TW202132642A - Apparatus and method for producing nanofiber - Google Patents

Apparatus and method for producing nanofiber Download PDF

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TW202132642A
TW202132642A TW109138309A TW109138309A TW202132642A TW 202132642 A TW202132642 A TW 202132642A TW 109138309 A TW109138309 A TW 109138309A TW 109138309 A TW109138309 A TW 109138309A TW 202132642 A TW202132642 A TW 202132642A
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raw material
pressure gas
resin
ejection
liquid raw
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TW109138309A
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TWI789643B (en
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池谷守彥
曾田浩義
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日商艾姆特克斯股份有限公司
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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

奈米纖維製造裝置及奈米纖維製造方法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奈米纖維的奈米纖維製造裝置及奈米纖維製造方法。The present invention relates to a nanofiber manufacturing device and a nanofiber manufacturing method that can provide high-quality nanofibers with a simple structure.

近年來,隨著奈米級直徑的纖維、所謂奈米纖維的用途的擴大,需求急速提高。奈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奈米纖維。並且,關於奈米纖維的製造,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, the demand for fibers with nanometer diameters, so-called nanofibers, has increased rapidly. As the use of nanofibers expands, special nanofibers of higher quality and corresponding to the application are required. In addition, various known methods such as electrospinning and meltblowing are known for the production of nanofibers, and each method has advantages and disadvantages.

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 the above-mentioned background art, Patent Document 1 discloses a method for producing a nonwoven fabric composed of a plurality of types of fibers in which a solution is mixed with melt-blown fibers and the fibers are discharged. Specifically, the solution ejection fiber is mixed into the fiber stream of the melt blown fiber ejected from the nozzle by the melt blow method, wherein the solution ejection fiber uses the spinning solution ejected from the liquid ejection section by the gas ejection The solution spinning means that sprays out the gas to spray out the spinning solution and fiberize it.

並且,在非專利文獻1中公開有關於基於電紡絲法之奈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奈米纖維的製造,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奈米纖維製造方法的缺陷亦進行詳述。In addition, Non-Patent Document 1 discloses a method for producing nanofibers based on the electrospinning method. In this non-patent document 1, it is disclosed that compared with the conventional electrospinning method of resin-based swelling that requires a solvent, the production of nanofibers is performed by swelling based on heat without using a solvent to prevent ignition when a solvent is used. The composition of the explosion, etc. In addition, the defects of the nanofiber manufacturing method based on the melt blown 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 Fabric 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奈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奈米纖維。相對於此,電紡絲法中雖然生產性提高,但裝置變得複雑化,且需要應對引火・爆炸之對策,因此導致製造成本提高。As also described in Non-Patent Document 1, in the conventional melt-blown nanofiber manufacturing method, in order to reduce the fiber diameter, a method of blowing high-temperature air at a high speed and discharging the polymer can be considered. The method of suppression is low. However, when high-temperature air is ejected at a high speed, the fiber diameter becomes thin but the fiber length becomes fragmented. On the other hand, when the discharge of the polymer is suppressed to a low level, it results in a per unit time. The production volume is significantly reduced, and it is difficult to mass-produce high-quality nanofibers under any circumstances. In contrast to this, although the productivity of the electrospinning method is improved, the device has become complex, and countermeasures against ignition and explosion are required, which leads to an increase in manufacturing costs.

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奈米纖維製造方法中能夠大量供給品質良好的奈米纖維,且進一步可排除引火或爆炸的主要原因來提高安全性之奈米纖維製造方法及奈米纖維製造裝置。 [解決問題之技術手段]The present invention was made in view of the above-mentioned problems, and its purpose is to provide a method that can supply a large amount of high-quality nanofibers in a melt-blown nanofiber manufacturing method, and further eliminates the main cause of ignition or explosion to improve safety. The nanofiber manufacturing method and nanofiber manufacturing device. [Technical means to solve the problem]

本發明的奈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奈米纖維製造裝置,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 equipped with liquid raw material ejection means for ejecting liquid raw material from a high-pressure gas flow ejected from a high-pressure gas ejection means, wherein the liquid raw material ejection means is A plurality of high-pressure gas streams ejected from the aforementioned high-pressure gas ejection means are arranged at the center.

並且,本發明的奈米纖維製造裝置中,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。In addition, in the nanofiber manufacturing apparatus of the present invention, the liquid raw material ejection means includes an extrusion means for melting and extruding the raw material.

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

並且,本發明的奈米纖維製造裝置中,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。In addition, in the nanofiber manufacturing apparatus of the present invention, the high-pressure gas ejection means is provided with gas supply means for supplying high-pressure and high-temperature gas, and the high-temperature gas is ejected at high pressure from the high-pressure gas ejection means.

並且,本發明的奈米纖維製造裝置中,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。In addition, the nanofiber manufacturing apparatus of the present invention includes angle adjustment means capable of adjusting the installation angle of the liquid raw material ejection means with respect to the high-pressure gas flow ejected from the high-pressure gas ejection means.

並且,本發明的奈米纖維製造裝置中,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。In addition, in the nanofiber manufacturing apparatus of the present invention, at least two or more of the liquid raw material ejection means are arranged symmetrically with respect to the high-pressure gas ejection means.

