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TW201900963A - Non-woven cellulosic fabric comprising fibers having a non-circular cross section - Google Patents

Non-woven cellulosic fabric comprising fibers having a non-circular cross section Download PDF

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Publication number
TW201900963A
TW201900963A TW107110760A TW107110760A TW201900963A TW 201900963 A TW201900963 A TW 201900963A TW 107110760 A TW107110760 A TW 107110760A TW 107110760 A TW107110760 A TW 107110760A TW 201900963 A TW201900963 A TW 201900963A
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fibers
fabric
fiber
spinning solution
lyocell spinning
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TW107110760A
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Chinese (zh)
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TWI782967B (en
Inventor
湯姆 卡萊爾
馬可 茵茲曼
吉瑟拉 高荷姆
馬爾康 海赫斯
卡薩蓮娜 麥爾
亞柏罕 賽吉爾弗里克
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奧地利商蘭仁股份有限公司
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    • 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
    • D04H3/013Regenerated cellulose series
    • 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
    • D04H3/018Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the shape

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Nonwoven Fabrics (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
  • Chemical Or Physical Treatment Of Fibers (AREA)
  • Materials For Medical Uses (AREA)

Abstract

A nonwoven cellulose fiber fabric (102), in particular directly manufactured from lyocell spinning solution (104), wherein the fabric (102) comprises a network of substantially endless fibers (108), and wherein at least 1% of the fibers (108) has a non-circular cross sectional shape having a roundness of not more than 90%.

Description

包含具有非圓形截面之纖維的非織纖維素纖維織物Non-woven cellulosic fabric comprising fibers having a non-circular cross section

本發明是關於非織纖維素纖維織物、製造非織纖維素纖維織物的方法、用於製造非織纖維素纖維織物的裝置、產品或複合物、以及使用方法。This invention relates to nonwoven cellulosic fiber fabrics, methods of making nonwoven cellulosic fiber fabrics, devices, products or composites for making nonwoven cellulosic fiber fabrics, and methods of use.

萊賽爾技術(Lyocell technology)是關於纖維素木漿或其它纖維素系(cellulose-based)原料在極性溶劑(例如,N-甲基嗎啉-N-氧化物,其亦可稱為「氧化胺」或「AO」)中直接溶解以產生黏性的高剪切減黏溶液(highly shear-thinning solution),該溶液可轉換成一系列有用的纖維素系材料。商業上,使用該技術以生產一系列廣泛用於紡織工業之纖維素短纖維(可以商標名稱TENCEL®購自Lenzing AG, Lenzing, Austria)。來自萊賽爾技術的其他纖維素產品也已被使用。   纖維素短纖維長期以來一直被用作轉化成非織網的組分。然而,調整萊賽爾技術以直接生產非織網將獲得目前纖維素網產品所沒有的性質及性能。儘管由於重要的技術差異而不能直接將合成聚合物技術用於萊賽爾(lyocell),但這可視為是合成纖維工業中廣泛使用的熔噴及紡黏技術的纖維素版本。   已經進行許多研究以開發由萊賽爾溶液(尤其是WO 98/26122、WO 99/47733、WO 98/07911、US 6,197,230、WO 99/64649、WO 05/106085、EP 1 358 369、EP 2 013 390)直接形成纖維素網的技術。另外的技術是揭示於WO 07/124521 A1及WO 07/124522 A1。Lyocell technology is about cellulose wood pulp or other cellulose-based raw materials in polar solvents (for example, N-methylmorpholine-N-oxide, which can also be called "oxidation" A highly shear-thinning solution that dissolves directly in the amine or "AO" to produce a viscous solution that can be converted into a range of useful cellulosic materials. Commercially, this technology is used to produce a range of cellulosic staple fibers (available under the trade name TENCEL® from Lenzing AG, Lenzing, Austria). Other cellulose products from lyocell technology have also been used. Cellulose staple fibers have long been used as components for conversion to nonwoven webs. However, the adjustment of the lyocell technology to directly produce non-woven webs will result in properties and properties not currently available in cellulosic mesh products. Although synthetic polymer technology cannot be directly applied to lyocell due to important technical differences, it can be considered a cellulose version of the meltblown and spunbond technology widely used in the synthetic fiber industry. A number of studies have been carried out to develop solutions from lyocell (especially WO 98/26122, WO 99/47733, WO 98/07911, US 6,197,230, WO 99/64649, WO 05/106085, EP 1 358 369, EP 2 013 390) A technique for directly forming a cellulose network. Further techniques are disclosed in WO 07/124521 A1 and WO 07/124522 A1.

