒーターを通過させることにより、中心部
より外周部(面)を一層固くし、所定の外径に絞りなが
ら冷却装置に導入し、さらに引取機を経て切断部に挿入
して所定の寸法に切断した。
The method for producing the strip-shaped rod-shaped fiber molded product is the same as that of Example 1 in the production of the fiber molded product main body (fiber bundle), but in this case, since there is no jacket, it can be used as a unijet heating device. A tube-shaped electric heater is installed in the middle of the cooling device. Then, the rod-shaped special fibers uniformly heat-bonded to the central portion and the outer peripheral portion of the unijet heating device are passed through the same heater to further harden the outer peripheral portion (face) from the central portion to a predetermined outer diameter. It was introduced into the cooling device while being squeezed, and was then inserted into the cutting portion through the take-up machine and cut into a predetermined size.

【0017】実施例4 (樹脂成形体が繊維成形物の外周面を覆うように一体状
に成形した製造例) A.試料 1)特殊繊維スライバー; 目付量20g/m ポリエステルスライバー(2.5d ,融点245℃) …70% 編成ポリエステルスライバー(2.5d ,融点110℃)…30% 2)外被;(ポリエチレン及びポリプロピレン外被) 樹脂 ウルトゼックス 3)製品の規格、寸法; 直径14mmφ 長さ93mm B.各セクションの設定温度、及び条件 1)予熱装置; 温度100〜115℃ ジェット熱風量5.0m3 /min 2)マイクロウェーブ加熱装置; アタッチメント IN20mmφ,OUT17mmφ 出力パワー1.2kW 3)ユニジェット加熱装置; チューブ口径16mmφ 温度110〜115℃ ジェット熱風量5.0m3 /min 4)押出機ダイス; 口金口径15mmφ ダイス温度170℃ 5)冷却水槽; サイジング14mmφ 水槽温度19℃ 6)引取速度; 15m/min 7)切断部回転数; 160RPM
Example 4 (Production example in which a resin molded body is integrally molded so as to cover the outer peripheral surface of a fiber molded article) A. Sample 1) Special fiber sliver; Unit weight 20 g / m Polyester sliver (2.5 d , melting point 245 ° C) 70% Knitted polyester sliver (2.5 d , melting point 110 ° C) 30% 2) Jacket; (Polyethylene) And polypropylene jacket) Resin Ultzex 3) Product specifications and dimensions; Diameter 14 mm φ Length 93 mm B. Set temperature and conditions of each section 1) Preheating device; Temperature 100 to 115 ° C. Jet hot air volume 5.0 m 3 / min 2) Microwave heating device; Attachment IN 20 mmφ, OUT 17 mmφ Output power 1.2 kW 3) Unijet heating device; Tube caliber 16mmφ Temperature 110-115 ° C Jet hot air volume 5.0m 3 / min 4) Extruder die; Die temperature 15mmφ Die temperature 170 ° C 5) Cooling water tank; Sizing 14mmφ Water tank temperature 19 ° C 6) Take-up speed; 15m / min 7 ) Cutting speed: 160RPM

【0018】この実施例4は、押出機による樹脂成形を
行なうものであるため、実施例1,2の製造方法とは、
若干製造方法が異なるところがある。即ち、第1工程の
予熱装置から特殊繊維スライバーを挿入し、第2工程の
マイクロウェーブ加熱装置を経て、第3工程のユニジェ
ット加熱装置までは、実施例1の製造工程と殆ど変わり
はない。そして、第4工程の押出セクションにおいて、
押出基本体に投入された樹脂(粒子)をスクリューで移
送する間に加熱して熱溶融させ、ダイス金型に挿入され
た特殊繊維の外周面にダイス内部において被覆、圧縮し
ながらサイジングに通して成形する。次いで、冷却水槽
内で冷却、凝固せしめ、引取機を通して切断機で所定の
長さに切断した。
Since Example 4 is to perform resin molding with an extruder, the manufacturing method of Examples 1 and 2 is
There are some differences in the manufacturing method. That is, the special fiber sliver is inserted from the preheating device of the first step, the microwave heating device of the second step is passed, and the unijet heating device of the third step is almost the same as the manufacturing process of the first embodiment. And in the extrusion section of the fourth step,
The resin (particles) put into the extrusion basic body is heated and melted by heat while being transferred by a screw, and the outer peripheral surface of the special fiber inserted into the die die is coated inside the die and passed through sizing while being compressed. Mold. Then, it was cooled and solidified in a cooling water tank, and cut into a predetermined length with a cutter through a take-up machine.

【0019】上記した実施例3及び4で得られたインキ
吸蔵体は、以下のような性状を示した。 外被(樹脂)と繊維が平均に密着している。 繊維と繊維が網目状に密着し、中心部、外周部とも均
一化している。 径の不同はなく、固さ、繊維の充填量が安定してい
る。 そして、繊維の融着具合、硬度、径の不同、繊維充填
量、インク吸上げ,保持,排出等テストの結果、ユーザ
の要求に応えられるものであった。
The ink occlusion bodies obtained in Examples 3 and 4 described above exhibited the following properties. The outer cover (resin) and fibers are in close contact on average. The fibers are in close contact with each other in a mesh shape, and are uniform in both the central part and the outer peripheral part. There is no difference in diameter, and hardness and the amount of fiber filled are stable. Then, as a result of tests such as fiber fusion, hardness, diameter difference, fiber filling amount, ink sucking, holding, and discharging, it was possible to meet the user's request.