並且,本發明的奈米纖維製造裝置中,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。In addition, in the nanofiber manufacturing apparatus of the present invention, the liquid raw material ejection means is arranged at equal intervals around the high-pressure gas flow ejected from the high-pressure gas ejection means.

並且,本發明的奈米纖維製造裝置中,從前述高壓氣體噴出手段噴出之高壓氣流設置於相對於奈米纖維製造裝置的設置面垂直的方向。In addition, in the nanofiber manufacturing apparatus of the present invention, the high-pressure gas flow ejected from the high-pressure gas ejection means is installed in a direction perpendicular to the installation surface of the nanofiber manufacturing apparatus.

本發明的奈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奈米纖維之奈米纖維製造方法,該奈米纖維製造方法中,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 nanofibers of the present invention is a method for producing nanofibers by ejecting a liquid raw material from a liquid raw material ejecting means to produce nanofibers with respect to a high-pressure gas flow ejected from a high-pressure gas ejecting means. In the method, when the liquid raw material is discharged from a plurality of the liquid raw material discharge means arranged around the high pressure gas flow discharged from the high pressure gas discharge means, the liquid raw material discharge means is adjusted relative to the high pressure The discharge angle of the liquid material in the air stream.

而且,本發明的奈米纖維製造方法係利用奈米纖維製造裝置之奈米纖維製造方法,前述奈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奈米級直徑的纖維。Furthermore, the nanofiber manufacturing method of the present invention is a nanofiber manufacturing method using a nanofiber manufacturing device. The nanofiber manufacturing device is provided with a heating cylinder to which raw materials are supplied, heating means for heating the heating cylinder, and In the extrusion device for extruding the raw material in the heating cylinder, in the method, a gas ejection port for injecting high-pressure gas is provided at the end of the heating cylinder, and the gas ejection port is provided around the gas ejection port to be melted in the heating cylinder A plurality of raw material discharging means of the raw material in the state, the heating cylinder is heated by the heating means to melt the raw material supplied to the inside of the heating cylinder or maintain the molten state of the raw material, and the raw material is removed from the heating cylinder by the extrusion device The raw material ejection means ejects, generates a gas flow by the gas ejected from the gas ejection port, and stretches the ejected raw material into a nanometer diameter fiber by mounting the ejected raw material on the flow of the ejected gas from the outer periphery.

依本發明,能夠安全地製造直徑更小且品質更高的奈米纖維。並且,在製造奈米纖維時,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, nanofibers with smaller diameter and higher quality can be safely manufactured. In addition, when manufacturing nanofibers, it is possible to compensate for the production volume per unit time which is a defect based on the melt-blown method by installing a plurality of resin ejection means without using a high-voltage device.

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 mode for carrying out the present invention will be described below. Of course, it goes without saying that the present invention can be easily applied to a structure other than the structure described in this embodiment within the scope of not violating the spirit 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奈米纖維者,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”係指成形奈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奈米纖維之實施例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奈米纖維之實施例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 raw material is supplied to form nanofibers with respect to a fluid (a gaseous fluid is preferred) ejected at a high pressure. However, in the specification of the present application, when the composition is referred to as "gas" without specifying the composition, It includes gases composed of all components or molecular structures. In addition, in the specification of this application, "raw material" refers to all materials used when forming nanofibers. In the following examples, examples of using synthetic resin as "raw material" are described, but it is not limited to this. , Various constituent materials can be used. In addition, in the specification of this application, the term "liquid raw material" is not limited to those in which the properties of the raw materials are liquid, and is included in Example 1 where a solid raw material is melted and extruded by an extrusion device to form nanofibers. The "melted raw material" used in the chemistry is included in pre-melting a predetermined solvent to make a solid raw material or a liquid raw material to a predetermined concentration, and send it to the outlet or squeeze it by an appropriate means. Come out to form the "melted raw material" used in Example 2 of nanofibers. That is, the "liquid raw material" in the present invention refers to those that need to have a viscosity to the extent that the "raw material" can be supplied (discharged, discharged) from the supply port (discharge port, discharge port). In the present invention, , The "raw material" with such liquid properties is called "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而進行說明之奈米纖維製造裝置及奈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 will be described later, but the concept of the basic invention common to the nanofiber manufacturing apparatus and the nanofiber manufacturing method explained as the first and second embodiments of the present invention is shown in Figure 11, with the center In the high-pressure gas ejection means 71, around the high-pressure gas flow 90 ejected from the high-pressure gas ejection means 71, the installation angles of the plurality of ejection means 73a for ejecting liquid raw materials can be changed. That is, it is one that can change the supply angle θ of the liquid raw material relative to the high-pressure gas flow 90. The basic concept of the present invention is shown in Fig. 11. The discharge means 73a for discharging the liquid raw material is arranged at a supply angle θ with respect to the center line 91 of the high-pressure airflow 90, and the supplied discharged liquid raw material is discharged from the plurality of discharge means 73a. It is arranged toward the center line 91 of the high-pressure airflow 90. The liquid raw material discharged from the plurality of discharge means 73a is preferably arranged so as to cross on 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。 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°。In Figure 11, the arrangement state of each constituent element is as above, and the positional relationship is as follows. If these are expressed based on the position of the gas ejection port 71 (open nozzle) of the high-pressure gas, and the positional relationship is retreated further downstream than it, then a is the raw material ejection port from the ejection port of the ejection means 73a The retreat distance, b is the retreat distance from the discharge port of the discharge means 73a where the discharge material crosses, c is the opening diameter of the discharge port of the discharge means 73a, and d is the gas discharge port gap. Here, the configuration is as follows: with respect to the center line 91 of the high-pressure airflow 90, the discharge means 73a for discharging the liquid raw material is arranged at a supply angle θ, and the raw material supply tangent angle represented by tanθ=d/(ba)(1) θ can be adjusted within the range of 0°<θ<90°. As an example, when the material ejection port retreat distance a=30mm, the ejection port opening diameter c=2mm, the gas ejection port gap d=7mm, and the ejection pressure of the high-pressure gas is about 0.15MPa, it is desirable that θ=20°±10°.

