TW201702443A - Apparatus and method for producing nanofiber - Google Patents

Apparatus and method for producing nanofiber Download PDF

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TW201702443A
TW201702443A TW105109425A TW105109425A TW201702443A TW 201702443 A TW201702443 A TW 201702443A TW 105109425 A TW105109425 A TW 105109425A TW 105109425 A TW105109425 A TW 105109425A TW 201702443 A TW201702443 A TW 201702443A
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gas
resin
raw material
discharge
pressure gas
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TW105109425A
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Chinese (zh)
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TWI711729B (en
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Morihiko Ikegaya
Hiroyoshi SOTA
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Saint Force Inc
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    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/08Melt spinning methods
    • D01D5/098Melt spinning methods with simultaneous stretching
    • D01D5/0985Melt spinning methods with simultaneous stretching by means of a flowing gas (e.g. melt-blowing)
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/08Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating
    • D04H3/16Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with bonds between thermoplastic filaments produced in association with filament formation, e.g. immediately following extrusion
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D13/00Complete machines for producing artificial threads
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D4/00Spinnerette packs; Cleaning thereof
    • D01D4/02Spinnerettes
    • D01D4/025Melt-blowing or solution-blowing dies
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H1/00Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/40Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties
    • D04H1/54Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties by welding together the fibres, e.g. by partially melting or dissolving
    • D04H1/56Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties by welding together the fibres, e.g. by partially melting or dissolving in association with fibre formation, e.g. immediately following extrusion of staple fibres
    • D04H1/565Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres without existing or potential cohesive properties by welding together the fibres, e.g. by partially melting or dissolving in association with fibre formation, e.g. immediately following extrusion of staple fibres by melt-blowing

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
  • Nonwoven Fabrics (AREA)
  • Artificial Filaments (AREA)

Abstract

An object of the present invention is to provide an apparatus and method for producing a nanofiber by using a melt blown method improving productivity. A pellet-shaped raw material (resin) fed into a hopper 2 is supplied and melted in a heating cylinder 3 heated by a heater 4, and sent to a front part of the heating cylinder 3 by a screw 5 rotated by a motor 6. The heating cylinder 3 is provided with a head portion 7, and a high-pressure gas is ejected from the gas ejection hole 71 provided at a center of the head portion 7. The melted resin sent to an end of the heating cylinder 3 is discharged from a resin discharging hole 73 having six superfine tubes provided in a downstream side of the resin ejection hole 73 through inside of the head portion 7. The melted resin discharged from the resin discharge hole 73 is elongated and a fiber having nanometer-order diameter can be formed.

Description

納米纖維製造裝置及納米纖維製造方法 Nanofiber manufacturing device and nanofiber manufacturing method

本發明係有關一種能夠藉由簡單的結構來提供高品質的納米纖維的納米纖維製造裝置及納米纖維製造方法。 The present invention relates to a nanofiber manufacturing apparatus and a nanofiber manufacturing method capable of providing high quality nanofibers by a simple structure.

近年來,隨著納米級直徑的纖維、所謂納米纖維的用途的擴大,需求急速提高。納米纖維隨著其用途的擴大,要求品質較高且與用途相對應之特殊的納米纖維。並且,關於納米纖維的製造,已知有電紡絲法或熔噴法等各種已知的方法,各個方法中存在優點及缺點。 In recent years, with the expansion of the use of nano-diameter fibers and so-called nanofibers, demand has rapidly increased. As its use expands, nanofibers require special nanofibers of higher quality and corresponding to their use. Further, various known methods such as an electrospinning method and a melt-blown method are known for the production of nanofibers, and there are advantages and disadvantages in each method.

作為上述背景技術,在專利文獻1中公開有在熔噴纖維中混入溶液吐出纖維之、由複數種纖維構成之不織布的製造方法。具體地係使溶液吐出纖維混入到藉由熔噴法從噴嘴吐出之熔噴纖維的纖維流中者,其中,前述溶液吐出纖維係利用使從液體吐出部吐出之紡絲溶液藉由從氣體吐出部噴出之氣體來噴出之溶液紡絲手段來吐出紡絲溶液並纖維化。 As a background art described above, Patent Document 1 discloses a method of producing a nonwoven fabric comprising a plurality of types of fibers in which a solution is discharged into a melt-blown fiber. Specifically, the solution discharge fiber is mixed into a fiber flow of the melt blown fiber discharged from the nozzle by a melt blow method, wherein the solution discharge fiber is discharged from the gas by the spinning solution discharged from the liquid discharge portion. The portion of the spun gas is ejected by the solution spinning means to discharge the spinning solution and fibrillate.

並且,在非專利文獻1中公開有關於基於電紡絲法之納米纖維的製造方法之內容。在該非專利文獻1中,公開有相對於在以往基於樹脂的膨潤需要溶劑之電紡絲法之納米纖維的製造,藉由進行不使用溶劑而基於熱之膨潤來防止使用溶劑時的引火、爆炸之構成等。並且對於基於熔噴法之納米纖維製造方法的缺陷亦進行詳述。 Further, Non-Patent Document 1 discloses a content of a method for producing a nanofiber based on an electrospinning method. In the non-patent document 1, it is disclosed that the production of nanofibers in the electrospinning method in which a resin is required for swelling by a resin is used to prevent ignition and explosion when using a solvent by using a solvent without using a solvent. The composition and so on. Further, the defects of the method for manufacturing a nanofiber based on the melt blow method are also described in detail.

專利文獻1:日本專利公開2010-185153號公報 Patent Document 1: Japanese Patent Publication No. 2010-185153

非專利文獻1:WEB-Journal No.151不織布增刊號(http://www.webj.co.jp/index.html) Non-Patent Document 1: WEB-Journal No. 151 Non-woven Supplemental Supplement (http://www.webj.co.jp/index.html)

如在上述非專利文獻1中亦記載,在基於以往的熔噴法之納米纖維的製造方法中為了使其纖維直徑變細,可以考慮以高速噴出高溫空氣之方法、及將聚合物的吐出抑制為較低之方法,但以高速噴出高溫空氣時,導致纖維直徑變細但纖維的長度變短而成為零碎狀,另一方面在將聚合物的吐出抑制為較低時,導致每單位時間的生產量顯著降低,任何情況下均難以大量生產品質良好的納米纖維。相對於此,電紡絲法中雖然生產性提高,但裝置變得複雜化,且需要應對引火.爆炸之對策,因此導致製造成本提高。 As described in the above-mentioned Non-Patent Document 1, in order to reduce the fiber diameter in the method for producing a nanofiber based on the conventional melt blow method, a method of ejecting high-temperature air at a high speed and suppressing discharge of a polymer can be considered. In the lower method, when the high-temperature air is ejected at a high speed, the diameter of the fiber is reduced, but the length of the fiber is shortened to be zero-grained, and on the other hand, when the discharge of the polymer is suppressed to be low, the per unit time is caused. The production volume is significantly reduced, and it is difficult to mass produce good quality nanofibers under any circumstances. On the other hand, in the electrospinning method, although the productivity is improved, the apparatus is complicated, and it is necessary to cope with the countermeasures of the ignition and the explosion, and thus the manufacturing cost is increased.

本發明係鑑於上述課題而完成者,其目的在於提供一種在熔噴方式的 納米纖維製造方法中能夠大量供給品質良好的納米纖維,且進一步可排除引火或爆炸的主要原因來提高安全性之納米纖維製造方法及納米纖維製造裝置。 The present invention has been made in view of the above problems, and an object thereof is to provide a melt blown method. In the nanofiber manufacturing method, a nanofiber having a good quality can be supplied in a large amount, and a nanofiber manufacturing method and a nanofiber manufacturing apparatus which can improve safety by further eliminating the cause of ignition or explosion can be further eliminated.

本發明的納米纖維製造裝置係具備相對於從高壓氣體噴出手段噴出之高壓氣流吐出液狀性原料之液狀性原料吐出手段之納米纖維製造裝置,其中,該液狀性原料吐出手段以從前述高壓氣體噴出手段噴出之高壓氣流為中心配置有複數個。 The nanofiber manufacturing apparatus of the present invention is a nanofiber manufacturing apparatus including a liquid material discharging means for discharging a liquid material from a high-pressure gas stream discharged from a high-pressure gas discharging means, wherein the liquid material discharging means is from the foregoing A plurality of high-pressure gas streams ejected by the high-pressure gas ejecting means are disposed in the center.