本發明的目的是提供具有可調整之機械穩定性的纖維素系織物。   為了實現以上明確的目的,提供如申請專利範圍獨立項的非織纖維素纖維織物、製造非織纖維素纖維織物的方法、用於製造非織纖維素纖維織物的裝置、產品或複合物、以及使用方法。   根據本發明的例示性實施例,提供一種(特別是溶噴的)非織纖維素纖維織物(其特別是直接(特別是在原位(in situ)製程中或在連續操作的生產線中之可執行的連續製程中)由萊賽爾紡絲溶液製造),並且其中至少1%的纖維具有不大於90%的真圓度(roundness)之非圓形截面形狀(特別是沿著整個纖維的縱向延伸或僅沿著部分纖維的縱向延伸)。   根據另一例示性實施例,提供一種直接由萊賽爾紡絲溶液製造(特別是溶噴的)非織纖維素纖維織物的方法,其中該方法包含將萊賽爾紡絲溶液經由孔口(其可實施為或其可形成部分的紡嘴或擠出單元)在藉助氣流下擠出而進入到凝聚流體環境(特別是分散的凝聚流體環境)中從而形成實質無末端纖維,將纖維收集在纖維支撐單元上從而形成織物,並調整製程參數,使得至少1%的纖維具有不大於90%的真圓度之非圓形截面形狀。   根據另外的例示性實施例,提供一種用於直接由萊賽爾紡絲溶液製造(特別是溶噴的)非織纖維素纖維織物的裝置,其中該裝置包含具有孔口的噴射嘴,其經配置用於將萊賽爾紡絲溶液在藉助氣流下擠出;凝聚單元,其經配置用於為擠出的萊賽爾紡絲溶液提供凝聚流體環境,從而形成實質無末端纖維;纖維支撐單元,其經配置用於收集纖維,從而形成織物;及控制單元(諸如處理器,其經配置用於執行用於直接從萊賽爾紡絲溶液製造非織纖維素纖維織物的程式碼),其經配置用於調整製程參數,使得至少1%的纖維具有不大於90%的真圓度之非圓形截面形狀。   根據又另一實施例,具有上述性質的非織纖維素纖維織物是用於由下列所組成的群組之至少一者:擦巾(wipe);過濾器;吸收性衛生產品;醫療應用產品;地工織物;農用織物;衣服;用於建築技術的產品;汽車產品;居家裝飾用品(furnishing);工業產品;與美容、休閒、運動或旅行相關的產品;以及與學校或辦公室相關的產品。   根據又另一實施例,提供包含具有上述性質的織物之產品或複合物。   在本申請案的上下文中,用語「非織纖維素纖維織物」(其也可表示為非織纖維素長絲織物)可具體地表示由複數個實質無末端纖維所組成的織物或網。用語「實質無末端纖維」特別具有長絲纖維的含義,該長絲纖維具有比習知短纖維顯著更長的長度。在替代性調配物中,用語「實質無末端纖維」可特別具有長絲纖維所形成之網的含義,該長絲纖維具有比習知短纖維顯著更小的每體積纖維末端量(amount of fiber ends per volume)。特別地,根據本發明的例示性實施例,織物的無末端纖維可具有小於10,000個末端/cm3 、特別是小於5,000個末端/cm3 的每體積纖維末端量。例如,當使用短纖維作為棉的代用品時,彼等可具有38mm的長度(對應於棉纖維的一般自然長度)。與此相反,非織纖維素纖維織物的實質無末端纖維可具有至少200mm、特別是至少1000mm的長度。然而,所屬技術領域中具有通常知識者會知道即使是無末端纖維素纖維也可能有中斷的事實,這可能是在纖維形成期間、及/或纖維形成之後的製程形成的。結果,相較於由相同丹尼(denier)的短纖維製成的非織物(nonwoven fabric),由實質無末端纖維素纖維製成的非織纖維素纖維織物具有顯著較低的每質量纖維數目。可藉由將複數個纖維紡絲,並藉由使該複數個纖維朝向較佳的移動式纖維支撐單元來抽長及拉伸,而製造非織纖維素纖維織物。因此,形成了纖維素纖維的三維網絡或網,而構成非織纖維素纖維織物。可由纖維素作為主要成分(或僅作為成分)製成該織物。   在本申請案的上下文中,用語「萊賽爾紡絲溶液」可具體地表示溶劑(例如,材料的極性溶液,諸如N-甲基-嗎啉N-氧化物;NMMO;「氧化胺」;或「AO」),纖維素(例如,木漿或其他纖維素系原料)在其中是溶解的。萊賽爾紡絲溶液是一種溶液而不是熔體(melt)。可藉由降低溶劑的濃度(例如,藉由使所述長絲與水接觸)而從萊賽爾紡絲溶液產生纖維素長絲。從萊賽爾紡絲溶液開始產生纖維素纖維的製程可描述為凝聚(coagulation)。   在本申請案的上下文中,用語「氣流」可具體地表示當萊賽爾紡絲溶液離開紡嘴時(及/或萊賽爾紡絲溶液離開紡嘴之後、或萊賽爾紡絲溶液已經離開紡嘴)實質上平行於纖維素纖維或其預成型體(亦即,萊賽爾紡絲溶液)的移動方向之氣體(例如空氣)的流動。   在本申請案的上下文中,用語「凝聚流體」可具體地表示非溶劑流體(亦即,氣體及/或液體,任意地包括固體粒子),該非溶劑流體具有將萊賽爾紡絲溶液稀釋、並且與溶劑交換至某種程度而使纖維素纖維由萊賽爾長絲形成之能力。例如,這種凝聚流體可以是水霧。   在本申請案的上下文中,用語「製程參數」可具體地表示用於製造非織纖維素纖維織物的物質、及/或裝置組件的所有物理參數、及/或化學參數、及/或裝置參數,其可能影響纖維及/或織物的性質,特別是纖維直徑及/或纖維直徑分佈。可藉由控制單元自動調整及/或由使用者手動調整這種製程參數,從而調諧(tune)或調整非織纖維素纖維織物之纖維的性質。可能影響纖維性質(特別是彼等之直徑或直徑分佈)的物理參數可以是該製程中涉及的各種介質(諸如萊賽爾紡絲溶液、凝聚流體、氣流等)的溫度、壓力、及/或密度。化學參數可以是涉及的介質(諸如萊賽爾紡絲溶液、凝聚流體等)之濃度、量、pH值。裝置參數可以是孔口之間的大小及/或距離、孔口與纖維支撐單元之間的距離、纖維支撐單元的運輸速度、一或多個任意的原位後加工單元之提供、氣流等。   用語「纖維」可具體地表示包含纖維素材料之細長片(elongated piece),例如,大致上圓形的、或非規則地形成的截面,任意地與其他纖維撚合。纖維可具有大於10、特別是大於100、更特別是大於1000的外觀比(aspect ratio)。外觀比是纖維長度與纖維直徑之間的比。纖維可藉由合併(以便形成整體的多纖維結構)或藉由摩擦(以便纖維保持分離,但藉由當相互移動中的纖維彼此物理性接觸時所施加的摩擦力微弱地機械耦合)而透過互連形成網絡。纖維可具有實質圓柱形式,然而其可以是直的、彎曲的,扭結的(kinked)、或弧形的。纖維可由單一均質材料(亦即,纖維素)組成。然而,纖維也可包含一或多種添加劑。液體材料(諸如水或油)可在纖維之間積累。   在本文件的上下文中,「具有孔口的噴射嘴」(其可例如表示為「孔口的配置」)可以是包含線性地配置的孔口之配置的任何結構。   在本申請案的上下文中,用語「真圓度」可具體地表示纖維截面的內切圓與外接圓之間的比值,亦即,剛好是足以適合纖維的截面內部、以及包圍纖維的截面形狀之圓的最大及最小尺寸。為了測定真圓度,可將垂直於纖維延伸方向的截面與纖維相交。因此,真圓度可表示為測量各個纖維的截面形狀接近100%的真圓度之圓的程度。例如,各個纖維的截面可具有卵形(oval)(特別是橢圓形(elliptic))形狀,或者可具有多邊形形狀。普遍地,界定纖維截面的外部界限之軌跡可以是顯示與圓之偏差的任何閉合平面線。各個纖維的截面可以是完全圓形的,或者可具有一或多個銳利的邊緣。   根據例示性實施例,提供具有實質無末端纖維並顯示與整個圓柱形形狀顯著偏差的非織纖維素纖維織物。