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 retreat distance a of the raw material discharge port, the retreat distance b of the discharge material crossing position, and the gas discharge port gap d. Moreover, it should be determined by the high pressure gas discharge port opening diameter c and the discharge high pressure Determined by the relationship between gas pressure and temperature.

在本發明的實施例1的奈米纖維製造裝置及奈米纖維製造方法中,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,並形成奈米級直徑的纖維。In the nanofiber manufacturing apparatus and the nanofiber manufacturing method of Example 1 of the present invention, the pelletized raw material (resin) put in the hopper is fed into a heating cylinder heated by a heater to be melted, It is sent out to the front of the heating cylinder by a screw that rotates by a motor. The heating cylinder is provided with a head, and high-pressure gas is ejected from a gas ejection port formed in the center of the head. The liquid molten raw material (melted resin) that reaches the tip of the heating cylinder passes through the inside of the head and is supplied from a plurality of ultra-thin tubes arranged on the downstream side of the gas ejection means ( The means of spitting out) is supplied (spitting out). The liquid molten raw material ejection means of a plurality of ultra-thin tubes are uniformly arranged around the gas ejection port arranged in the center. Thereby, the molten resin discharged from the liquid molten raw material discharging means is stretched to form fibers with nanometer diameter.

在本發明的實施例2的奈米纖維製造裝置及奈米纖維製造方法中,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 in the center. In contrast, the liquid melted raw material is ejected from the The means for discharging the liquid molten raw material with a plurality of ultra-thin tubes on the downstream side of the means discharges high-pressure gas.

(實施例1) 以下,對於本發明的實施例1中之奈米纖維製造裝置的整體構成,依據第1圖~第3圖進行說明。(Example 1) Hereinafter, the overall configuration of the nanofiber manufacturing apparatus in Example 1 of the present invention will be described based on Figs. 1 to 3.

作為本發明的實施例1,第1圖所示之奈米纖維製造裝置1由以下構成:料斗2,用於將作為奈米纖維的素材之樹脂(微細粒徑的粒體狀合成樹脂)投入到奈米纖維製造裝置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。As the first embodiment of the present invention, the nanofiber manufacturing apparatus 1 shown in Fig. 1 is composed of the following: a hopper 2 for charging the resin (fine particle size granular synthetic resin) as the material of the nanofiber Into the nanofiber manufacturing device 1; the heating cylinder 3 is used to receive the supply of resin from the hopper 2 and heat and melt it; the heater 4 is used as a heating means for heating the heating cylinder from the outside; the screw 5 is rotatable It is housed in the heating cylinder 3 and is used as an extrusion device for moving the molten resin to the tip of the heating cylinder 3 by rotation; the motor 6 is used to rotate the screw 5 through the connection part 61 (details not shown) The driving means; and the cylindrical head 7 is provided at the front end of the heating cylinder 3, and is equipped with a resin ejection means for ejecting the molten resin described later from the surroundings, and also has a gaseous hot air jet from the center The gas ejection port 71 (open nozzle). In order to inject the jet gas from the center portion of the cylindrical head 7, a high-pressure gas is supplied through a pipe 81 connected to a gas piping portion 8 as a gas supply pipe. The gas piping portion 8 is provided with heating means (not shown) such as a heater, and is configured to blow hot air from the gas ejection port 71 (open nozzle). In addition, the head 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 structure in which molten resin does not leak out of the device.

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 arranged on the outer periphery of the heating cylinder 3 are configured by a control means not shown so as to be able to individually or collectively perform temperature control. In this embodiment, as shown in Fig. 1, four heaters 4 are provided, but it is not limited to this. The diameter or length of the heating cylinder 3 can be determined according to the material or nature of the resin used. Wait for many conditions to change the number of settings, or change the size of each heater, or change the configuration conditions appropriately.