並且,本發明的納米纖維製造裝置中,前述液狀性原料吐出手段具備將原料熔融並進行擠出之擠出手段。 Further, in the nanofiber manufacturing apparatus of the present invention, the liquid material discharging means includes an extrusion means for melting and extruding the raw material.

並且,本發明的納米纖維製造裝置中,前述液狀性原料吐出手段具備供給熔解原料之手段。 Further, in the nanofiber manufacturing apparatus of the present invention, the liquid material discharging means includes means for supplying a melting material.

並且,本發明的納米纖維製造裝置中,在前述高壓氣體噴出手段上設置有用於供給高壓且高溫的氣體之氣體供給手段,從前述高壓氣體噴出手段以高壓噴出高溫的氣體。 Further, in the nanofiber manufacturing apparatus of the present invention, the high pressure gas discharge means is provided with a gas supply means for supplying a high-pressure and high-temperature gas, and the high-pressure gas discharge means discharges a high-temperature gas at a high pressure.

並且,本發明的納米纖維製造裝置中,具備能夠調整相對於從前述高壓氣體噴出手段噴出之高壓氣流之前述液狀性原料吐出手段的設置角度的 角度調整手段。 Further, the nanofiber manufacturing apparatus of the present invention includes an installation angle capable of adjusting the liquid material discharging means for the high-pressure air stream ejected from the high-pressure gas ejecting means. Angle adjustment means.

並且,本發明的納米纖維製造裝置中,至少兩個以上的前述液狀性原料吐出手段相對於前述高壓氣體噴出手段對稱配置。 Further, in the nanofiber manufacturing apparatus of the present invention, at least two or more of the liquid material discharging means are disposed symmetrically with respect to the high pressure gas discharging means.

並且,本發明的納米纖維製造裝置中,前述液狀性原料吐出手段在從前述高壓氣體噴出手段噴出之高壓氣流的周圍以等間隔配置。 Further, in the nanofiber manufacturing apparatus of the present invention, the liquid material discharging means is disposed at equal intervals around the high-pressure air stream ejected from the high-pressure gas ejecting means.

並且,本發明的納米纖維製造裝置中,從前述高壓氣體噴出手段噴出之高壓氣流設置於相對於納米纖維製造裝置的設置面垂直的方向。 Further, in the nanofiber manufacturing apparatus of the present invention, the high pressure gas stream ejected from the high pressure gas ejecting means is disposed in a direction perpendicular to the installation surface of the nanofiber manufacturing apparatus.

本發明的納米纖維製造方法係相對於從高壓氣體噴出手段噴出之高壓氣流,從液狀性原料吐出手段吐出液狀性原料來製造納米纖維之納米纖維製造方法,該納米纖維製造方法中,從以從前述高壓氣體噴出手段噴出之高壓氣流為中心而配置有複數個之前述液狀性原料吐出手段吐出液狀性原料時,調整從前述液狀性原料吐出手段相對於前述高壓氣流之液狀性原料的吐出角度。 The method for producing a nanofiber according to the present invention is a method for producing a nanofiber in which a liquid material is discharged from a liquid material discharge means with respect to a high-pressure gas stream discharged from a high-pressure gas discharge means to produce a nanofiber. When a plurality of the liquid material discharging means are disposed to discharge the liquid material from the high-pressure gas stream ejected from the high-pressure gas ejecting means, the liquid material is discharged from the liquid material discharging means to the high-pressure air stream. The angle of spit of raw materials.

而且,本發明的納米纖維製造方法係利用納米纖維製造裝置之納米纖維製造方法,前述納米纖維製造裝置具備被供給原料之加熱筒、對該加熱筒進行加熱之加熱手段、及在前述加熱筒內擠出原料之擠出裝置,前述方法中,在前述加熱筒的端部設置有噴射高壓氣體之氣體噴出口,在該氣體 噴出口的周圍設置有吐出在前述加熱筒內成為熔融狀態之原料之複數個原料吐出手段,藉由前述加熱手段對前述加熱筒進行加熱來使供給至前述加熱筒的內部之原料熔融或維持原料的熔融狀態,藉由前述擠出裝置來使原料從前述原料吐出手段吐出,藉由從前述氣體噴出口噴射之氣體生成氣流,藉由將前述吐出原料從外周搭載於噴出氣體的氣流來使其伸長並形成為納米級直徑的纖維。 Further, the nanofiber manufacturing method of the present invention is a nanofiber manufacturing method using a nanofiber manufacturing apparatus including a heating cylinder to which a raw material is supplied, a heating means for heating the heating cylinder, and a heating means in the heating cylinder An extrusion device for extruding a raw material, wherein in the method, a gas discharge port for injecting a high-pressure gas is provided at an end of the heating cylinder, A plurality of raw material discharge means for discharging the raw material which is in a molten state in the heating cylinder are provided around the discharge port, and the heating cylinder is heated by the heating means to melt or maintain the raw material supplied to the inside of the heating cylinder. In the molten state, the raw material is discharged from the raw material discharge means by the extrusion device, and a gas stream is generated from the gas injected from the gas discharge port, and the discharge raw material is charged from the outer circumference to the gas flow of the discharge gas. Fibers that are elongated and formed into nanometer diameters.

依本發明,能夠安全地製造直徑更小且品質更高的納米纖維。並且,在製造納米纖維時,能夠不使用利用高電壓之裝置而藉由設置複數個樹脂吐出手段來彌補作為基於熔噴方式之缺陷之每單位時間的生產量。 According to the present invention, it is possible to safely manufacture nanofibers having a smaller diameter and higher quality. Further, in the production of the nanofibers, it is possible to compensate for the throughput per unit time which is a defect based on the melt blow method by providing a plurality of resin discharge means without using a device using a high voltage.

以下對用於實施本發明之形態進行說明。當然,本發明在不違反其發明的趣旨之範圍內,能夠輕鬆地應用除在本實施形態中進行說明之構成以外的構成者自不必說。 The form for carrying out the invention will be described below. Needless to say, the present invention can be easily applied to components other than the configuration described in the embodiment without departing from the scope of the invention.

本發明係相對於以高壓噴出之流體(氣體狀的流體為較佳)供給液狀性原料來形成納米纖維者,但在本申請說明書中,未特別指定組成而稱作“氣體”時,係包含由所有組成或分子構造構成之氣體者。並且,在本申請說明書中,“原料”係指成形納米纖維時的所有的材料,在以下的實施例中,對於作為“原料”而使用合成樹脂之例子進行說明,但並不限定於此,可使用各種組成材料。並且,在本申請說明書中,術語“液狀性原料”並不限定於原料 的性狀為液體者,係包含在將固態的原料熔融並以擠出裝置進行擠出來形成納米纖維之實施例1中應用之“熔融原料”,且包含在對於規定的溶剤預先進行熔解以使固態的原料或液狀的原料成為規定濃度,並將其藉由適當的手段送給並從吐出口吐出或進行擠出來形成納米纖維之實施例2中應用之“熔解原料”者。亦即,本發明中之“液狀性原料”係指需要具有能夠從供給口(噴出口、吐出口)供給(噴出、吐出)“原料”之程度的黏性之性狀者,在本發明中,將具有該種液狀的性質之“原料”稱作“液狀性原料”。 In the present invention, a liquid material is supplied to a liquid material (a gas-like fluid is preferably used) to form a nanofiber. However, in the specification of the present application, when the composition is not specifically specified, it is called "gas". Contains gases consisting of all constituents or molecular structures. In the specification of the present application, the term "raw material" refers to all materials in the case of forming a nanofiber. In the following examples, an example in which a synthetic resin is used as a "raw material" will be described, but the invention is not limited thereto. Various constituent materials can be used. Moreover, in the specification of the present application, the term "liquid raw material" is not limited to the raw material. The trait of being a liquid is a "melting raw material" used in Example 1 in which a solid raw material is melted and extruded by an extrusion device to form a nanofiber, and is included in a predetermined melting solution to be solidified in advance. The raw material or the liquid material is a predetermined concentration, and is applied to a "melting material" used in Example 2 by a suitable means, which is sent out from a discharge port or extruded to form a nanofiber. In other words, the "liquid raw material" in the present invention means a viscous property which is required to be capable of supplying (discharging and discharging) "raw material" from a supply port (a discharge port or a discharge port), and is in the present invention. The "raw material" having such a liquid property is referred to as "liquid raw material".

