JPH08144120A - Production of thermoplastic resin fiber and apparatus therefor - Google Patents

Production of thermoplastic resin fiber and apparatus therefor

Info

Publication number
JPH08144120A
JPH08144120A JP30955394A JP30955394A JPH08144120A JP H08144120 A JPH08144120 A JP H08144120A JP 30955394 A JP30955394 A JP 30955394A JP 30955394 A JP30955394 A JP 30955394A JP H08144120 A JPH08144120 A JP H08144120A
Authority
JP
Japan
Prior art keywords
thermoplastic resin
fiber
spinners
spinner
fibers
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.)
Withdrawn
Application number
JP30955394A
Other languages
Japanese (ja)
Inventor
Susumu Kitani
進 木谷
Chikamichi Matsuyama
睦宙 松山
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.)
Nippon Muki Co Ltd
Original Assignee
Nippon Muki Co 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 Nippon Muki Co Ltd filed Critical Nippon Muki Co Ltd
Priority to JP30955394A priority Critical patent/JPH08144120A/en
Publication of JPH08144120A publication Critical patent/JPH08144120A/en
Withdrawn legal-status Critical Current

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Landscapes

  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)

Abstract

PURPOSE: To provide a process for producing a thermoplastic resin fiber and an apparatus for the production of the fiber by simultaneously fibrillating two or more kinds of raw material resins by centrifugal spinning and simultaneously collecting the fibers to form two or more kinds of fibers having different fiber properties in uniformly mixed state. CONSTITUTION: This apparatus for the production of a thermoplastic resin fiber is composed of a spinner for releasing a molten thermoplastic resin polymer through an orifice 17 by centrifugal force to form primary fibers and an air-blowing apparatus 16 to blow a high-speed air flow against the primary fiber to form a secondary fiber. In the above apparatus, two or more spinners are vertically arranged in plural stages and molten polymers of different raw materials are released through the orifices of these spinners.

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、遠心法により異なる繊
維特性を有する2種類以上の繊維を均一に混合形成する
ことができる熱可塑性樹脂繊維の製造方法とその製造装
置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a thermoplastic resin fiber capable of uniformly mixing and forming two or more kinds of fibers having different fiber characteristics by a centrifugal method, and an apparatus for producing the same.

【0002】[0002]

【従来の技術】従来、遠心法で異なる繊維特性を有する
2種類以上の繊維を混合形成する方法としては、特公昭
52−33229号公報に開示されているように、遠心
法で落下させる短繊維中にロービングまたはストランド
の開繊したものを吹き付け、これらを均一に混合させて
成形する鉱物質繊維マットの製造方法がある。また、別
の方法として、特開平6−166945号公報に開示さ
れているように、1つの樹脂を紡糸口に導くノズルオリ
フィスと他の樹脂を紡糸口に導くノズルオリフィスとを
ノズルピースの中心線上に巾方向に渡って交互に設けた
ダイヘッドを用いたメルトブロー法による方法がある。
2. Description of the Related Art Conventionally, as a method for mixing and forming two or more kinds of fibers having different fiber characteristics by a centrifugal method, as disclosed in Japanese Patent Publication No. 52-332229, a short fiber dropped by a centrifugal method is used. There is a method for producing a mineral fiber mat in which rovings or opened strands are sprayed, and these are uniformly mixed and molded. As another method, as disclosed in Japanese Patent Laid-Open No. 6-166945, a nozzle orifice that guides one resin to a spinning port and a nozzle orifice that guides another resin to a spinning port are on the center line of the nozzle piece. There is a method by a melt blow method using die heads alternately provided in the width direction.