第2圖係本實施例的奈米纖維製造裝置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 diagrams showing the structure 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 7 as an embodiment of the present invention, a pipe 81 for supplying high-pressure gas is connected from the outer periphery of the heating cylinder 3 via a gas piping portion 8. The high-pressure gas from the pipe 81 is introduced into the inside of the head 7 and is ejected from the gas ejection port 71 (open nozzle: Fig. 3) formed in the center. Around the gas ejection port 71, a plurality of resin ejection means 73 are arranged at equal intervals. In the present embodiment, the resin ejection means 73 is constituted by a resin ejection needle attachment portion 73b provided with a resin ejection needle 73a and a structure for attaching the resin ejection needle 73a to the head 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 7 shown in FIG. 3 includes a heating cylinder cover 77 covering the front end of the heating cylinder 3, and a resin ejection means holding ring 78 as a means for holding the resin ejection means 73. The resin ejection means holding ring portion 78 is fixed to the heating cylinder cover portion 77 by fixing means (unsigned) such as bolts.

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奈米纖維的生產量。When multiple resin ejection means 73 are arranged around the gas ejection port 71 (open nozzle) by the retaining ring 78 of the resin ejection means, the plurality of resin ejection means 73 are arranged at equal intervals and equal distances (from the gas ejection port). The distance a), or equal angle (discharge angle θ) is set, which can greatly increase the production of nanofibers with uniform diameter and fiber length.

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 ejection port 71 (open nozzle) and the resin ejection means 73 arranged around will be described with reference to FIG. 11. It is ejected by the air flow 90 ejected from the gas ejection port 71 arranged at the center of the head 7. The air flow 90 is provided with a plurality of resin ejection means 73 arranged around it, and is ejected from the resin ejection needle 73a as the resin ejection port toward the air flow 90 ejected from the ejection port 71 at the ejection angle θ. The resin ejection port of the resin ejection needle 73a is arranged in front of the distance a from the ejection port 71 (the downstream side when following the airflow 90 from the ejection port 71). The resin ejection ports of the plurality of resin ejection needles 73a are ejected so that the ejected resin crosses the distance b from the ejection port 71 (the downstream side when following the airflow 90 from the ejection port 71).

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奈米纖維。因此根據所製造之奈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 ejection port), arrangement angle (θ) of the resin ejection means 73 as the arrangement conditions of the plural resin ejection means 73, it is also possible to form a non-uniform diameter Or nanofiber of fiber length. Therefore, the placement conditions such as the placement interval of the resin ejection means 73 may be appropriately selected and changed according to the use of the nanofibers to be produced.

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。Figure 4 is a cross-sectional view taken along the line AA of the head 7 in Figure 3, and Figure 5 (a), Figure 5 (b), and Figure 5 (c) show the main parts of the head 7 in Figure 4 (BB section, CC section, DD section) each section view. In addition, FIG. 6 is an explanatory diagram showing the flow path A of the high-pressure gas and the flow path B of the molten resin. As shown in FIGS. 4 to 6, six resin flow paths 75 (arrow B in the figure) corresponding to the resin ejection means 73 are formed at equal intervals in the interior of the head 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 cross-sectional view of Fig. 5(c), and flows into the resin flow path 75 shown in the CC cross-sectional view, as shown in the BB cross-sectional view The resin is ejected from the inside of the resin ejection needle attachment portion 73b and ejected from the resin ejection 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 7 so as not to interfere with the resin flow path 75 (arrow B in the figure), as shown in Fig. 5 As shown in the CC cross-sectional view of (b), it passes between any adjacent resin flow paths 75, and is formed by changing the direction from the outside of the head 7 to the inside. The gas piping portion 8 is connected to the gas flow path 72 via the pipe 81. Through the gas flow path 72 formed in this way, the high-pressure and high-temperature gas supplied by the gas injection portion 8 is injected from the gas injection port 71 (open nozzle). In this way, the resin flow path 75 and the gas flow path 72 are formed without interfering with each other in the head 7. In addition, the reference numeral 79 in FIG. 7( b) is the threaded portion 79 when the pipe (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, a holding adjustment means 74 of the resin discharge means 73 is provided. However, the diameter of the resin ejection port of the resin ejection needle 73a of the resin ejection means 73 is very small, and it is very susceptible to stresses such as device vibration and resin pressure. The arrangement conditions of the resin ejection means 73 described above may also be changed. Or detachment from the head 7 occurs. Therefore, even if the angle of the resin ejection port 74 is adjusted and changed, it is necessary to set the resin ejection needle 73a so that the resin ejection needle 73a does not detach from the head 7 so as not to apply stress to the resin ejection 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。Figure 7 (a) is an explanatory view showing the support structure based on the resin ejection port support portion 74. The resin ejection port support portion 74 is used to fix and adjust the resin ejection means 73 with respect to the resin ejection means holding ring 78 installation angle. The resin ejection means 73 is composed of a resin ejection needle 73a and a resin ejection needle attachment portion 73b. The resin ejection needle attachment portion 73b is fixed to the head 7 by appropriate fixing means based on screws, engagements, pins, etc., not shown. The resin ejection means holds the ring portion 78. A resin ejection port support portion 74 is provided on the resin ejection needle 73a. The resin ejection port support portion 74 is provided with a resin ejection needle grip portion 74a such that the resin ejection needle 73a is gripped from the surroundings, and as shown in FIG. The adjustment means 74b constitutes. By operating the adjustment means 74b to advance and retreat the adjustment rod 74c and move the resin ejection needle grip 74a in the diameter direction of the head 7, the resin ejection needle 73a can be fixed at a desired position and angle. With this kind of resin ejection port support portion 74, the resin ejection means 73 can be adjusted to eject the molten resin at a desired ejection angle with respect to the ejection airflow from the gas ejection port 71, and can be reliably adjusted 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,其前端在奈米纖維製造裝置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 structure, it is useful as a means for adjusting the ejection angle of the molten resin with respect to the ejected airflow, and the resin ejection needle 73a is a very thin tube, and its tip may be caused by the motor 6 or the motor 6 when the nanofiber manufacturing apparatus 1 is operating. The driving of the screw 5 causes a large amount of vibration, but the resin ejection port support portion 74 can also effectively suppress the vibration. In addition, in Figure 2 of this embodiment, the resin ejection means 73 is set to six, and the resin ejection port support portion 74 is provided with six correspondingly. However, it is not limited to this, and it can be determined according to the resin used. , Production volume, product characteristics and other conditions to select the quantity appropriately.