詳細內容將進行後述,但作為本發明的實施例1及實施例2而進行說明之納米纖維製造裝置及納米纖維製造方法的共同之基本發明的概念如第11圖所示,在中心具備高壓氣體噴出手段71,在從高壓氣體噴出手段71噴出之高壓氣流90的周圍,複數個吐出液狀性原料之吐出手段73a的設置角度可改變。亦即,係可改變相對於高壓氣流90之液狀性原料的供給角度θ者。本發明的基本概念如第11圖所示,吐出液狀性原料之吐出手段73a相對於高壓氣流90的中心線91以供給角度θ配置,從複數個吐出手段73a吐出供給之吐出液狀性原料朝向高壓氣流90的中心線91而配置。從複數個吐出手段73a吐出供給之吐出液狀性原料以在中心線91上交叉之方式配置為較佳。 The details of the basic invention of the nanofiber manufacturing apparatus and the nanofiber manufacturing method described in the first and second embodiments of the present invention are as shown in Fig. 11, and the high pressure gas is provided at the center. The discharge means 71 can change the installation angle of the plurality of discharge means 73a for discharging the liquid raw material around the high-pressure gas stream 90 discharged from the high-pressure gas discharge means 71. That is, the supply angle θ of the liquid material relative to the high pressure gas stream 90 can be changed. In the basic concept of the present invention, as shown in Fig. 11, the discharge means 73a for discharging the liquid material is disposed at a supply angle θ with respect to the center line 91 of the high-pressure air stream 90, and the discharged liquid material is discharged from a plurality of discharge means 73a. It is disposed toward the center line 91 of the high pressure airflow 90. It is preferable to discharge the liquid material to be discharged from the plurality of discharge means 73a so as to intersect the center line 91.

在第11圖中,各構成要件的配置狀態如上,位置関係則如下。若將該些以高壓氣體的氣體噴出口71(開口噴嘴)的位置為基準,以後退至比其更靠下游側之位置関係來表示,則a為自吐出手段73a的吐出口之原料吐出 口後退距離,b為自吐出手段73a的吐出口之吐出原料交差之位置的後退距離,c為吐出手段73a的吐出口的開口直徑,d為氣體噴出口間隙。 In Fig. 11, the arrangement state of each constituent element is as above, and the positional relationship is as follows. When the position of the gas discharge port 71 (opening nozzle) of the high-pressure gas is used as a reference, and then the positional relationship is further described on the downstream side, a is discharged from the raw material of the discharge port of the discharge means 73a. The port receding distance, b is the retreat distance from the discharge port of the discharge port 73a, and c is the opening diameter of the discharge port of the discharge means 73a, and d is the gas discharge port gap.

在此,係如下構成者:相對於高壓氣流90的中心線91,吐出液狀性原料之吐出手段73a以供給角度θ配置,以tanθ=d/(b-a)(1)表示之原料供給正切角度θ能夠在0°<θ<90°的範圍內調整。作為一例,原料吐出口後退距離a=30mm,吐出口開口直徑c=2mm,氣體噴出口間隙d=7mm,將噴出高壓氣體的壓力設為約0.15MPa時,期望θ=20°±10°。 Here, it is assumed that the discharge means 73a for discharging the liquid raw material is disposed at the supply angle θ with respect to the center line 91 of the high-pressure airflow 90, and the raw material supply tangent angle is represented by tan θ = d / (ba) (1). θ can be adjusted within a range of 0° < θ < 90°. As an example, when the raw material discharge port retreat distance a=30 mm, the discharge port opening diameter c=2 mm, the gas discharge port gap d=7 mm, and the pressure at which the high pressure gas is discharged is about 0.15 MPa, θ=20°±10° is desirable.

如此,原料供給正切角度θ係應由原料吐出口後退距離a、吐出原料交差位置後退距離b、氣體噴出口間隙d而決定者,而且,係應由高壓氣體的噴出口開口直徑c、噴出高壓氣體的壓力及溫度之間的關係而決定者。 In this way, the raw material supply tangent angle θ should be determined by the raw material discharge port retreat distance a, the discharge material intersection position retreat distance b, and the gas discharge port gap d, and the high-pressure gas discharge port opening diameter c and the discharge high pressure should be The relationship between the pressure of the gas and the temperature is determined.

在本發明的實施例1的納米纖維製造裝置及納米纖維製造方法中,將投入於料斗中之顆粒狀的原料(樹脂)供給至藉由加熱器進行加熱之加熱筒內來進行熔融,並藉由以馬達進行旋轉之螺桿來送出到加熱筒的前方。在加熱筒上設置有頭部,從形成於頭部的中心之氣體噴出口噴出高壓氣體。到達至加熱筒的前端之液狀性熔融原料(熔融樹脂)經由頭部的內部而從配置於氣體噴出手段的下游側之複數根極細管的液狀性熔融原料(熔融樹脂)的供給手段(吐出手段)被供給(吐出)。複數根的極細管的液狀性熔融原料吐出手段均勻地配置於在中心配置之氣體噴出口的周圍。藉此,使從液狀性熔融原料吐出手段吐出之熔融樹脂拉伸,並形成納米級直徑的纖維。 In the nanofiber manufacturing apparatus and the nanofiber manufacturing method according to the first embodiment of the present invention, the particulate raw material (resin) charged in the hopper is supplied to a heating cylinder heated by a heater to be melted, and borrowed. It is sent out to the front of the heating cylinder by a screw that is rotated by a motor. A head is provided on the heating cylinder, and high-pressure gas is ejected from a gas discharge port formed at the center of the head. The liquid molten raw material (molten resin) that has reached the front end of the heating cylinder is supplied from a liquid molten raw material (molten resin) of a plurality of ultrafine tubes disposed on the downstream side of the gas discharge means through the inside of the head ( The spitting means is supplied (spit). The liquid molten raw material discharge means of the plurality of extremely thin tubes is uniformly disposed around the gas discharge port disposed at the center. Thereby, the molten resin discharged from the liquid molten raw material discharge means is stretched to form a fiber having a nanometer diameter.

在本發明的實施例2的納米纖維製造裝置及納米纖維製造方法中,以從形成於中心之氣體噴出口噴出高壓氣體之方式構成,相對於此,從配置於液狀性熔解原料吐出手段的下游側之複數根極細管的液狀性熔解原料吐出手段吐出高壓氣體。 In the nanofiber manufacturing apparatus and the nanofiber manufacturing method of the second embodiment of the present invention, the high-pressure gas is ejected from the gas ejection port formed at the center, and is disposed from the liquid-dissolving material discharging means. The liquid-melting raw material discharge means of the plurality of ultrafine tubes on the downstream side discharges the high-pressure gas.

(實施例1) (Example 1)

以下,對於本發明的實施例1中之納米纖維製造裝置的整體構成,依據第1圖~第3圖進行說明。 Hereinafter, the overall configuration of the nanofiber manufacturing apparatus in the first embodiment of the present invention will be described with reference to Figs. 1 to 3 .