【0003】[0003]

【発明が解決しようとする課題】前記従来例では、前者
の場合、2種類以上の材料からなる熱可塑性樹脂繊維の
不織布を得ようとすると、2種類以上の繊維を別々に製
綿して得た綿を乾式不織布製造装置にかけて製造しなけ
ればならない。そして、この方法を適用しようとする
と、多くの場合熱融着している高強度の綿を無理に開繊
することが必要であり、かつ、バインダーで再融着させ
なければならないというデメリットが大きい。また、繊
維が0.5d(デニール)以下の場合には、それに対応
できる乾式不織布製造装置がない。また、後者の場合、
メルトブロー法に使用できる樹脂は耐熱性を有するポリ
オレフィン系、ポリアミド系等に限定され、しかも、ダ
イヘッドの加熱制御上の問題から溶融粘度特性が近似す
るものの組合せしか実質上できないという問題がある。
In the former example, in the former case, when an attempt is made to obtain a non-woven fabric of thermoplastic resin fibers composed of two or more kinds of materials, two or more kinds of fibers are separately produced by cotton. The cotton must be applied to the dry non-woven fabric manufacturing equipment. And when trying to apply this method, in many cases it is necessary to forcibly open the high-strength cotton that is heat-sealed, and there is a big disadvantage that it must be re-sealed with a binder. . Further, when the fiber is 0.5 d (denier) or less, there is no dry-type nonwoven fabric manufacturing apparatus capable of coping with it. In the latter case,
The resins that can be used in the melt-blowing method are limited to heat-resistant polyolefin-based and polyamide-based resins, and there is a problem that only a combination of resins having similar melt viscosity characteristics can be practically used due to the problem of heat control of the die head.

【0004】[0004]

【課題を解決するための手段】本発明者等は、遠心法を
用いて、2種類以上の原料樹脂を同時に繊維化し、か
つ、同時に集綿して、異なる繊維特性を有する2種類以
上の繊維を均一に混合形成することができる熱可塑性樹
脂繊維の製造方法とその製造装置を提供することを目的
とし、本発明を完成させたものである。即ち、本発明の
熱可塑性樹脂繊維の製造方法は、熱可塑性樹脂の溶融ポ
リマーをスピナのオリフィスから遠心力により放出して
一次繊維化すると共にその放出される一次繊維に高速気
流を吹き付けて二次繊維化する熱可塑性樹脂繊維の製造
方法において、前記スピナを上下複数段に配置し、各ス
ピナより異なる原料の溶融ポリマーを放出させることを
特徴とする。また、本発明の熱可塑性樹脂繊維の製造装
置は、熱可塑性樹脂の溶融ポリマーをオリフィスから遠
心力により放出して一次繊維化するためのスピナと、前
記一次繊維に高速気流を吹き付けて二次繊維化するため
気流吹き付け装置とからなる熱可塑性樹脂繊維の製造装
置において、前記スピナを上下複数段に配置させたこと
を特徴とする。この場合、前記上下複数段に配置された
各スピナは、高周波加熱により各々別々に加熱制御する
ようにすることが好ましい。また、前記気流吹き付け装
置の高速気流の吹き出し口は、前記上下複数段に配置さ
れた各スピナのオリフィスの延長上に下方に向けて各々
設けることが好ましい。また、前記スピナの回転駆動軸
は中空管にて構成し、該中空管を介して各スピナに原料
の溶融ポリマーを供給するようにすることが好ましい。
Means for Solving the Problems The present inventors have used a centrifugal method to simultaneously fiberize two or more kinds of raw material resins and simultaneously collect cotton to obtain two or more kinds of fibers having different fiber characteristics. The present invention has been completed for the purpose of providing a method and an apparatus for producing a thermoplastic resin fiber capable of uniformly mixing and forming the same. That is, the method for producing a thermoplastic resin fiber of the present invention is a method in which a molten polymer of a thermoplastic resin is discharged from an orifice of a spinner by centrifugal force to form primary fibers and a high-speed air stream is blown to the discharged primary fibers to generate secondary fibers. In the method for producing a thermoplastic resin fiber to be fibrillated, the spinners are arranged in a plurality of upper and lower stages, and different spinners release molten polymers of different raw materials. Further, the apparatus for producing a thermoplastic resin fiber of the present invention comprises a spinner for releasing a molten polymer of a thermoplastic resin from an orifice by centrifugal force to form a primary fiber, and a secondary fiber by blowing a high-speed air stream on the primary fiber. In order to realize the above, in the apparatus for producing a thermoplastic resin fiber, which comprises an air flow blowing device, the spinners are arranged in a plurality of upper and lower stages. In this case, it is preferable that the spinners arranged in a plurality of upper and lower stages are individually controlled by high frequency heating. Further, it is preferable that the high-speed airflow outlet of the airflow blowing device is provided downward on each extension of the orifices of the spinners arranged in the upper and lower stages. Further, it is preferable that the rotation drive shaft of the spinner is formed of a hollow tube, and the molten polymer as a raw material is supplied to each spinner through the hollow tube.