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 this embodiment, the resin ejection port support portion 74 is also provided with a resin ejection needle grip portion 74d so as to hold the resin ejection needle 73a from the surroundings, and an adjustment rod 74e that can advance and retreat provided from the outside of the head 7 toward the inside. The adjustment means (not shown) constitute. At this time, the adjustment means is operated to advance and retreat the adjustment rod 74e to move the resin ejection needle grip 74d in the diameter direction of the head 7, thereby fixing the resin ejection needle 73a at a desired position and angle. At this time, the resin ejection needle attachment portion 73c is made into a spherical or cylindrical shape, and the resin ejection needle attachment portion 73c is formed as a rotatable and rotatable sliding surface 76 on the resin ejection means retaining ring portion 78 of the head 7. By attaching the resin ejection needle attachment portion 73c, the angle of the resin ejection needle 73a can be easily adjusted. Thereby, it is possible to adjust the angle of the resin ejection means 73 without worrying about falling off of the resin ejection 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奈米級直徑的纖維狀。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奈米纖維。In addition, as shown in the figure, the gas ejection port 71 and the resin ejection means 73 are configured such that the gas ejection port 71 is retracted to a position on the downstream side of the resin ejection means 73 and arranged. With this configuration, the molten resin is gradually stretched along the distribution of the jet flow of the gas jetted from the gas jet port 71 and becomes a fiber shape with a nanometer diameter. In addition, the gas as hot air is injected from the gas injection section 8 by a heating means not shown, so that the resin discharged from the resin discharge means 73 can be made longer and with a smaller fiber diameter than when the room temperature gas is injected. Nano fiber.

關於如上所述的構成的奈米纖維製造裝置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奈米纖維。A series of operations of the nanofiber manufacturing apparatus 1 configured as described above will be described. The raw material (resin) put into the hopper 2 is heated by the heater 4 in the heating cylinder 3 to be melted, and is sent out to the front of the heating cylinder 3 by a screw rotated by the motor 6. The molten resin reaching the tip of the heating cylinder 3 is ejected from the raw material ejection ports of the six resin ejection needles through the six resin flow paths 75 formed in the inside of the head 7. The ejected molten resin is transported by the air flow generated by the high-pressure and high-temperature gas supplied from the gas ejection portion 8 and ejected from the gas ejection port 71. At this time, the molten resin is stretched to form nanofibers due to the speed difference between the faster high-temperature gas flow and the slower air remaining around it.

(實施例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奈米纖維製造裝置進行了詳述,但如先前所述,作為奈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奈米纖維之奈米纖維製造裝置。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。(Example 2) As Example 1 of the present invention, the nanofiber manufacturing device that melts the granular synthetic resin of fine particle size and is used as a raw material is described in detail. It is not limited to this, and it is also possible to use a solid raw material or a liquid raw material melt|dissolved in advance with respect to a predetermined solvent, so that it may become a molten raw material of a predetermined concentration. It is also a liquid raw material. Figures 8 to 10 show a nanofiber manufacturing device for forming nanofibers from molten raw materials. In addition, the same reference numerals are assigned to the same configurations as those of the first embodiment, and detailed descriptions thereof 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 Example 2 of the present invention, a solvent reservoir 5A having a function of applying a predetermined pressure to the molten raw material to perform extrusion is used instead of the hopper 2, screw 5, and motor 6 of Example 1. The prescribed pressure may be the pressure based on the gravity generated by the height difference. The head 7A is connected to the solvent supply pipe 3A and the gas injection unit 8. Although illustration is omitted, a means for ejecting gas may be appropriately provided in the gas injection section 8 or introduced into the gas injection section 8 from a high-pressure gas supply section (not shown). As shown in FIG. 9, the head 7A is provided with a gas flow path 72A serving as a flow path of the gas supplied from the gas injection unit 8 and a gas injection port 71A. In addition, the head 7A is also provided with a resin flow path 75A as a flow path of the melting material, and the resin flow path 75A is connected to the resin discharge means 73. The resin ejection means 73 is composed of a resin ejection needle 73a as the ejection port of the molten raw material, and a resin ejection needle attachment portion not shown in Figs. 8 to 10, as in Example 1. In addition, the head 7A is provided with a resin ejection means holding plate portion 78A, and here is provided an adjustment means provided with a resin ejection needle holding portion 74a and an adjustment rod 74c that can advance and retreat installed from the outside to the inside of the head 7A. The resin ejection port support portion 74 constituted by 74b can thereby freely adjust the ejection angle of the resin ejection needle 73a by the resin ejection port support portion 74 as in the first embodiment.