作為本發明的實施例1,第1圖所示之納米纖維製造裝置1由以下構成:料斗2,用於將作為納米纖維的素材之樹脂(微細粒徑的粒體狀合成樹脂)投入到納米纖維製造裝置1中;加熱筒3,用於從料斗2接受樹脂的供給並使其加熱熔融;加熱器4,作為對加熱筒從外側進行加熱之加熱手段;螺桿5,能夠旋轉地容納於加熱筒3內,且作為用於藉由旋轉來使熔融樹脂向加熱筒3的前端移動之擠出裝置;馬達6,作為使螺桿5經由連結部61(詳細內容未圖示)進行旋轉之驅動手段;及圓柱狀的頭部7,設置於加熱筒3的前端,並且在內部具備用於使後述的熔融樹脂從周圍吐出之樹脂吐出手段,另外,具備從中心部噴射氣體狀的熱風之氣體噴出口71(開口噴嘴)。對於該圓柱狀頭部7,為了從中心部噴射噴射氣體,經由連結於作為氣體供給管之氣體配管部8之管道81供給高壓氣體。在氣體配管部8設置有加熱器等未圖示之加熱手段,且構成為從氣體噴出口71(開口噴嘴)噴 射熱風。另外,頭部7和加熱筒3經由O型環或環形狀的薄片構件等薄片部9而被連接,且具備熔融樹脂不會漏出到裝置外之構成。 In the first embodiment of the present invention, the nanofiber manufacturing apparatus 1 shown in Fig. 1 has a hopper 2 for putting a resin (fine particle size granular synthetic resin) as a material of nanofibers into the nanometer. In the fiber manufacturing apparatus 1, the heating cylinder 3 receives the supply of the resin from the hopper 2 and heat-melts it; the heater 4 serves as a heating means for heating the heating cylinder from the outside; and the screw 5 is rotatably accommodated in the heating. In the cylinder 3, as an extrusion device for moving the molten resin to the tip end of the heating cylinder 3 by rotation, the motor 6 is a driving means for rotating the screw 5 via the coupling portion 61 (not shown in detail) And a cylindrical head portion 7 provided at the front end of the heating cylinder 3, and having a resin discharge means for discharging a molten resin to be described later from the periphery, and a gas spray for ejecting a gaseous hot air from the center portion. Outlet 71 (open nozzle). In order to eject the injection gas from the center portion, the cylindrical head portion 7 supplies high-pressure gas via a pipe 81 connected to the gas pipe portion 8 as a gas supply pipe. The gas piping unit 8 is provided with a heating means (not shown) such as a heater, and is configured to be sprayed from the gas discharge port 71 (open nozzle). Shoot hot air. Further, the head portion 7 and the heating cylinder 3 are connected via a sheet portion 9 such as an O-ring or a ring-shaped sheet member, and have a configuration in which molten resin does not leak out of the apparatus.

在加熱筒3外周配置之複數個加熱器4藉由未圖示之控制手段構成為能夠各自独立或統一進行溫度控制。在本實施例中,如第1圖所示,示出配設有4台加熱器4者,但並不限定於此,可根據所使用之樹脂的素材或性質、加熱筒3的直徑或長度等諸多條件來改變設置數量,或改變各加熱器的大小,或適當改變配置條件。 The plurality of heaters 4 disposed on the outer circumference of the heating cylinder 3 are configured by control means (not shown) so that temperature control can be performed independently or collectively. In the present embodiment, as shown in Fig. 1, four heaters 4 are provided. However, the present invention is not limited thereto, and the diameter or length of the heating cylinder 3 may be different depending on the material or property of the resin to be used. Wait for a number of conditions to change the number of settings, or change the size of each heater, or change the configuration conditions appropriately.

第2圖係本實施例的納米纖維製造裝置1的俯視圖,第3圖係主視圖。第4圖至第6圖係表示頭部7的構造之說明圖。 Fig. 2 is a plan view of the nanofiber manufacturing apparatus 1 of the present embodiment, and Fig. 3 is a front view. 4 to 6 are explanatory views showing the configuration of the head 7.

如第3圖所示,在作為本發明的實施例之頭部7,從加熱筒3的外周經由氣體配管部8而連結有供給高壓氣體之管道81。來自管道81之高壓氣體被導入於頭部7的內部並從形成於中心部之氣體噴出口71(開口噴嘴:第3圖)噴出。在該氣體噴出口71的周圍,樹脂吐出手段73以等間隔配置有複數個。在本實施例中,樹脂吐出手段73設為由具備樹脂吐出針73a及具備將該樹脂吐出針73a安裝於頭部7之構造之樹脂吐出針安裝部73b構成者。 As shown in FIG. 3, in the head portion 7 which is an embodiment of the present invention, a duct 81 for supplying a high-pressure gas is connected from the outer circumference of the heating cylinder 3 via the gas piping portion 8. The high-pressure gas from the pipe 81 is introduced into the inside of the head portion 7 and is ejected from the gas discharge port 71 (opening nozzle: Fig. 3) formed at the center portion. A plurality of resin discharge means 73 are disposed at equal intervals around the gas discharge port 71. In the present embodiment, the resin discharge means 73 is constituted by a resin discharge needle attachment portion 73b having a resin discharge needle 73a and a structure in which the resin discharge needle 73a is attached to the head portion 7.

第3圖所示之頭部7具備遮蓋加熱筒3的前端部之加熱筒蓋部77、及作為保持樹脂吐出手段73之手段之樹脂吐出手段保持環部78。樹脂吐出手 段保持環部78相對於加熱筒蓋部77藉由螺栓等固定手段(無符號)而被固定。 The head portion 7 shown in Fig. 3 includes a heating cylinder cover portion 77 that covers the front end portion of the heating cylinder 3, and a resin discharge means holding ring portion 78 as a means for holding the resin discharge means 73. Resin spit out The segment holding ring portion 78 is fixed to the heating cylinder cover portion 77 by a fixing means (unsigned) such as a bolt.

藉由該樹脂吐出手段保持環部78將樹脂吐出手段73在氣體噴出口71(開口噴嘴)的周圍配置複數個時,將複數個樹脂吐出手段73以等間隔、等距離(自氣體噴出口之距離a)、或等角度(吐出角度θ)來設置,藉此能夠大幅提高具有均勻的直徑和纖維長度之納米纖維的生產量。 When a plurality of resin discharge means 73 are disposed around the gas discharge port 71 (opening nozzle) by the resin discharge means holding ring portion 78, a plurality of resin discharge means 73 are equally spaced and equidistant (from the gas discharge port) The distance a), or an equal angle (discharge angle θ) is set, whereby the production amount of the nanofiber having a uniform diameter and a fiber length can be greatly improved.

在此,藉由第11圖來對氣體噴出口71(開口噴嘴)和配置於周圍之樹脂吐出手段73的配置関係進行說明。藉由從配置於頭部7的中心部之氣體噴出口71噴出之氣流90而被噴出。相對於該氣流90,設置有在周圍配置有複數個之樹脂吐出手段73,從作為樹脂吐出口之樹脂吐出針73a,朝向藉由吐出角度θ從噴出口71噴出之氣流90被吐出。樹脂吐出針73a的樹脂吐出口配置於自噴出口71距離a的前方(沿著自噴出口71的氣流90時為下游側)。複數個樹脂吐出針73a的各樹脂吐出口以吐出樹脂朝向自噴出口71距離b的前方(沿著自噴出口71的氣流90時為下游側)交叉之方式被吐出。 Here, the arrangement relationship between the gas discharge port 71 (opening nozzle) and the resin discharge means 73 disposed in the periphery will be described with reference to FIG. The airflow 90 ejected from the gas discharge port 71 disposed at the center of the head portion 7 is ejected. In the air flow 90, a plurality of resin discharge means 73 are disposed around the resin discharge port 73a as a resin discharge port, and the air flow 90 discharged from the discharge port 71 by the discharge angle θ is discharged. The resin discharge port of the resin discharge needle 73a is disposed in front of the distance a from the discharge port 71 (downstream side along the air flow 90 from the discharge port 71). Each of the resin discharge ports of the plurality of resin discharge needles 73a is discharged so that the discharge resin crosses the front side of the distance b from the discharge port 71 (the downstream side when the air flow 90 from the discharge port 71 is downstream).

藉由改變作為複數個樹脂吐出手段73的配置條件之樹脂吐出手段73的數量、配置間隔、配置距離(自氣體噴出口的距離a)、配置角度(θ),亦能夠形成具有不均勻的直徑或纖維長度之納米纖維。因此根據所製造之納米纖維的用途來適當地選擇並改變樹脂吐出手段73的配置間隔等配置條 件即可。 By changing the number, arrangement interval, arrangement distance (distance a from the gas discharge port), and arrangement angle (θ) of the resin discharge means 73 as the arrangement conditions of the plurality of resin discharge means 73, it is also possible to form a non-uniform diameter. Or nanofibers of fiber length. Therefore, the arrangement bar such as the arrangement interval of the resin discharge means 73 is appropriately selected and changed depending on the use of the manufactured nanofibers. You can do it.