從機械角度來看,這也導致在機械負載存在時,纖維的較佳彎曲方向是由纖維截面的設計所定義。例如,其中纖維具有橢圓形截面形狀,其具有長度不同的兩個主軸(亦即,長軸及短軸),在施加力的情況下將主要地以短軸作為彎曲線而發生彎曲。因此,此類纖維織物的彎曲特性不再是統計的及不可預測的,與此相反地,增加了非織纖維素纖維織物的明確順序。因此,藉由簡單地影響單根纖維的截面幾何,可用簡單的方式調整織物的明確機械性質。還可藉由調整一些或實質上全部纖維與完美圓形度的偏差而調整纖維的相互沉積(lay down)行為或網絡行為。此外,當非圓柱形纖維以有序的或部分有序的方式排列時,可製造具有異向性機械性質的非織纖維素纖維織物。It is an object of the present invention to provide cellulosic fabrics having adjustable mechanical stability. In order to achieve the above stated objectives, a nonwoven cellulosic fabric, a method of making a nonwoven cellulosic fabric, a device, product or composite for making a nonwoven cellulosic fabric, and Instructions. According to an exemplary embodiment of the invention, there is provided a (especially spray-sprayed) nonwoven cellulosic fibrous web (which is particularly straightforward (especially in an in situ process or in a continuously operated production line) In the continuous process performed) manufactured by lyocell spinning solution), and wherein at least 1% of the fibers have a non-circular cross-sectional shape of no more than 90% roundness (especially along the longitudinal direction of the entire fiber) Extending or extending only along the longitudinal direction of a portion of the fiber). According to another exemplary embodiment, there is provided a method of making a (particularly spray-sprayed) nonwoven cellulosic fabric directly from a lyocell spinning solution, wherein the method comprises passing the lyocell spinning solution through an orifice ( It can be embodied as a part of its spinning nozzle or extrusion unit) which, after being extruded by means of a gas stream, enters into a cohesive fluid environment, in particular a dispersed coacervate environment, to form substantially endless fibers, collecting the fibers in The fiber is supported on the unit to form a fabric and the process parameters are adjusted such that at least 1% of the fibers have a non-circular cross-sectional shape of no more than 90% roundness. According to a further exemplary embodiment, there is provided a device for the manufacture of a (especially spray-sprayed) nonwoven cellulosic fabric directly from a lyocell spinning solution, wherein the device comprises a spray nozzle having an orifice, the Arranged for extruding a lyocell spinning solution by means of a gas stream; a coalescing unit configured to provide a cohesive fluid environment for the extruded lyocell spinning solution to form a substantially endless fiber; a fiber support unit Having been configured to collect fibers to form a fabric; and a control unit (such as a processor configured to perform a code for fabricating a nonwoven cellulosic fabric directly from a lyocell spinning solution), It is configured to adjust process parameters such that at least 1% of the fibers have a non-circular cross-sectional shape of no more than 90% roundness. According to still another embodiment, the nonwoven cellulosic fiber fabric having the above properties is at least one of the group consisting of: a wipe; a filter; an absorbent hygiene product; a medical application