實施例2中之奈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 Example 2 is provided with two resin ejection means 73. Of course, 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 provide the resin discharge means 73 uniformly. In addition, the embodiment shown in the figure shows a horizontal ejection type, but as long as those skilled in the art can easily imagine that the gas flow path 72A from the gas ejection port 71A is vertical (from the top to the bottom, or from the top to the bottom). A modified example of spraying from the bottom to the top).

藉由如此構成,與實施例1的構成相比,使用在溶剤中溶化有原料之熔解原料,藉此能夠不使用加熱筒或馬達、螺桿等複雑的裝置而構成奈米纖維製造裝置,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奈米纖維製造裝置。當為該種輕便型的奈米纖維製造裝置時,能夠藉由朝向欲使奈米纖維附著之位置噴吹奈米纖維來形成奈米纖維,且奈米纖維的用途擴大。With such a configuration, compared with the configuration of Example 1, the molten raw material in which the raw material is melted in the solvent is used, thereby making it possible to construct a nanofiber manufacturing device without using heating cylinders, motors, screws, etc. The size becomes compact and space saving can be achieved. In addition, the device can be constructed compactly, thereby making it possible to construct a lightweight nanofiber manufacturing device. In the case of this kind of portable nanofiber manufacturing device, nanofibers can be formed by spraying nanofibers toward the position where the nanofibers are to be attached, and the applications of nanofibers are 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奈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奈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,但需要所製造之奈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 foregoing embodiments, and various modifications can be implemented within the scope of the gist of the present invention. For example, in the above-mentioned embodiment, it is shown as a horizontal type nanofiber manufacturing device with the molten resin and gas ejection port facing the horizontal direction, but it is not limited to this, and it is used as a horizontal type nanofiber manufacturing device facing downward. There is no problem with the fiber manufacturing device and manufacturing method. This situation can effectively avoid the influence of gravity. In addition, the extrusion device is described as the screw 5, but the manufactured nanofibers are required to be cut off, but there is no problem even if the solution is sequentially supplied like die casting and the extrusion is interrupted by a piston or the like. Furthermore, the gas ejection port 71 can be formed into a tapered shape and a nozzle shape, and the pressure can be increased. Furthermore, the structure for adjusting the angle of the resin ejection needle 73a will be described with two specific examples, but for example, any structure may be adopted as long as the structure can adjust the angle of the bellows type resin ejection means.

1:奈米纖維製造裝置 2:料斗 3:加熱筒 4:加熱器(加熱手段) 5:螺桿(擠出裝置) 6:馬達(驅動手段) 7:頭部 71:氣體噴出口 72:氣體流路 73:樹脂吐出手段 73a:樹脂吐出針(原料吐出口) 73b、73c:樹脂吐出針安裝部 74:樹脂吐出口支撐部 74a:樹脂吐出針把持部 74b:調整部 74c:調整桿 75:樹脂流路 76:氣體流路 77:加熱筒蓋部 78:樹脂吐出手段保持環部 8:氣體噴射部(氣體噴射手段) 81:管道(氣體流路) 90:高壓氣流 91:高壓氣流的中心線1: Nano fiber manufacturing equipment 2: Hopper 3: heating cylinder 4: Heater (heating means) 5: Screw (extrusion device) 6: Motor (driving means) 7: head 71: Gas outlet 72: Gas flow path 73: Resin spit out means 73a: Resin ejection needle (raw material ejection port) 73b, 73c: Resin ejection needle mounting part 74: Resin discharge port support part 74a: Resin ejection needle grip 74b: Adjustment Department 74c: adjustment lever 75: Resin flow path 76: Gas flow path 77: Heating cylinder cover 78: Resin discharge means holding ring 8: Gas injection part (gas injection means) 81: Pipe (gas flow path) 90: high-pressure airflow 91: Centerline of high-pressure airflow