第4圖係第3圖的頭部7的A-A線處之剖面圖,第5圖(a)、第5圖(b)、第5圖(c)表示第4圖的頭部7的主要部位(B-B截面、C-C截面、D-D截面)處之各剖面圖。並且,第6圖係表示高壓氣體的流路A及熔融樹脂的流路B之說明圖。如第4圖至第6圖所示,在頭部7的內部等間隔地形成有與樹脂吐出手段73對應之6條樹脂流路75(圖中的箭頭B)。樹脂吐出手段73經由樹脂流路75連接於加熱筒3。藉由螺桿5的旋轉被擠壓之熔融樹脂向第5圖(c)的D-D剖面圖所示之樹脂流路75流入,經由C-C剖面圖所示之樹脂流路75,流入B-B剖面圖所示之樹脂吐出針安裝部73b的內部,且從樹脂吐出針73a吐出。並且此時,如第4圖所示,氣體流路72(圖中的箭頭A)以不干擾樹脂流路75(圖中的箭頭B)之方式形成於頭部7的中央,如第5圖(b)的C-C剖面圖所示,通過任意相鄰之樹脂流路75之間,且從頭部7的外側朝向內側改變方向而形成。經由管道81,氣體配管部8連接於氣體流路72。經由如此形成之氣體流路72,從氣體噴出口71(開口噴嘴)噴射藉由氣體噴射部8而供給之高壓且高溫的氣體。如此,樹脂流路75和氣體流路72在頭部7內互相不干擾而形成。另外,第7圖(b)中之符號79係相對於加熱筒蓋部77安裝管道(氣體流路)81時的螺紋部79。 Fig. 4 is a cross-sectional view taken along line AA of the head portion 7 of Fig. 3, and Fig. 5(a), Fig. 5(b), and Fig. 5(c) show main parts of the head portion 7 of Fig. 4. Cross-sectional views at (BB section, CC section, DD section). In addition, Fig. 6 is an explanatory view showing a flow path A of the high pressure gas and a flow path B of the molten resin. As shown in FIGS. 4 to 6 , six resin flow paths 75 (arrow B in the drawing) corresponding to the resin discharge means 73 are formed at equal intervals inside the head portion 7. The resin discharge means 73 is connected to the heating cylinder 3 via the resin flow path 75. The molten resin extruded by the rotation of the screw 5 flows into the resin flow path 75 shown in the DD sectional view of Fig. 5(c), and flows through the resin flow path 75 shown in the CC sectional view, and flows into the BB sectional view. The resin is discharged from the inside of the needle attachment portion 73b, and is discharged from the resin discharge needle 73a. At this time, as shown in Fig. 4, the gas flow path 72 (arrow A in the figure) is formed in the center of the head portion 7 so as not to interfere with the resin flow path 75 (arrow B in the figure), as shown in Fig. 5. The CC cross-sectional view of (b) is formed by passing between the adjacent resin flow paths 75 and changing directions from the outer side toward the inner side of the head portion 7. The gas piping portion 8 is connected to the gas flow path 72 via the pipe 81. Through the gas flow path 72 thus formed, the high-pressure and high-temperature gas supplied by the gas injection unit 8 is ejected from the gas discharge port 71 (open nozzle). In this manner, the resin flow path 75 and the gas flow path 72 are formed without interfering with each other in the head portion 7. Further, reference numeral 79 in Fig. 7(b) is a screw portion 79 when the duct (gas flow path) 81 is attached to the heating cylinder cover portion 77.

為了調節相對於樹脂吐出手段73的氣體流路72之配置條件,設置樹脂吐出手段73的保持調節手段74。然而,樹脂吐出手段73的樹脂吐出針 73a的樹脂吐出口的直徑非常小,非常易受裝置的振動、樹脂的壓力等應力的影響,有時亦會改變前述的樹脂吐出手段73的配置條件,或產生從頭部7的脫離。因此,即使調節改變樹脂吐出口74的角度,亦需要以不對樹脂吐出針73a施加應力之方式設為如樹脂吐出針73a不從頭部7脫離之構成。 In order to adjust the arrangement condition of the gas flow path 72 with respect to the resin discharge means 73, the holding adjustment means 74 of the resin discharge means 73 is provided. However, the resin discharge means 73 of the resin discharge means The resin discharge port of 73a has a very small diameter and is highly susceptible to stress such as vibration of the device or pressure of the resin, and may change the arrangement conditions of the resin discharge means 73 or the detachment from the head portion 7. Therefore, even if the angle at which the resin discharge port 74 is changed is adjusted, it is necessary to prevent the resin discharge needle 73a from being detached from the head portion 7 without applying stress to the resin discharge needle 73a.

第7圖(a)係表示基於樹脂吐出口支撐部74之支撐構造之說明圖,前述樹脂吐出口支撐部74用於將樹脂吐出手段73相對於樹脂吐出手段保持環部78固定且能夠調整其安裝角度。樹脂吐出手段73由樹脂吐出針73a和樹脂吐出針安裝部73b構成,樹脂吐出針安裝部73b藉由基於未圖示之螺合、卡合、銷等之適當的固定手段固定於頭部7的樹脂吐出手段保持環部78。在樹脂吐出針73a上設置有樹脂吐出口支撐部74。該樹脂吐出口支撐部74以從周圍把持樹脂吐出針73a之方式由樹脂吐出針把持部74a、及如第7圖所示具備從頭部7的外側朝向內部貫穿而設置之能夠進退之調整桿74c之調整手段74b構成。藉由使調整手段74b工作來使調整桿74c進退並使樹脂吐出針把持部74a朝向頭部7的直徑方向移動,藉此能夠將樹脂吐出針73a以所希望的位置、角度固定。藉由該種樹脂吐出口支撐部74,樹脂吐出手段73能夠以相對於來自氣體噴出口71之噴出氣流按照所希望的吐出角度來吐出吐出熔融樹脂之方式進行調整,且能夠以該角度可靠地固定。 (a) of FIG. 7 is an explanatory view showing a support structure of the resin discharge port support portion 74 for fixing the resin discharge means 73 to the resin discharge means holding ring portion 78 and adjusting the same. installation angle. The resin discharge means 73 is composed of a resin discharge needle 73a and a resin discharge needle attachment portion 73b, and the resin discharge needle attachment portion 73b is fixed to the head portion 7 by an appropriate fixing means such as screwing, engagement, or pin (not shown). The resin discharge means holds the ring portion 78. A resin discharge port support portion 74 is provided in the resin discharge needle 73a. The resin discharge port support portion 74 is provided with a resin discharge needle holding portion 74a so as to hold the resin discharge needle 73a from the periphery, and an adjustment rod 74c that can be moved forward and backward from the outer side of the head portion 7 as shown in Fig. 7 The adjustment means 74b is configured. By operating the adjustment means 74b, the adjustment lever 74c is moved forward and backward, and the resin discharge needle grip portion 74a is moved in the radial direction of the head portion 7, whereby the resin discharge needle 73a can be fixed at a desired position and angle. By the resin discharge port support portion 74, the resin discharge means 73 can adjust the discharge of the molten resin at a desired discharge angle with respect to the discharge airflow from the gas discharge port 71, and can reliably at this angle. fixed.

依該構成,作為相對於噴出氣流之熔融樹脂的吐出角度的調整手段而有用,且樹脂吐出針73a為非常細的管狀,其前端在納米纖維製造裝置1 運轉時有可能會由馬達6或螺桿5的驅動而导致大幅度地振動,但該樹脂吐出口支撐部74亦能夠有效地抑制該振動。另外,在本實施例的第2圖中將樹脂吐出手段73設為6根,將樹脂吐出口支撐部74相應地設置6台而示出,但並不限定於此,可根據所使用之樹脂、生產量、產品的特性等條件來適當地選擇其數量。 According to this configuration, it is useful as an adjustment means for the discharge angle of the molten resin of the discharge airflow, and the resin discharge needle 73a is a very thin tubular shape, and the tip end is in the nanofiber manufacturing apparatus 1 Although the motor 6 or the screw 5 may be driven to greatly vibrate during operation, the resin discharge port support portion 74 can effectively suppress the vibration. In the second embodiment of the present embodiment, six resin discharge means 73 are provided, and six resin discharge port support portions 74 are provided correspondingly. However, the present invention is not limited thereto, and may be used depending on the resin used. Conditions such as production volume and product characteristics are appropriately selected.