product; Geotextiles; agricultural fabrics; clothing; products used in construction technology; automotive products; furnishing; industrial products; products related to beauty, leisure, sports or travel; and products related to schools or offices. According to yet another embodiment, a product or composite comprising a fabric having the above properties is provided. In the context of this application, the term "non-woven cellulosic fiber fabric" (which may also be referred to as a non-woven cellulose filament fabric) may specifically represent a fabric or web composed of a plurality of substantially endless fibers. The term "substantially endless fibers" particularly has the meaning of filament fibers which have a significantly longer length than conventional staple fibers. In alternative formulations, the term "substantially endless fibers" may particularly have the meaning of a web formed from filament fibers having a significantly smaller amount of fiber ends per volume than conventional short fibers (amount of fiber). Ends per volume). In particular, according to an exemplary embodiment of the invention, the endless fibers of the fabric may have an amount of fiber ends per volume of less than 10,000 ends/cm 3 , particularly less than 5,000 ends/cm 3 . For example, when staple fibers are used as a substitute for cotton, they may have a length of 38 mm (corresponding to the generally natural length of cotton fibers). In contrast, the substantially endless fibers of the nonwoven cellulosic fibrous web may have a length of at least 200 mm, especially at least 1000 mm. However, those of ordinary skill in the art will recognize the fact that even endless cellulosic fibers may be interrupted, which may be formed during the formation of the fibers, and/or after the formation of the fibers. As a result, the nonwoven cellulosic fabric made of substantially endless cellulosic fibers has a significantly lower number of fibers per mass than the nonwoven fabric made of the same denier staple fibers. . Nonwoven cellulosic fabrics can be made by spinning a plurality of fibers and by drawing and stretching the plurality of fibers toward a preferred mobile fiber support unit. Thus, a three-dimensional network or mesh of cellulosic fibers is formed to form a nonwoven cellulosic fiber fabric. The fabric can be made from cellulose as a main component (or only as a component). In the context of the present application, the term "Lysel spinning solution" may particularly denote a solvent (for example, a polar solution of a material such as N-methyl-morpholine N-oxide; NMMO; "amine oxide"; Or "AO"), in which cellulose (for example, wood pulp or other cellulosic materials) is dissolved. The lyocell spinning solution is a solution rather than a melt. Cellulosic filaments can be produced from a lyocell spinning solution by reducing the concentration of the solvent (e.g., by contacting the filaments with water). The process of producing cellulose fibers starting from a lyocell spinning solution can be described as coagulation. In the context of