【0005】[0005]

【作用】別々の原料溶融機で溶融した複数種の原料樹脂
を各原料投入管を通して各スピナに投入する。それぞれ
の溶融樹脂は、繊維化に適した温度に制御されたそれぞ
れのスピナより、そのオリフィスから遠心力により一次
繊維として放出される。放出された一次繊維は高速気流
(ブラスト気流)により延伸されながら2次繊維化さ
れ、下方の集綿ネット上に集綿される。その際、上段側
のスピナからの繊維と下段側のスピナからの繊維は互い
に絡み合いながら均一に混合されて集綿される。そのた
め、繊維化と同時に混合集綿が行なわれる。
Function: Plural kinds of raw material resins melted by different raw material melting machines are charged into each spinner through each raw material charging pipe. Each molten resin is discharged as a primary fiber from its orifice by centrifugal force from each spinner controlled to a temperature suitable for fiberizing. The discharged primary fibers are made into secondary fibers while being drawn by a high-speed air flow (blast air flow), and are collected on a lower cotton collecting net. At that time, the fibers from the upper spinner and the fibers from the lower spinner are uniformly mixed while being entangled with each other and collected. Therefore, mixed cotton collection is performed simultaneously with fiberization.

【0006】[0006]

【実施例】以下、本発明の実施例を図面に基づき説明す
る。図1は本発明による熱可塑性樹脂繊維の製造装置の
一実施例を示すもので、図中1は、外径130mm、内
径118mm、深さ30mmの上段スピナ、図中2は、
外径130mm、内径118mm、深さ30mmの下段
スピナを示し、これらスピナ1,2は同軸上に上下二段
に積層配置されている。該上段のスピナ1には回転駆動
軸3が接続され、回転ベルト4を介してモータ5により
所望速度で回転自在となっている。尚、図中6は回転駆
動軸3の支持部材を示す。該回転駆動軸3は中空管で構
成され、上下各スピナ1,2用の各原料溶融機7,8に
接続される原料投入管9,10を該中空管を介して上下
各スピナ1,2にそれぞれ導いている。また、各原料投
入管9,10には加熱ヒータ11,12が設けられ、ス
ピナ1,2へ導くまで原料樹脂の溶融状態を維持できる
ようになっている。スピナ1,2の加熱制御は、上段ス
ピナ1は上段スピナ用加熱コイル13を経て、下段スピ
ナ2は下段スピナ用加熱コイル14を経て高周波誘導加
熱装置15により行っている。尚、図中16は、スピナ
1,2のオリフィス17の延長上に下方に向けて二次繊
維化するための高速気流を吹き出す気流吹き付け装置を
示す。また、図中18は気流吹き付け装置16の気流吹
き出し口を示す。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows an embodiment of a thermoplastic resin fiber manufacturing apparatus according to the present invention, in which 1 is an upper spinner having an outer diameter of 130 mm, an inner diameter of 118 mm and a depth of 30 mm, and 2 in the drawing is
A lower spinner having an outer diameter of 130 mm, an inner diameter of 118 mm, and a depth of 30 mm is shown, and the spinners 1 and 2 are coaxially stacked in two upper and lower layers. A rotary drive shaft 3 is connected to the upper spinner 1 and is rotatable at a desired speed by a motor 5 via a rotary belt 4. Incidentally, reference numeral 6 in the figure denotes a support member for the rotary drive shaft 3. The rotary drive shaft 3 is formed of a hollow tube, and raw material feeding pipes 9 and 10 connected to the raw material melting machines 7 and 8 for the upper and lower spinners 1 and 2 are connected to the upper and lower spinners 1 via the hollow tubes. , 2 respectively. Further, heaters 11 and 12 are provided in the raw material feeding pipes 9 and 10, respectively, so that the molten state of the raw material resin can be maintained until the raw materials are introduced into the spinners 1 and 2. The heating control of the spinners 1 and 2 is performed by the high frequency induction heating device 15 via the upper spinner 1 through the upper spinner heating coil 13 and the lower spinner 2 through the lower spinner heating coil 14. Reference numeral 16 in the figure denotes an air flow blowing device that blows down a high-speed air flow for secondary fiber formation on the extension of the orifices 17 of the spinners 1 and 2. In addition, reference numeral 18 in the drawing denotes an air flow outlet of the air flow blowing device 16.