第7圖(b)中示出樹脂吐出手段73的角度調整功能的其他例子。在該實施例中,樹脂吐出口支撐部74亦以從周圍把持樹脂吐出針73a之方式由樹脂吐出針把持部74d、及具備從頭部7的外側朝向內部貫穿而設置之能夠進退的調整桿74e之調整手段(未圖示)構成。此時,使調整手段工作,藉此使調整桿74e進退來使樹脂吐出針把持部74d朝向頭部7的直徑方向移動,藉此能夠將樹脂吐出針73a以所希望的位置、角度來固定。此時,將樹脂吐出針安裝部73c設為球狀或圓柱狀,將如該樹脂吐出針安裝部73c成為旋轉、回轉自如之滑動面76形成於頭部7的樹脂吐出手段保持環部78,安裝樹脂吐出針安裝部73c,藉此能夠輕鬆地調整樹脂吐出針73a的角度。藉此,能夠不擔心樹脂吐出針73a的脫落而調整樹脂吐出手段73的角度。 Another example of the angle adjustment function of the resin discharge means 73 is shown in Fig. 7(b). In the embodiment, the resin discharge port support portion 74 is also provided with a resin discharge needle holding portion 74d so as to be able to advance and retreat from the outer side of the head portion 7 so as to hold the resin discharge needle 73a from the periphery. The adjustment means (not shown) is configured. At this time, the adjustment means is operated to move the adjustment rod 74e forward and backward, and the resin discharge needle holding portion 74d is moved in the radial direction of the head portion 7, whereby the resin discharge needle 73a can be fixed at a desired position and angle. At this time, the resin discharge needle attachment portion 73c is formed in a spherical shape or a columnar shape, and the resin discharge means retaining ring portion 78 which is formed on the head portion 7 by the sliding surface 76 which is rotatable and rotatable as the resin discharge needle attachment portion 73c is formed. By attaching the resin discharge needle attachment portion 73c, the angle of the resin discharge needle 73a can be easily adjusted. Thereby, the angle of the resin discharge means 73 can be adjusted without fear of falling off of the resin discharge needle 73a.

另外,氣體噴出口71和樹脂吐出手段73如圖示,構成為氣體噴出口71後退至比樹脂吐出手段73更靠下游側之位置而配置。藉由如此構成,沿著從氣體噴出口71噴射之氣體的噴出氣流的分佈而熔融樹脂漸漸被拉伸並成為納米級直徑的纖維狀。並且,藉由未圖示之加溫手段,從氣體噴射部8 噴射作為熱風之氣體,因此從樹脂吐出手段73吐出之樹脂與噴射常溫氣體時相比,能夠製造更長且纖維直徑更小的納米纖維。 In addition, as shown in the figure, the gas discharge port 71 and the resin discharge means 73 are disposed such that the gas discharge port 71 is retracted to a position on the downstream side of the resin discharge means 73. According to this configuration, the molten resin is gradually stretched along the distribution of the discharge gas flow of the gas ejected from the gas discharge port 71, and becomes a fiber having a nanometer diameter. Further, the gas ejecting unit 8 is provided by a heating means (not shown). Since the gas which is hot air is ejected, the resin discharged from the resin discharge means 73 can produce a nanofiber which is longer and has a smaller fiber diameter than when the normal temperature gas is ejected.

關於如上所述的構成的納米纖維製造裝置1的一系列的動作進行說明。投入到料斗2之原料(樹脂)在加熱筒3內藉由加熱器4而被加熱,藉此熔融,且藉由利用馬達6回轉之螺桿而送出到加熱筒3的前方。到達至加熱筒3的前端之熔融樹脂經由形成於頭部7的內部之6條樹脂流路75而從6根樹脂吐出針的原料吐出口被吐出。被吐出之熔融樹脂乘著藉由由氣體噴射部8供給且從氣體噴出口71噴射之高壓、高溫氣體而產生之氣流而被輸送。此時,藉由較快的高溫氣體的氣流與滯留於周圍之較慢的空氣之間的速度差,熔融樹脂被拉伸並形成納米纖維。 A series of operations of the nanofiber manufacturing apparatus 1 having the above configuration will be described. The raw material (resin) charged into the hopper 2 is heated by the heater 4 in the heating cylinder 3, melted, and sent out to the front of the heating cylinder 3 by the screw that is rotated by the motor 6. The molten resin that has reached the tip end of the heating cylinder 3 is discharged from the raw material discharge ports of the six resin discharge needles via the six resin flow paths 75 formed inside the head portion 7. The molten resin to be discharged is transported by the air current generated by the high-pressure, high-temperature gas supplied from the gas injection port 8 and injected from the gas discharge port 71. At this time, the molten resin is stretched and forms nanofibers by the speed difference between the gas stream of the faster high-temperature gas and the slower air trapped around.

(實施例2) (Example 2)

作為本發明的實施例1,對於使微細粒徑的粒體狀合成樹脂熔融並用作原料之納米纖維製造裝置進行了詳述,但如先前所述,作為納米纖維的液狀性原料並不限定於此,相對於規定的溶剤亦可以使用使固態的原料或液狀的原料預先進行熔解以成為規定濃度之熔解原料。其亦係液狀性原料。第8圖至第10圖表示用於由熔解原料形成納米纖維之納米纖維製造裝置。另外,對於與實施例1相同的構成賦予相同的符號,並省略其詳細說明。 In the first embodiment of the present invention, a nanofiber manufacturing apparatus that melts and uses a fine-grained granular synthetic resin as a raw material is described in detail. However, as described above, the liquid raw material as a nanofiber is not limited. Here, a solid raw material or a liquid raw material may be melted in advance to form a molten material having a predetermined concentration with respect to a predetermined solvent. It is also a liquid raw material. 8 to 10 show a nanofiber manufacturing apparatus for forming nanofibers from a molten raw material. The same components as those in the first embodiment are denoted by the same reference numerals, and their detailed descriptions are omitted.

在本發明的實施例2中,使用具有對熔解原料施加規定壓力來進行擠出之功能之溶剤儲存器5A來代替實施例1的料斗2、螺桿5、馬達6。規 定壓力可為基於因高低差而產生之重力之壓力。在頭部7A上連接有溶剤供給用較管3A及氣體噴射部8。雖省略了圖示,但用於噴出氣體之手段適當地配備於氣體噴射部8內或從高壓氣體供給部(未圖示)導入到氣體噴射部8內即可。在頭部7A上如第9圖所示設置有成為從氣體噴射部8供給之氣體的流路之氣體流路72A和氣體噴射口71A。並且,同様地在頭部7A設置有作為熔解原料的流路之樹脂流路75A,樹脂流路75A與樹脂吐出手段73相連接。樹脂吐出手段73的構成與實施例1同樣地由作為熔解原料的吐出口之樹脂吐出針73a、及在第8圖至第10圖中未圖示之樹脂吐出針安裝部構成。並且,在頭部7A設置有樹脂吐出手段保持板部78A,且在此設置由樹脂吐出針把持部74a、及具備從頭部7A的外側朝向內部貫穿而設置之能夠進退的調整桿74c之調整手段74b構成之樹脂吐出口支撐部74,藉此與實施例1同樣地能夠藉由樹脂吐出口支撐部74自如地調整樹脂吐出針73a的吐出角度。 In the second embodiment of the present invention, the hopper 2A having the function of applying a predetermined pressure to the molten material to perform the extrusion is used instead of the hopper 2, the screw 5, and the motor 6 of the first embodiment. regulation The constant pressure can be a pressure based on gravity generated by the height difference. The solvent supply tube 3A and the gas injection unit 8 are connected to the head portion 7A. Although not shown in the drawings, the means for ejecting the gas may be appropriately provided in the gas ejecting unit 8 or introduced into the gas ejecting unit 8 from a high-pressure gas supply unit (not shown). As shown in FIG. 9, the head 7A is provided with a gas flow path 72A and a gas injection port 71A which are flow paths of the gas supplied from the gas injection unit 8. Further, in the head portion 7A, a resin flow path 75A as a flow path of the melting material is provided, and the resin flow path 75A is connected to the resin discharge means 73. In the same manner as in the first embodiment, the resin discharge means 73 is composed of a resin discharge needle 73a as a discharge port of the melting material and a resin discharge needle attachment portion (not shown) in Figs. 8 to 10 . Further, the resin discharge device holding plate portion 78A is provided in the head portion 7A, and the resin discharge needle holding portion 74a and the adjustment means for providing the adjustment lever 74c that can be advanced and retracted from the outside of the head portion 7A are provided. In the same manner as in the first embodiment, the discharge angle of the resin discharge needle 73a can be freely adjusted by the resin discharge port support portion 74 in the same manner as in the first embodiment.