the present application, the term "airflow" may specifically mean when the lyocell spinning solution leaves the spinning nozzle (and/or after the lyocell spinning solution leaves the spinning nozzle, or the lyocell spinning solution has The exiting spout) is substantially parallel to the flow of gas (e.g., air) in the direction of movement of the cellulosic fibers or preforms thereof (i.e., the lyocell spinning solution). In the context of the present application, the term "condensed fluid" may particularly denote a non-solvent fluid (ie, a gas and/or a liquid, optionally including solid particles) having a dilution of the lyocell spinning solution, And the ability to exchange the solvent to some extent to form the cellulose fibers from the lyocell filaments. For example, such a cohesive fluid can be a water mist. In the context of the present application, the term "process parameters" may particularly denote all physical parameters, and/or chemical parameters, and/or device parameters of the materials used to make the nonwoven cellulosic fabric, and/or device components. It may affect the properties of the fibers and/or fabrics, in particular the fiber diameter and/or fiber diameter distribution. Such process parameters can be adjusted automatically by the control unit and/or manually adjusted by the user to tune or adjust the properties of the fibers of the nonwoven cellulosic fabric. Physical parameters that may affect the properties of the fibers (especially their diameter or diameter distribution) may be the temperature, pressure, and/or temperature of various media (such as lyocell spinning solution, coagulating fluid, gas stream, etc.) involved in the process. density. The chemical parameter can be the concentration, amount, pH of the medium involved (such as a lyocell spinning solution, a coagulating fluid, etc.). The device parameters may be the size and/or distance between the orifices, the distance between the orifices and the fiber support unit, the transport speed of the fiber support unit, the provision of one or more arbitrary in-situ processing units, gas flow, and the like. The term "fiber" may particularly denote an elongated piece comprising a cellulosic material, for example, a substantially circular, or irregularly formed, cross-section, optionally entangled with other fibers. The fibers may have an aspect ratio of greater than 10, especially greater than 100, and more specifically greater than 1000. The aspect ratio is the ratio between fiber length and fiber diameter. The fibers may be permeable by merging (to form a unitary multi-fiber structure) or by friction (so that the fibers remain separated, but weakly mechanically coupled by friction applied when the mutually moving fibers are in physical contact with each other) The interconnection forms a network. The fibers may have a substantially cylindrical shape, however they may be straight, curved, kinked, or curved. The fibers can be composed of a single homogeneous material (ie, cellulose). However, the fibers may also contain one or more additives. Liquid