【0007】かくして、前記製造装置によれば、所定の
回転速度で回転駆動されるスピナ1,2内に原料投入管
9,10を介して原料溶融機7,8よりそれぞれ別々の
溶融原料樹脂が供給され、これら原料樹脂はそれぞれの
スピナ1,2のオリフィス17から一次繊維化されて放
出され、気流吹き付け装置16によって高速気流を吹き
付けられて二次繊維化され、これら2種類の繊維は均一
に混合されながら集綿される。
Thus, according to the above-mentioned manufacturing apparatus, separate molten raw material resins are supplied from the raw material melting machines 7 and 8 through the raw material feeding pipes 9 and 10 into the spinners 1 and 2 which are rotationally driven at a predetermined rotational speed. These raw material resins are supplied and primary fibers are discharged from the orifices 17 of the spinners 1 and 2 and discharged, and a high-speed air stream is sprayed by the air stream spraying device 16 to form secondary fibers. Cotton is collected while being mixed.

【0008】図2は本発明による熱可塑性樹脂繊維の製
造装置の他実施例を示すもので、上段スピナ1と下段ス
ピナ2の間に断熱材19を介在させ、加熱温度の制御を
し易くしている。また、気流吹き付け装置16も、上下
スピナ1,2に別々に設け、それぞれの気流吹き出し口
18を、各スピナ1,2のオリフィス17の延長上に下
方に向けて高速気流を吹き出せるようにし、二次繊維化
も上下スピナ1,2とも確実に行えるようにした。尚、
前記実施例と作用的に同一部材は図中同一符号を付して
詳細な説明は省略した。
FIG. 2 shows another embodiment of the apparatus for producing thermoplastic resin fibers according to the present invention, in which a heat insulating material 19 is interposed between the upper spinner 1 and the lower spinner 2 to facilitate control of the heating temperature. ing. In addition, the air flow blowing device 16 is also provided separately for the upper and lower spinners 1 and 2, so that each air flow outlet 18 can blow a high speed air flow downward on the extension of the orifice 17 of each spinner 1, 2. Secondary fibers can be surely formed in the upper and lower spinners 1 and 2. still,
The same members as those of the above-described embodiment are designated by the same reference numerals in the drawings and their detailed description is omitted.

【0009】次に、前記製造装置を用い、繊維化し、混
合集綿した製造方法の実施例を示す。 (実施例1)2種類の原料樹脂としてポリプロピレン
(三菱油化株式会社製 MR002V、融点167℃、
メルトフローレイト240g/10分)と、アスファル
ト(昭和シェル株式会社製 プレパウダーアスファル
ト、軟化点95〜120℃)を用いた。上段スピナの温
度を260℃とし、ポリプロピレンを投入し、下段スピ
ナの温度を200℃とし、アスファルトを投入した。ス
ピナの回転速度は3000rpm、ブラスト気流温度は
約230℃で、噴出速度300m/sの条件で繊維化し
た。
Next, an example of a manufacturing method in which the above-mentioned manufacturing apparatus is used to make fibers, and mixed and collect cotton is shown. Example 1 Polypropylene (MR002V manufactured by Mitsubishi Yuka Co., Ltd., melting point 167 ° C.) as two kinds of raw material resins,
Melt flow rate 240 g / 10 minutes) and asphalt (pre-powder asphalt manufactured by Showa Shell Co., Ltd., softening point 95 to 120 ° C.) were used. The temperature of the upper spinner was set to 260 ° C, polypropylene was added, the temperature of the lower spinner was set to 200 ° C, and asphalt was added. The spinner was rotated at 3000 rpm, the blast airflow temperature was about 230 ° C., and the fibers were spun into fibers at a jet speed of 300 m / s.