【0020】[0020]

【発明の効果】以上説明したように、本発明の繊維成形
物の製造方法では、マイクロ波加熱を施すので、繊維束
の中心部から発熱し、融点の低い繊維が溶融して繊維同
士を融着(点接着)する。そして、均一に熱処理が施さ
れるので、上記した点接着により形成される網目構造が
均一化する。したがって、本発明により得られる繊維成
形物をマーキングペンのインキ吸蔵体として使用した場
合、ペン先体からのインキのフローが安定になり、衝撃
によるスリップ現象も起こさない。また、マイクロ波加
熱は、短時間に誘導体(繊維)を発熱させることができ
るので、処理時間が短く、生産性が良い。品質も安定す
る。さらに、マイクロ波加熱は、例えば加熱炉などを加
熱する必要がないため、エネルギー効率が高く、生産管
理も容易であり、生産コストも軽減することができる。
そして、本発明は、上記したインキ吸蔵体以外にも、化
粧用溶液の吸蔵体、芳香剤用吸上げ芯、歯科用マウスピ
ース、シガレットフィルター及び各種フィルター等を容
易に製造することができる。
As described above, in the method for producing a fiber molded product of the present invention, since microwave heating is performed, heat is generated from the central portion of the fiber bundle, the fibers having a low melting point are melted, and the fibers are fused to each other. Put on (point adhesion). Then, since the heat treatment is performed uniformly, the network structure formed by the point adhesion described above becomes uniform. Therefore, when the fiber molded product obtained according to the present invention is used as an ink occlusion body of a marking pen, the ink flow from the pen tip body becomes stable, and the slip phenomenon due to impact does not occur. In addition, since microwave heating can heat the derivative (fiber) in a short time, the processing time is short and the productivity is good. The quality is stable. Furthermore, since microwave heating does not require heating of, for example, a heating furnace, energy efficiency is high, production management is easy, and production cost can be reduced.
In addition to the above-mentioned ink occlusion body, the present invention can easily produce a cosmetic solution occlusion body, an aromatic wick, a dental mouthpiece, a cigarette filter and various filters.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 融点が異なる合成繊維を混合してなる繊
維束を、マイクロ波加熱工程で中心部から加熱し、その
後、熱風加熱工程で外周部を加熱することにより、繊維
同士を部分的に熱融着させるようにしたことを特徴とす
る繊維成形物の製造方法。
1. A fiber bundle formed by mixing synthetic fibers having different melting points is heated from the central portion in a microwave heating step, and then the outer peripheral portion is heated in a hot air heating step to partially bond the fibers to each other. A method for producing a fiber molded article, characterized in that it is heat-sealed.
JP3255959A 1991-09-09 1991-09-09 Production of fiber formed product Pending JPH0571058A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3255959A JPH0571058A (en) 1991-09-09 1991-09-09 Production of fiber formed product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3255959A JPH0571058A (en) 1991-09-09 1991-09-09 Production of fiber formed product

Publications (1)

Publication Number Publication Date
JPH0571058A true JPH0571058A (en) 1993-03-23

Family

ID=17285955

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3255959A Pending JPH0571058A (en) 1991-09-09 1991-09-09 Production of fiber formed product

Country Status (1)

Country Link
JP (1) JPH0571058A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0748771A (en) * 1993-06-18 1995-02-21 Rhone Poulenc Rhodia Ag Fiber strip with multi-width, method for preparing this and apparatus for practicing this method in use
EP0756935A2 (en) * 1995-08-02 1997-02-05 Canon Kabushiki Kaisha Absorber mounted in an ink tank and process for manufacturing this tank
WO1997020090A1 (en) * 1995-11-29 1997-06-05 Oji Paper Co., Ltd. Liquid absorbent material and process for preparing the same
JP2012025104A (en) * 2010-07-27 2012-02-09 Mitsubishi Pencil Co Ltd Fiber bundle and method for manufacturing the same
WO2017060094A1 (en) * 2015-10-06 2017-04-13 Gambro Lundia Ab Contact-free thermoforming of fiber bundles

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0748771A (en) * 1993-06-18 1995-02-21 Rhone Poulenc Rhodia Ag Fiber strip with multi-width, method for preparing this and apparatus for practicing this method in use
EP0756935A2 (en) * 1995-08-02 1997-02-05 Canon Kabushiki Kaisha Absorber mounted in an ink tank and process for manufacturing this tank
EP0756935A3 (en) * 1995-08-02 1998-07-01 Canon Kabushiki Kaisha Absorber mounted in an ink tank and process for manufacturing this tank
US6334674B1 (en) 1995-08-02 2002-01-01 Canon Kabushiki Kaisha Absorber mounted in an ink tank and process for manufacturing this tank
WO1997020090A1 (en) * 1995-11-29 1997-06-05 Oji Paper Co., Ltd. Liquid absorbent material and process for preparing the same
JP2012025104A (en) * 2010-07-27 2012-02-09 Mitsubishi Pencil Co Ltd Fiber bundle and method for manufacturing the same
WO2017060094A1 (en) * 2015-10-06 2017-04-13 Gambro Lundia Ab Contact-free thermoforming of fiber bundles
US10661228B2 (en) 2015-10-06 2020-05-26 Gambro Lundia Ab Contact-free thermoforming of fiber bundles

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