materials such as water or oil can accumulate between the fibers. In the context of this document, "a nozzle having an orifice" (which may be, for example, referred to as "arrangement of orifices") may be of any configuration including a configuration of orifices arranged linearly. In the context of the present application, the term "roundness" may specifically mean the ratio between the inscribed circle of the fiber section and the circumscribed circle, that is, just enough to fit inside the section of the fiber, and the section shape surrounding the fiber. The largest and smallest dimensions of the circle. To determine the roundness, a cross section perpendicular to the direction in which the fibers extend can be intersected with the fibers. Therefore, the roundness can be expressed as the degree of measuring the circle of the true circularity of the cross-sectional shape of each fiber close to 100%. For example, the cross section of each fiber may have an oval (especially elliptic) shape, or may have a polygonal shape. Generally, the trajectory defining the outer boundary of the fiber section can be any closed plane line that exhibits a deviation from the circle. The cross-section of each fiber may be completely circular or may have one or more sharp edges. According to an exemplary embodiment, a nonwoven cellulosic fiber fabric having substantial endless fibers and exhibiting significant deviation from the overall cylindrical shape is provided. From a mechanical point of view, this also results in the preferred direction of bending of the fibers in the presence of mechanical loads as defined by the design of the fiber cross-section. For example, in which the fiber has an elliptical cross-sectional shape having two major axes (i.e., a long axis and a short axis) having different lengths, the bending will be mainly performed with the short axis as a bending line in the case of applying a force. Therefore, the bending properties of such fiber fabrics are no longer statistical and unpredictable, and conversely, the clear sequence of nonwoven cellulosic fiber fabrics is increased. Thus, the clear mechanical properties of the fabric can be adjusted in a simple manner by simply affecting the cross-sectional geometry of the individual fibers. It is also possible to adjust the laydown behavior or network behavior of the fibers by adjusting the deviation of some or substantially all of the fibers from the perfect circularity. Further, when the non-cylindrical fibers are arranged in an ordered or partially ordered manner, a non-woven cellulose fiber fabric having anisotropic mechanical properties can be produced.