實施例2中之納米纖維製造裝置如第10圖所示,設置有兩個樹脂吐出手段73。當然,樹脂吐出手段73的配置並不限定於兩個,亦可以在氣體噴射口71A的周圍設置3個以上的樹脂吐出手段73。此時,期望均勻地設置樹脂吐出手段73。並且,圖中所示之實施例示出横噴出型,但只要係本領域技術人員則能夠輕鬆地想到將自氣體噴射口71A之氣體流路72A作為垂直方向來垂直(從上方向下方、或從下方向上方)地噴出之變形例。 As shown in Fig. 10, the nanofiber manufacturing apparatus in the second embodiment is provided with two resin discharge means 73. Needless to say, the arrangement of the resin discharge means 73 is not limited to two, and three or more resin discharge means 73 may be provided around the gas injection port 71A. At this time, it is desirable to uniformly provide the resin discharge means 73. Further, the embodiment shown in the drawing shows a horizontal discharge type, but it is easily exemplified by those skilled in the art that the gas flow path 72A from the gas injection port 71A is perpendicular to the vertical direction (from top to bottom, or from A modified example in which the lower side is sprayed upward.

藉由如此構成,與實施例1的構成相比,使用在溶剖中溶化有原料之 熔解原料,藉此能夠不使用加熱筒或馬達、螺桿等複雜的裝置而構成納米纖維製造裝置,因此裝置的尺寸變得緊湊,且能夠實現節省空間化。並且,裝置能夠緊湊地構成,藉此能夠構成輕便的納米纖維製造裝置。當為該種輕便型的納米纖維製造裝置時,能夠藉由朝向欲使納米纖維附著之位置噴吹納米纖維來形成納米纖維,且納米纖維的用途擴大。 According to this configuration, compared with the configuration of the first embodiment, the raw material is melted in the cross-section. By melting the raw material, the nanofiber manufacturing apparatus can be configured without using a complicated device such as a heating cylinder or a motor or a screw. Therefore, the size of the apparatus can be made compact, and space saving can be achieved. Further, the device can be configured compactly, whereby a portable nanofiber manufacturing device can be constructed. In the case of such a portable nanofiber manufacturing apparatus, nanofibers can be formed by blowing nanofibers toward a position where nanofibers are to be attached, and the use of the nanofibers is expanded.

以上,對本發明的實施例進行詳述,但本發明並非限定於前述實施例者,在本發明的要旨的範圍內可進行各種變形實施。例如,在上述實施例中,作為使熔融樹脂及氣體噴出口朝向水平方向之横向型的納米纖維製造裝置而示出,但並不限定於此,作為朝向下方構成之縦向型的納米纖維製造裝置及製造方法亦沒有任何問題。這種情形可有效地避免基於重力之影響。並且,將擠出裝置作為螺桿5進行說明,但需要所製造之納米纖維被截斷之対策,但即使藉由如模鑄般依次供給溶液並利用活塞等進行間斷的擠出亦沒有任何問題。而且,可使氣體噴出口71形成為錐狀並設為噴嘴形狀,並提高壓力而構成。而且,關於用於調整樹脂吐出針73a的角度之構造,舉出兩個具體例來進行說明,但例如只要為能夠調整蛇腹式的樹脂吐出手段等的角度的構造則可為任何形態。 The embodiments of the present invention have been described in detail above, but the present invention is not limited to the embodiments described above, and various modifications can be made without departing from the spirit and scope of the invention. For example, in the above-described embodiment, the nanofiber manufacturing apparatus which is a horizontal type in which the molten resin and the gas discharge port are oriented in the horizontal direction is shown. However, the present invention is not limited thereto, and is manufactured as a radial type nanofiber which is formed downward. There are no problems with the device and the manufacturing method. This situation can effectively avoid the influence based on gravity. Further, the extrusion device will be described as the screw 5, but the nanofibers to be produced are required to be cut off. However, there is no problem even if the solution is sequentially supplied by die casting and intermittently extruded by a piston or the like. Further, the gas discharge port 71 can be formed in a tapered shape and formed into a nozzle shape, and the pressure can be increased. In addition, the structure for adjusting the angle of the resin discharge needle 73a is described in two specific examples. For example, the structure may be any shape as long as it can adjust the angle of the resin discharge means of the bellows type.

1‧‧‧納米纖維製造裝置 1‧‧‧Nanofiber manufacturing equipment

2‧‧‧料斗 2‧‧‧ hopper

3‧‧‧加熱筒 3‧‧‧heating cylinder

4‧‧‧加熱器(加熱手段) 4‧‧‧heater (heating means)

5‧‧‧螺桿(擠出裝置) 5‧‧‧ screw (extrusion device)

6‧‧‧馬達(驅動手段) 6‧‧‧Motor (driver)

7‧‧‧頭部 7‧‧‧ head

71‧‧‧氣體噴出口 71‧‧‧ gas outlet

72‧‧‧氣體流路 72‧‧‧ gas flow path

73‧‧‧樹脂吐出手段 73‧‧‧Resin discharge means

73a‧‧‧樹脂吐出針(原料吐出口) 73a‧‧‧Resin spit out (raw material spit)

73b、73c‧‧‧樹脂吐出針安裝部 73b, 73c‧‧‧ resin spit needle installation

74‧‧‧樹脂吐出口支撐部 74‧‧‧Resin spout support

74a‧‧‧樹脂吐出針把持部 74a‧‧‧Resin spit out the needle grip

74b‧‧‧調整部 74b‧‧‧Adjustment Department

74c‧‧‧調整桿 74c‧‧‧Adjustment rod

75‧‧‧樹脂流路 75‧‧‧Resin flow path

76‧‧‧氣體流路 76‧‧‧ gas flow path

77‧‧‧加熱筒蓋部 77‧‧‧heating cylinder cover

78‧‧‧樹脂吐出手段保持環部 78‧‧‧Resin discharge means to keep the ring

8‧‧‧氣體噴射部(氣體噴射手段) 8‧‧‧ gas injection department (gas injection means)

81‧‧‧管道(氣體流路) 81‧‧‧Pipe (gas flow path)

90‧‧‧高壓氣流 90‧‧‧High pressure airflow

91‧‧‧高壓氣流的中心線 91‧‧‧Center line of high pressure airflow

第1圖係剖視表示本發明的納米纖維製造裝置的實施例1的整體構成之一部分之側視圖。 Fig. 1 is a side view showing a part of the overall configuration of a first embodiment of the nanofiber manufacturing apparatus of the present invention.

第2圖係作為本發明的實施例1之納米纖維製造裝置中之頭部及加熱 筒的外觀俯視圖。 Fig. 2 is a head and a heating in a nanofiber manufacturing apparatus of Example 1 of the present invention. The top view of the tube.

第3圖係表示作為本發明的實施例之納米纖維製造裝置中之頭部前端之外觀主視圖。 Fig. 3 is a front elevational view showing the front end of the head in the nanofiber manufacturing apparatus as an embodiment of the present invention.

第4圖係第3圖所示之納米纖維製造裝置的A-A線處之剖面圖。 Fig. 4 is a cross-sectional view taken along line A-A of the nanofiber manufacturing apparatus shown in Fig. 3.

第5圖係第4圖所示之納米纖維製造裝置的B-B線、C-C線、D-D線各處之剖面圖。 Fig. 5 is a cross-sectional view showing the B-B line, the C-C line, and the D-D line of the nanofiber manufacturing apparatus shown in Fig. 4.

第6圖係表示作為本發明的實施例1之納米纖維製造裝置中之頭部內部的樹脂流路及氣體流路之說明圖。 Fig. 6 is an explanatory view showing a resin flow path and a gas flow path inside the head in the nanofiber manufacturing apparatus of the first embodiment of the present invention.

第7圖係表示作為本發明的實施例1之納米纖維製造裝置中之第7圖(a)樹脂吐出手段的支撐構造的一例、第7圖(b)樹脂吐出手段的支撐構造的其他一例之說明圖。 Fig. 7 is a view showing an example of a support structure of the resin discharge means in Fig. 7 (a) of the nanofiber manufacturing apparatus according to the first embodiment of the present invention, and Fig. 7 (b) another example of the support structure of the resin discharge means. Illustrating.