第1圖係剖視表示本發明的奈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。 第2圖係作為本發明的實施例1之奈米纖維製造裝置中之頭部及加熱筒的外觀俯視圖。 第3圖係表示作為本發明的實施例之奈米纖維製造裝置中之頭部前端之外觀主視圖。 第4圖係第3圖所示之奈米纖維製造裝置的A-A線處之剖面圖。 第5圖係第4圖所示之奈米纖維製造裝置的B-B線、C-C線、D-D線各處之剖面圖。 第6圖係表示作為本發明的實施例1之奈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。 第7圖係表示作為本發明的實施例1之奈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。 第8圖係表示本發明的奈米纖維製造裝置的實施例2的整體構成之側視圖。 第9圖係表示本發明的奈米纖維製造裝置的實施例2的整體構成之俯視圖。 第10圖係表示本發明的奈米纖維製造裝置的實施例2的頭部構成之主視圖。 第11圖係用於說明本發明的奈米纖維製造裝置及奈米纖維製造方法的基本發明概念之說明圖。Fig. 1 is a cross-sectional side view showing a part of the overall configuration of Embodiment 1 of the nanofiber manufacturing apparatus of the present invention. Figure 2 is a plan view of the external appearance of the head and heating cylinder in the nanofiber manufacturing apparatus as the first embodiment of the present invention. Fig. 3 is a front view showing the external appearance of the tip of the head in the nanofiber manufacturing apparatus as an embodiment of the present invention. Figure 4 is a cross-sectional view taken along the line A-A of the nanofiber manufacturing device shown in Figure 3. Figure 5 is a cross-sectional view of the B-B, C-C, and D-D lines of the nanofiber manufacturing device shown in Figure 4. Fig. 6 is an explanatory diagram showing the resin flow path and the gas flow path inside the head of the nanofiber manufacturing apparatus as the first embodiment of the present invention. Figure 7 shows an example of the support structure of Figure 7 (a) of the resin ejection means and another example of Figure 7 (b) of the support structure of the resin ejection means in the nanofiber manufacturing apparatus of Example 1 of the present invention The explanatory diagram. Fig. 8 is a side view showing the overall configuration of Embodiment 2 of the nanofiber manufacturing apparatus of the present invention. Fig. 9 is a plan view showing the overall configuration of Example 2 of the nanofiber manufacturing apparatus of the present invention. Fig. 10 is a front view showing the structure of the head of Example 2 of the nanofiber manufacturing apparatus of the present invention. Figure 11 is an explanatory diagram for explaining the basic inventive concept of the nanofiber manufacturing apparatus and 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: Thin section

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 ejection needle (raw material ejection outlet)

73b:樹脂吐出針安裝部 73b: Resin ejection needle mounting part

74a:樹脂吐出針把持部 74a: Resin ejection 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 holding ring

B:線 B: line

C:線 C: line

D:線 D: line

Claims (9)