【0010】得られた不織布は、白色のポリプロピレン
繊維と黒色のアスファルト繊維が均一に混合されてい
た。また、それぞれの平均繊維径を測定したところ、ポ
リプロピレン繊維が約2μmで、アスファルト繊維が約
30μmであった。前記実施例で明らかなように本発明
によれば、2種類以上の原料から混合不織布が製造でき
ることが明らかである。
The non-woven fabric obtained was a uniform mixture of white polypropylene fibers and black asphalt fibers. Further, when the average fiber diameter of each was measured, the polypropylene fiber was about 2 μm and the asphalt fiber was about 30 μm. As is clear from the above examples, according to the present invention, it is clear that a mixed nonwoven fabric can be produced from two or more kinds of raw materials.

【0011】[0011]

【発明の効果】本発明によれば、遠心法を用いて2種類
以上の原料を同時に繊維化し、かつ、同時に集綿するこ
とにより、異なる繊維特性を有する2種類以上の繊維を
均一に混合形成することができる。従って、従来2種以
上の原料を用いて不織布を製造する際に必要であった、
開繊等が必要でなくなった。また、2種同時製綿のため
時間的なメリットも大きい。
EFFECTS OF THE INVENTION According to the present invention, two or more kinds of raw materials having different fiber characteristics are uniformly mixed and formed by simultaneously centrifuging two or more kinds of raw materials using a centrifugal method and collecting cotton simultaneously. can do. Therefore, conventionally, it was necessary to manufacture a nonwoven fabric using two or more kinds of raw materials,
No need to open the fiber. In addition, since two types of cotton are made simultaneously, there are significant time advantages.

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

【図1】本発明装置の一実施例の断面図FIG. 1 is a sectional view of an embodiment of the device of the present invention.

【図2】本発明装置の他の実施例の要部断面図FIG. 2 is a sectional view of a main part of another embodiment of the device of the present invention.

【符号の説明】[Explanation of symbols]

1 上段スピナ 2 下段スピナ 3 回転駆動軸 4 回転ベルト 5 モータ 6 支持部材 7 原料溶融機 8 原料溶融機 9 原料投入管 10 原料投入管 11 加熱ヒータ 12 加熱ヒータ 13 加熱コイル 14 加熱コイル 15 高周波誘導加熱装置 16 気流吹き付け装置 17 オリフィス 18 気流吹き出し口 19 断熱材 1 Upper Spinner 2 Lower Spinner 3 Rotating Drive Shaft 4 Rotating Belt 5 Motor 6 Supporting Member 7 Raw Material Melting Machine 8 Raw Material Melting Machine 9 Raw Material Feeding Pipe 10 Raw Material Feeding Pipe 11 Heating Heater 12 Heating Heater 13 Heating Coil 14 Heating Coil 15 High Frequency Induction Heating Device 16 Airflow spraying device 17 Orifice 18 Airflow outlet 19 Thermal insulation