第8圖係表示本發明的納米纖維製造裝置的實施例2的整體構成之側視圖。 Fig. 8 is a side view showing the overall configuration of a second embodiment of the nanofiber manufacturing apparatus of the present invention.

第9圖係表示本發明的納米纖維製造裝置的實施例2的整體構成之俯視圖。 Fig. 9 is a plan view showing the overall configuration of a second embodiment of the nanofiber manufacturing apparatus of the present invention.

第10圖係表示本發明的納米纖維製造裝置的實施例2的頭部構成之主視圖。 Fig. 10 is a front elevational view showing the head configuration of a second embodiment of the nanofiber manufacturing apparatus of the present invention.

第11圖係用於說明本發明的納米纖維製造裝置及納米纖維製造方法的基本發明概念之說明圖。 Fig. 11 is an explanatory view for explaining the basic inventive concept of the nanofiber manufacturing apparatus and the nanofiber manufacturing method of the present invention.

3‧‧‧加熱筒 3‧‧‧heating cylinder

4‧‧‧加熱器 4‧‧‧heater

5‧‧‧螺桿 5‧‧‧ screw

7‧‧‧頭部 7‧‧‧ head

9‧‧‧薄片部 9‧‧‧Sheet Department

71‧‧‧氣體噴出口 71‧‧‧ gas outlet

72‧‧‧氣體流路 72‧‧‧ gas flow path

73a‧‧‧樹脂吐出針(原料吐出口) 73a‧‧‧Resin spit out (raw material spit)

73b‧‧‧樹脂吐出針安裝部 73b‧‧‧Resin spit needle installation

74a‧‧‧樹脂吐出針把持部 74a‧‧‧Resin spit out the needle grip

74b‧‧‧調整部 74b‧‧‧Adjustment Department

75‧‧‧樹脂流路 75‧‧‧Resin flow path

77‧‧‧加熱筒蓋部 77‧‧‧heating cylinder cover

78‧‧‧樹脂吐出手段保持環部 78‧‧‧Resin discharge means to keep the ring

B‧‧‧線 B‧‧‧ line

C‧‧‧線 C‧‧‧ line

D‧‧‧線 D‧‧‧ line

Claims (10)

一種納米纖維製造裝置,其具備相對於從高壓氣體噴出手段噴出之高壓氣流吐出液狀性原料之液狀性原料吐出手段,其中,該液狀性原料吐出手段以從前述高壓氣體噴出手段噴出之高壓氣流為中心配置有複數個。 A nanofiber manufacturing apparatus comprising: a liquid material discharging device that discharges a liquid material from a high-pressure gas stream discharged from a high-pressure gas discharging means, wherein the liquid material discharging means ejects from the high-pressure gas discharging means The high-pressure airflow is provided with a plurality of centers. 如申請專利範圍第1項所述之納米纖維製造裝置,其中,前述液狀性原料吐出手段具備將原料熔融並擠出之擠出手段。 The nanofiber manufacturing apparatus according to the first aspect of the invention, wherein the liquid material discharging means includes an extrusion means for melting and extruding the raw material. 如申請專利範圍第1項所述之納米纖維製造裝置,其中,前述液狀性原料吐出手段具備供給熔解原料之手段。 The nanofiber manufacturing apparatus according to the first aspect of the invention, wherein the liquid material discharging means includes means for supplying a melting material. 如申請專利範圍第1至3項中任一項所述之納米纖維製造裝置,其中,在前述高壓氣體噴出手段上設置有用於供給高壓且高溫的氣體之氣體供給手段,從前述高壓氣體噴出手段以高壓噴出高溫的氣體。 The apparatus for producing a nanofiber according to any one of the first to third aspect, wherein the high-pressure gas discharge means is provided with a gas supply means for supplying a high-pressure and high-temperature gas, and the high-pressure gas discharge means A high temperature gas is ejected at a high pressure. 如申請專利範圍第1至4項中任一項所述之納米纖維製造裝置,其中,具備能夠調整相對於從前述高壓氣體噴出手段噴出之高壓氣流之前述液狀性原料吐出手段的設置角度之角度調整手段。 The apparatus for producing a nanofiber according to any one of the first to fourth aspects of the present invention, wherein the apparatus for adjusting the liquid material discharge means for adjusting the high-pressure gas stream ejected from the high-pressure gas discharge means is provided. Angle adjustment means. 如申請專利範圍第1至5項中任一項所述之納米纖維製造裝置,其中,前述液狀性原料吐出手段中,至少兩個以上相對於前述高壓氣體噴出手段對稱配置。 The nanofiber manufacturing apparatus according to any one of the first to fifth aspects of the present invention, wherein at least two or more of the liquid material discharging means are disposed symmetrically with respect to the high pressure gas discharging means. 如申請專利範圍第1至6項中任一項所述之納米纖維製造裝置,其中,前述液狀性原料吐出手段在從前述高壓氣體噴出手段噴出之高壓氣流的周圍以等間隔配置。 The apparatus for producing a nanofiber according to any one of the first aspect of the present invention, wherein the liquid material discharging means is disposed at equal intervals around a high-pressure air stream ejected from the high-pressure gas ejecting means. 如申請專利範圍第1至7項中任一項所述之納米纖維製造裝置,其中,從前述高壓氣體噴出手段噴出之高壓氣流在相對於納米纖維製造裝置的設置面垂直的方向上設置。 The apparatus for producing a nanofiber according to any one of the first to seventh aspect, wherein the high-pressure gas stream ejected from the high-pressure gas ejecting means is disposed in a direction perpendicular to a surface on which the nanofiber manufacturing apparatus is disposed. 一種納米纖維製造方法,其相對於從高壓氣體噴出手段噴出之高壓氣流從液狀性原料吐出手段吐出液狀性原料來製造納米纖維,其中,從以從前述高壓氣體噴出手段噴出之高壓氣流為中心而配置有複數個之前述液狀性原料吐出手段吐出液狀性原料時,調整從前述液狀性原料吐出手段相對於前述高壓氣流之液狀性原料的吐出角度。 A method for producing a nanofiber, which is produced by discharging a liquid raw material from a liquid raw material discharge means with respect to a high-pressure gas stream discharged from a high-pressure gas discharge means, wherein a high-pressure gas stream discharged from the high-pressure gas discharge means is used When a plurality of the liquid material discharging means are disposed at the center to discharge the liquid material, the discharge angle of the liquid material discharging means from the liquid material of the high-pressure air stream is adjusted. 一種納米纖維製造方法,其利用具備被供給原料之加熱筒、對該加熱筒進行加熱之加熱手段、及在前述加熱筒內擠出原料之擠出裝置之納米纖維製造裝置,其中,在前述加熱筒的端部設置有噴射高壓氣體之氣體噴出口,在該氣體噴出口的周圍設置有吐出在前述加熱筒內成為熔融狀態之原料之複數個原料吐出手段,藉由前述加熱手段對前述加熱筒進行加熱來使供給至前述加熱筒的內部之原料熔融或維持原料的熔融狀態,藉由前述擠出裝置來使原料從前述原料吐出手段吐出,藉由從前述氣體噴出口噴射之氣體生成氣流,藉由將前述吐出原料從外周搭載於噴出氣體的氣流來使其伸長並形成為納米級直徑的纖維。 A method for producing a nanofiber, comprising: a heating tube provided with a raw material, a heating means for heating the heating cylinder, and a nanofiber manufacturing apparatus for extruding a raw material in the heating cylinder, wherein the heating is performed A gas discharge port for injecting a high-pressure gas is provided at an end of the cylinder, and a plurality of raw material discharge means for discharging a raw material which is in a molten state in the heating cylinder are provided around the gas discharge port, and the heating means is used for the heating cylinder Heating is performed to melt the raw material supplied to the inside of the heating cylinder or to maintain the molten state of the raw material, and the raw material is discharged from the raw material discharging means by the extrusion device, and the gas is generated by the gas injected from the gas discharge port. The discharge raw material is stretched from the outer circumference by a gas flow of the discharge gas to form a fiber having a nanometer diameter.
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