以下,描述非織纖維素纖維織物的另外的例示性實施例、製造非織纖維素纖維織物的方法、用於製造非織纖維素纖維織物的裝置、產品或複合物、以及使用方法。   在實施例中,至少3%、特別是至少5%、更特別是至少10%的纖維具有不大於90%的真圓度之非圓形截面形狀。甚至更具體地,可能至少10%、至少20%、至少30%、至少50%、或至少80%的纖維具有不大於90%、不大於80%、不大於70%、不大於60%、不大於50%、或不大於30%的真圓度之非圓形截面形狀。偏離圓形截面形狀的纖維量愈高,所製造的纖維織物與等方性(isotropic)機械行為的偏差越高,並且織物的機械性質的可調整性越顯著。   在實施例中,至少1%、至少10%、至少20%、至少30%、至少50%、或至少80%的纖維具有不大於80%、特別是不大於70%、更特別是不大於50%的真圓度之非圓形截面形狀。甚至更具體地,可能至少1%的纖維具有不大於60%、不大於50%、不大於40%、或不大於10%的真圓度之非圓形截面形狀。偏離圓形截面形狀的至少部分的纖維量愈高,所製造的纖維織物與等方性機械行為的偏差越高,並且織物機械性質的可調整性越顯著。   例如,藉由調整孔口的數目及/或形狀,可調整具有具備相應真圓度值的非圓形截面形狀的纖維百分比,通過該孔口射出萊賽爾紡絲溶液,該萊賽爾紡絲溶液在凝聚後形成纖維。附加地或替代地,例如藉由調整萊賽爾紡絲溶液(其在凝聚前經受用於改變截面形狀之機械衝擊)之長絲的數目,可調整具有具備相應真圓度值的非圓形截面形狀之纖維百分比。   在實施例中,在非織標準WSP90.3的基礎上,用「織物手感測試儀(Handle-O-Meter)」分別測得織物之光滑度及具體手感是在2mNm2 /g與70mNm2 /g之間的範圍。藉由改變所述製造方法的製程參數,可因此在寬範圍內改變光滑度。當設計具有非圓形截面或非圓柱形幾何的纖維時,可能已經確保織物之足夠的及明確的穩定性。接著可自由地調整表面的光滑度(甚至是非常高的光滑度)而不會使織物的穩定性遭受此危害。   在非織標準WSP90.3的基礎上,用「織物手感測試儀」(商購自Thwing-Albert Instrument Co., Philadelphia, PA)可測量經提及之織物的光滑度。為了測定織物的光滑度,降低「織物手感測試儀」的樞轉臂,並將織物的樣本(例如具有10cmx10cm的正方形維度)壓入可調整的平行狹縫中。測量為了將樣本壓入狹縫所需的力。在此程序期間,在樣本上施加彎曲力及摩擦力。CD方向及MD方向上的測量平均值對應於將樣本壓過狹縫所需的平均力。平均力(例如以mN表示)與織物的基礎重量(例如以g/m2 表示)之間的比得到光滑度值(經測量以作為具體手感),以mNm2 /g表示,其代表織物材料的光滑度。   在實施例中,纖維具有小於5ppm的銅含量及/或具有小於2ppm的鎳含量。在本申請案中提及的ppm值都是關於質量(而不是體積)。除此之外,對於各個個別的化學元素,纖維或織物的重金屬污染可能不超過10ppm。由於使用萊賽爾紡絲溶液作為形成無末端纖維系織物的基礎(特別是當涉及溶劑(諸如N-甲基-嗎啉N-氧化物;NMMO)時),織物有重金屬諸如銅或鎳(其可能引起使用者的過敏反應)的污染可能會保持非常小。由於在藉由製程控制而可調節的某些條件下直接合併纖維的概念,在用於使纖維互連的製程中不需要引入額外的材料(諸如膠水或類似者)。這使織物的污染非常低。   在實施例中,至少部分的(特別是至少10%、更特別是至少20%的)纖維在合併位置處整體合併。在本申請案的上下文中,用語「合併」可具體地表示在各個合併位置處不同纖維的整體互連,其導致由先前分離的纖維預成型體所組成的一個整體連接的纖維結構形成。合併可表示為在一個、一些、或所有合併的纖維之凝聚期間建立纖維-纖維連接。互連的纖維可在各個合併位置處彼此強力地黏著,而不需要不同的附加材料(例如,單獨的黏著劑)以形成共同的結構。分離合併的纖維可能需要破壞纖維網絡或其部件。根據所述的實施例,提供非織纖維素纖維織物,其中一些或所有纖維藉由合併彼此整體連接。可藉由對製造非織纖維素纖維織物的方法之製程參數相應的控制來觸發合併。具體地,在尚未處於沉澱的固體纖維狀態之萊賽爾紡絲溶液的長絲之間第一次接觸之後,可觸發(或至少完成)這些長絲的凝聚。因此,這些長絲(當其仍處於溶液相時,然後或之後藉由凝聚將彼等轉化成固相)之間的交互作用允許適當地調整合併特徵。合併度是一個有力的參數,其可用於微調所製造的織物之性質。具體而言,網絡的機械穩定性愈大,合併位置的密度愈高。藉由在織物體積上的合併位置之不均勻分佈,亦有可能調整高機械穩定性的區域及其他低機械穩定性的區域。例如,將織物分離成單獨的部件可精確地限定在具有少量合併位置之機械性薄弱區域局部地發生。在較佳的實施例中,可藉由使不同的纖維預成型體以萊賽爾紡絲溶液的形式在凝聚之前彼此直接接觸,來觸發纖維之間的合併。藉由這種凝聚製程,來執行纖維的單一材料共同沉澱,從而形成合併位置。   在實施例中,合併點或合併位置由與合併的纖維相同的材料組成。因此,藉由直接由萊賽爾紡絲溶液的凝聚產生的纖維素材料可形成合併位置。這不僅使得單獨提供纖維連接材料(諸如黏著劑或黏合劑)可有可無,還可使織物保持清潔並由且單一材料製成。具有非圓形截面的纖維之形成及藉由合併互連的纖維之形成,可藉由一種單一的共同製程完成。其原因在於,纖維之間合併位置(諸如合併點或合併線)的形成以及具有偏離完美圓形直徑截面的纖維之形成,二者皆可在凝聚完成之前,藉由在萊賽爾紡絲溶液的長絲上施加機械力來實現。然而,萊賽爾紡絲溶液的長絲在其仍處於液相時可能受到機械影響。描述性地說,一方面對仍為液體或黏性(通常以蜂蜜狀稠度存在)萊賽爾紡絲溶液的長絲施加機械壓力,可促進圓柱形長絲變形成(例如卵形(特別是橢圓形))非圓形截面形狀,從而降低真圓度。同時,在仍為液體或黏性萊賽爾紡絲溶液的長絲上施加這種機械壓力以及使彼此物理性接觸,會在凝聚時觸發纖維之間合併位置的形成。   在實施例中,纖維的不同者至少部分地位於不同的可分辨(亦即,於層之間顯示可見的分離或界面區域)之層中。例如,可藉由各層的纖維之真圓度值的個別調整來調整層之間以及層之間的界面處之不同機械性質。   更具體地,不同的層之纖維在層之間的至少一個合併位置處整體合併。因此,至少部分地位於不同的可分辨之層中的纖維之不同者(其關於一或多個參數,諸如合併因子、纖維厚度等,可能相同或可能不同)可在至少一個合併位置處整體連接。例如,可藉由將二(或更多)個具有孔口的噴射嘴連續排列來形成織物的二(或更多)個不同層,通過該孔口擠出萊賽爾紡絲溶液以用於凝聚及纖維形成。當這種配置與移動式纖維支撐單元(諸如具有纖維容納表面的輸送帶)組合時,第一層纖維是藉由第一噴射嘴形成於纖維支撐單元上,並且當移動式纖維支撐單元到達第二噴射嘴的位置時,第二噴射嘴在第一層上形成第二層纖維。可調整此方法的製程參數,使得合併點在第一層與第二層之間形成。具體而言,正在形成的第二層纖維尚未完全藉由凝聚而固化(cured)或固體化(solidified),可能例如仍然具有仍處於液體萊賽爾溶液相且尚未處於完全固化(cured)之固態的外部表皮或表面區域。當這種預纖維結構(pre-fiber structure)彼此接觸並且之後完全固化成固體纖維狀態時,這會造成在不同層之間的界面處形成兩個合併的纖維。合併位置的數目愈多,織物層之間的互連穩定性愈高。因此,控制合併允許控制織物層之間連接的剛性。例如,在各層的預纖維結構到達纖維下層或預纖維結構上的纖維支撐板之前,可藉由調整固化或凝聚程度來控制合併。藉由在其間的界面處合併不同層的纖維,可防止層的非所欲分離。在層之間沒有合併點的情況下,可能使一層纖維與另一層纖維剝離。根據本發明的例示性實施例,可在「未合併的纖維或層」及「完全合併的纖維或層」之間逐漸調整纖維之間及/或層之間的黏附程度。結果,可控制並調整特別是在不同層之間的部分黏附,以使基於織物所製造的產品之織物功能化。例如,可使用這種(特別是多層)織物製造包裝,該織物提供輕微的黏附力,使得包裝好的產品可透過其微弱的黏附部件適當地處理。   為了測定織物的前述合併因子(其也可表示為面積合併因子),可執行下列的測定程序:可光學性地分析織物的正方形樣本。