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 熱可塑性樹脂の溶融ポリマーをスピナの
オリフィスから遠心力により放出して一次繊維化すると
共にその放出される一次繊維に高速気流を吹き付けて二
次繊維化する熱可塑性樹脂繊維の製造方法において、前
記スピナを上下複数段に配置し、各スピナのオリフィス
より異なる原料の溶融ポリマーを放出させることを特徴
とする熱可塑性樹脂繊維の製造方法。
1. Production of a thermoplastic resin fiber in which a molten polymer of a thermoplastic resin is discharged from an orifice of a spinner by centrifugal force to form a primary fiber, and a high speed air stream is blown to the released primary fiber to form a secondary fiber. In the method, the spinners are arranged in a plurality of upper and lower stages, and molten polymers of different raw materials are discharged from the orifices of the respective spinners.
【請求項2】 熱可塑性樹脂の溶融ポリマーをオリフィ
スから遠心力により放出して一次繊維化するためのスピ
ナと、前記一次繊維に高速気流を吹き付けて二次繊維化
するための気流吹き付け装置とからなる熱可塑性樹脂繊
維の製造装置において、前記スピナを上下複数段に配置
させたことを特徴とする熱可塑性樹脂繊維の製造装置。
2. A spinner for discharging a molten polymer of a thermoplastic resin from an orifice by centrifugal force to form primary fibers, and an air flow spraying device for spraying a high-speed air stream onto the primary fibers to form secondary fibers. The thermoplastic resin fiber manufacturing apparatus according to claim 1, wherein the spinners are arranged in a plurality of upper and lower stages.
【請求項3】 前記上下複数段に配置された各スピナを
高周波加熱により各々別々に加熱制御するようにしたこ
とを特徴とする請求項2記載の熱可塑性樹脂繊維の製造
装置。
3. The apparatus for producing a thermoplastic resin fiber according to claim 2, wherein the spinners arranged in a plurality of upper and lower stages are separately heated and controlled by high frequency heating.
【請求項4】 前記気流吹き付け装置の高速気流の吹き
出し口が、前記上下複数段に配置された各スピナのオリ
フィスの延長上に下方に向けて各々設けられたことを特
徴とする請求項2または3記載の熱可塑性樹脂繊維の製
造装置。
4. The high-speed airflow outlet of the airflow blowing device is provided downward on each extension of the orifices of the spinners arranged in the upper and lower stages. 3. The thermoplastic resin fiber manufacturing apparatus according to item 3.
【請求項5】 前記スピナの回転駆動軸を中空管にて構
成し、該中空管を介して各スピナに原料の溶融ポリマー
を供給するようにしたことを特徴とする請求項2乃至4
の何れかに記載の熱可塑性樹脂繊維の製造装置。
5. The spin drive shaft of the spinner is formed of a hollow tube, and the molten polymer as a raw material is supplied to each spinner through the hollow tube.
An apparatus for producing a thermoplastic resin fiber according to any one of 1.
JP30955394A 1994-11-19 1994-11-19 Production of thermoplastic resin fiber and apparatus therefor Withdrawn JPH08144120A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30955394A JPH08144120A (en) 1994-11-19 1994-11-19 Production of thermoplastic resin fiber and apparatus therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30955394A JPH08144120A (en) 1994-11-19 1994-11-19 Production of thermoplastic resin fiber and apparatus therefor

Publications (1)

Publication Number Publication Date
JPH08144120A true JPH08144120A (en) 1996-06-04

Family

ID=17994406

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30955394A Withdrawn JPH08144120A (en) 1994-11-19 1994-11-19 Production of thermoplastic resin fiber and apparatus therefor

Country Status (1)

Country Link
JP (1) JPH08144120A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014508230A (en) * 2011-02-07 2014-04-03 ファイブリオ・テクノロジー・コーポレーション Apparatus and method for depositing microfibers and nanofibers on a substrate
CZ307976B6 (en) * 2018-03-19 2019-09-25 Pardam s.r.o. Spinning head for producing bulky 3D fibre structures and the equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014508230A (en) * 2011-02-07 2014-04-03 ファイブリオ・テクノロジー・コーポレーション Apparatus and method for depositing microfibers and nanofibers on a substrate
CZ307976B6 (en) * 2018-03-19 2019-09-25 Pardam s.r.o. Spinning head for producing bulky 3D fibre structures and the equipment

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