一種奈米纖維製造裝置(1),其包含: 高壓氣體噴出手段(71),其用於噴出高壓氣流(90);以及 複數個液狀性原料吐出手段(73),其用於吐出液狀性原料至由該高壓氣體噴出手段(71)所噴出之該高壓氣流(90),其中 該等液狀性原料吐出手段(73)係以由該高壓氣體噴出手段(71)所噴出之該高壓氣流(90)為中心而配置, 其特徵在於, 角度調整手段(74),其能夠調整該等液狀性原料吐出手段(73)相對於由該高壓氣體噴出手段(71)所噴出之該高壓氣流(90)的設置角度(θ)。A nanofiber manufacturing device (1), which comprises: High-pressure gas ejection means (71) for ejecting high-pressure gas flow (90); and A plurality of liquid raw material ejection means (73) for ejecting liquid raw material to the high-pressure gas flow (90) ejected by the high-pressure gas ejection means (71), wherein The liquid raw material ejection means (73) is arranged centering on the high-pressure gas flow (90) ejected by the high-pressure gas ejection means (71), It is characterized by The angle adjusting means (74) can adjust the installation angle (θ) of the liquid raw material ejecting means (73) with respect to the high-pressure gas flow (90) ejected by the high-pressure gas ejecting means (71). 如請求項1所述之奈米纖維製造裝置(1),其中該等液狀性原料吐出手段(73)係配置有用於熔融並擠出原料的擠出裝置(5),且該等液狀性原料吐出手段(73)係吐出藉由該擠出裝置(5)而熔融並擠出的原料以作為液狀性原料。The nanofiber manufacturing device (1) according to claim 1, wherein the liquid raw material discharging means (73) is equipped with an extrusion device (5) for melting and extruding raw materials, and the liquid raw materials The sexual raw material discharge means (73) discharges the raw material melted and extruded by the extrusion device (5) as a liquid raw material. 如請求項1所述之奈米纖維製造裝置(1),其中該等液狀性原料吐出手段(73)係配置有用於供給經溶解之原料的儲存器(5A),且該液狀性原料吐出手段(73)將該經溶解之原料吐出而作為液狀性原料。The nanofiber manufacturing device (1) according to claim 1, wherein the liquid raw material discharge means (73) is equipped with a reservoir (5A) for supplying dissolved raw material, and the liquid raw material The discharge means (73) discharges the dissolved raw material as a liquid raw material. 如請求項1至3中任一項所述之奈米纖維製造裝置(1),其中該高壓氣體噴出手段(71)係配置有用於供給高壓且高溫之氣體的氣體供給手段,且該高壓氣體噴出手段(71)噴出該高壓且高溫之氣體而作為高壓氣流(90)。The nanofiber manufacturing device (1) according to any one of claims 1 to 3, wherein the high-pressure gas ejection means (71) is equipped with a gas supply means for supplying high-pressure and high-temperature gas, and the high-pressure gas The ejection means (71) ejects the high-pressure and high-temperature gas as a high-pressure gas flow (90). 如請求項1至4中任一項所述之奈米纖維製造裝置(1),其中至少兩個以上的該等液狀性原料吐出手段(73)係相對於該高壓氣體噴出手段(71)對稱地配置。The nanofiber manufacturing device (1) according to any one of claims 1 to 4, wherein at least two of the liquid raw material ejection means (73) are relative to the high-pressure gas ejection means (71) Configured symmetrically. 如請求項1至5中任一項所述之奈米纖維製造裝置(1),其中該等液狀性原料吐出手段(73)在由該高壓氣體噴出手段(71)所噴出之該高壓氣流(90)的周圍以等間隔配置。The nanofiber manufacturing device (1) according to any one of claims 1 to 5, wherein the liquid raw material ejection means (73) is used for the high-pressure gas flow ejected by the high-pressure gas ejection means (71) The surroundings of (90) are arranged at equal intervals. 如請求項1至6中任一項所述之奈米纖維製造裝置(1),其中由該高壓氣體噴出手段(71)所噴出之該高壓氣流(90)係設置於與該裝置(1)之設置面垂直的方向。The nanofiber manufacturing device (1) according to any one of claims 1 to 6, wherein the high-pressure gas flow (90) sprayed by the high-pressure gas spraying means (71) is installed in the device (1) The direction in which the setting surface is perpendicular. 一種使用如請求項1至7中任一項所述之奈米纖維製造裝置(1)製造奈米纖維的方法,其中 由高壓氣體噴出手段(71)噴出高壓氣流(90), 由液狀性原料吐出手段(73)吐出液狀性原料至由該高壓氣體噴出手段(71)所噴出之該高壓氣流(90),以及 當該等液狀性原料吐出手段(73)將液狀性原料吐出至作為中心的該高壓氣流(90)時,使用角度調整手段(74)調整該由該等液狀性原料吐出手段(73)所吐出之液狀性原料相對於該高壓氣流(90)的吐出角度(θ)。A method for manufacturing nanofibers using the nanofiber manufacturing device (1) according to any one of claims 1 to 7, wherein The high-pressure gas flow (90) is sprayed out by the high-pressure gas spraying means (71), The liquid raw material is discharged from the liquid raw material discharge means (73) to the high-pressure gas flow (90) discharged by the high-pressure gas discharge means (71), and When the liquid raw material ejection means (73) ejects the liquid raw material to the high-pressure air flow (90) as the center, the angle adjusting means (74) is used to adjust the liquid raw material ejection means (73). ) The discharge angle (θ) of the discharged liquid raw material with respect to the high-pressure airflow (90). 一種使用奈米纖維製造裝置(1)製造奈米纖維的方法,該奈米纖維製造裝置(1)包含被供給原料之加熱筒(3)、對該加熱筒(3)進行加熱之加熱手段(4)、及在該加熱筒(3)內擠出原料之擠出裝置(5),其中,在該方法中, 在該加熱筒(3)的端部設置有噴射高壓氣體的氣體噴出口(71), 在該氣體噴出口(71)的周圍設置用於吐出在該加熱筒(3)內為熔融狀態的原料的複數個原料吐出手段(73),以及 藉由該加熱手段(4)對該加熱筒(3)進行加熱,藉由使供給至該加熱筒(3)之內部的原料熔融或維持原料的熔融狀態,藉由從該擠出裝置(5)擠出原料並從該原料吐出手段(73)吐出,藉由從該氣體噴出口(71)噴射的氣體而生成氣流,及藉由將所吐出之原料從外周搭載於噴出氣體的氣流來使其伸長,以獲得奈米級直徑的纖維。A method of manufacturing nanofibers using a nanofiber manufacturing device (1), the nanofiber manufacturing device (1) includes a heating cylinder (3) to which raw materials are supplied, and a heating means for heating the heating cylinder (3) ( 4), and an extrusion device (5) for extruding raw materials in the heating cylinder (3), wherein, in the method, A gas jet port (71) for injecting high-pressure gas is provided at the end of the heating cylinder (3), A plurality of raw material ejection means (73) for ejecting the raw material in the molten state in the heating cylinder (3) is provided around the gas ejection port (71), and The heating cylinder (3) is heated by the heating means (4), the raw material supplied to the inside of the heating cylinder (3) is melted or the raw material is maintained in a molten state, and the extrusion device (5) ) The raw material is extruded and ejected from the raw material ejection means (73), the gas ejected from the gas ejection port (71) generates an air flow, and the ejected raw material is mounted on the outer periphery of the ejected gas flow to make It stretches to obtain fibers with nanometer diameter.
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EP3276051B1 (en) 2020-11-18
HUE052847T2 (en) 2021-05-28
AU2023233190A1 (en) 2023-10-12
JP2016183435A (en) 2016-10-20
EP3276051A1 (en) 2018-01-31
WO2016152999A1 (en) 2016-09-29
TWI789643B (en) 2023-01-11
CA3000318A1 (en) 2016-09-29

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