圍繞著與正方形樣本的至少一個對角線交叉的纖維的各合併位置來繪製圓,該圓具有必須完全留在正方形樣本內部的直徑。測定圓的尺寸,使得圓涵蓋合併的纖維之間的合併區域。計算所測定之圓的直徑之算術平均值。合併因子計算為正方形樣本的平均直徑值與對角線長度之間的比值,並且可以百分比表示。   在實施例中,至少部分的纖維是經加撚的。將纖維加撚是設計纖維網絡的機械強度更有力的工具。例如,加撚之纖維可具有比完全直的纖維更高的機械穩定性。同樣地,形成加撚之纖維組(例如加撚的合併纖維)可以類似的方式顯著提高織物的機械穩定性,因為加撚之長絲的繩具有比相應數目的單長絲顯著更高的機械穩定性。例如,可藉由在拉伸階段期間(亦即,在凝聚或沉澱之前),轉動或旋轉萊賽爾紡絲溶液的長絲來製造加撚之纖維。特別是渦度(vorticity)的應用,亦即在凝聚之前,萊賽爾紡絲溶液的長絲周圍的擾流可用於形成加撚之纖維。   在實施例中,纖維在織物內經各向異性地排列從而大致上界定出至少一個優先排列方向,相較於其他方向,較大部分的纖維沿著該至少一個優先排列方向排列。在這樣的實施例中,可對織物的一組纖維或所有纖維進行纖維形狀的調整以偏離圓形截面,使得當纖維沉積在纖維支撐單元上時,彼等大致上或較佳地沿一或多個主要方向排列,這是由於彼等的較佳彎曲軸由各纖維圓角的偏差確定。藉由採取這種措施,可在織物中引入一定程度的順序,其導致所製造的織物之非等方性(non-isotripic)性質。   在實施例中,調整製程參數包含在凝聚完成之前對萊賽爾紡絲溶液的長絲施加力。描述性地說,當在轉化為固相之前將壓縮力施加到萊賽爾紡絲溶液之黏性的且因而仍可流動的長絲時,該長絲可從例如圓柱形截面形狀變形成例如卵形(特別是橢圓形)截面形狀。可在垂直於分析中之纖維或纖維部分的縱向延伸方向上施加纖維變形力。當在萊賽爾紡絲溶液的長絲處於此變形形狀的同時進行凝聚時,獲得小於1之真圓度的纖維。   在實施例中,在凝聚完成之前,藉由將成形流體(其可以是液體及/或氣體)引導至萊賽爾紡絲溶液的長絲來施加力。這種成形流體可以是成形氣體(諸如空氣)或成形液體(諸如水)。當採用成形氣體時,可精確限定的機械力適用於尚未凝聚的長絲而不會引發凝聚。當使用成形液體時,可精確限定的機械力亦適用於尚未凝聚的長絲,其同時亦藉由以(特別是水性的)液體稀釋萊賽爾紡絲溶液來觸發凝聚。在這樣的實施例中,變形及凝聚可同時進行。   在實施例中,藉由氣體或液體(亦即,流體)流提及之壓力增加,可經配置使得各個流體流在某個位置處反平行(antiparallel),並且正在形成的纖維介於其間。結果,產生局部不對稱壓力增加,而影響纖維。同時,此現象不會進一步影響製造纖維的程序。   在實施例中,至少一些孔口是非圓形的,特別是卵形(特別是橢圓形)或多邊形。較佳地,界定孔口的纖維形成單元之噴射板中的開口,可具有與通過這些個別孔口所射出之沉澱的萊賽爾紡絲溶液所組成的纖維有實質上相同的真圓度(特別是不大於90%)之形狀。在一個實施例中,孔口的第一部分具有圓形開口,而孔口的第二部分具有非圓形開口。因此,孔口的形狀設計在某種程度上也允許限定所製造的纖維形狀。   在實施例中,調整用於調整合併的製程參數,包括在萊賽爾紡絲溶液已經離開孔口之後、並在萊賽爾紡絲溶液到達纖維支撐單元之前,形成至少部分的合併位置。當向下移動時,這可例如藉由觸發經擠出而通過不同孔口的萊賽爾紡絲溶液的股之間的相互作用來實現。例如,可在強度及方向方面調整氣流,使得(尚未完全凝聚的)紡絲溶液的不同股或長絲,在到達纖維支撐單元之前,被迫在橫向方向上彼此進行交互作用。也可在接近或處於擾流狀態下操作氣流,以促進纖維的各種預成型體之間的相互交互作用。因此,在凝聚之前,纖維的各個預成型體可彼此接觸,從而形成合併位置。   在實施例中,調整用於調整合併的製程參數,包括在萊賽爾紡絲溶液藉由沉積在纖維支撐單元上時觸發至少部分的纖維凝聚而到達纖維支撐單元之後,形成至少部分的合併位置。在這樣的實施例中,可有意地延遲凝聚程序(其可藉由凝聚單元的相應操作來調整,特別是藉由相應地調整凝聚流體的性質及供應位置)。更具體地,可延遲凝聚程序,直到紡絲溶液已經到達纖維支撐板。在這樣的實施例中,仍然在凝聚之前,將纖維的預成型體沉積在纖維支撐板上,從而又在凝聚之前與纖維的其他預成型體接觸。因此可迫使不同股或預成型體之紡絲溶液流動而彼此接觸,並且其後僅可觸發或完成凝聚。因此,在仍處於非凝聚狀態的不同纖維預成型體之間的初始接觸之後的凝聚,是形成合併位置的有效措施。   在實施例中,調整用於調整合併的製程參數,包含沿著可移動纖維支撐單元連續配置具有孔口的多個噴射嘴,在纖維支撐單元上沉積第一層纖維,以及在層之間的界面處至少部分的纖維已經完成凝聚之前,在第一層上沉積第二層纖維。對於待形成的各層,可調整操作相應噴射嘴的製程參數,以便獲得層特定的凝聚行為。可調整不同層的層特定的凝聚行為,使得在相應層內且較佳是在相鄰層之間形成合併位置。更具體地,可調整製程控制,藉由僅在與不同層相關的紡絲溶液之間的初始接觸之後促進兩層的凝聚,以便在兩個相鄰層之間形成合併位置。   在實施例中,該方法另外包含在纖維支撐單元上的收集之後,進一步加工纖維及/或織物,但較佳地仍在原位形成具有無末端纖維之非織纖維素纖維織物。這種原位製程可以是在製造的(特別是實質上無末端的)織物被儲存(例如由捲繞機捲起)之前進行的該等製程,用於運輸至產品製造目的地。例如,這種進一步加工可涉及水纏結。水纏結可表示為濕式或乾式纖維網的黏合製程,所得黏合織物是非織物。水纏結可使用細的高壓水注,其穿透纖維網、撞擊纖維支撐單元(特別是傳送帶)並反彈,導致纖維纏結。織物的相應壓縮可使織物更緊湊並且機械上更穩定。除了水纏結之外或替代地,可用加壓蒸汽對纖維進行蒸汽處理。附加地或替代地,這種進一步加工或後加工可能涉及對所製造的織物進行針刺處理。針扎系統可用於黏合織物或網的纖維。當刺針穿過纖維網時,可迫使一些纖維穿過纖維網,當針抽出時纖維留下,以生產針扎織物。如果適當地移位足夠的纖維,則藉由這些纖維柱塞的固結效果,可將網轉化成織物。網或織物的又另一個進一步加工或後處理是含浸處理。含浸無末端纖維的網絡可涉及在織物上施加一或多種化學品(例如軟化劑、疏水劑、抗靜電劑等)。又另一個進一步加工處理是壓延。壓延可表示為處理織物的加工製程,並且可使用壓延機來光滑、塗覆、及/或壓縮織物。   根據本發明的例示性實施例之非織纖維素纖維織物亦可與一或多種其他材料合併(例如原位或在後續的製程中),從而形成根據本發明的例示性實施例之複合物。可與用於形成這種複合物的織物合併的例示性材料,可選自包含(但不限於)下列材料或其組合的群組:短纖漿、纖維懸浮液、濕式成網非織物、氣流成網非織物、紡黏網、熔噴網、梳棉射流噴網、或針刺網,或由各種材料製成的其他片狀結構。在實施例中,不同材料之間的連接可藉由(但不限於)下列製程中的一種或其組合進行:合併、水纏結、針刺、氫鍵結、熱黏合、透過黏合劑膠合、貼合、及/或壓延。   以下,總結包含或使用根據本發明的例示性實施例之非織纖維素纖維織物的例示性有利產品:   網(100%纖維素纖維網、或例如包含二或更多種纖維或由二或更多種纖維組成的網、或化學改質纖維、或具有摻入材料(諸如抗菌材料、離子交換材料、活性碳、奈米粒子、洗劑、藥劑或阻燃劑、或雙組分纖維)的纖維)的特殊用途可如下列者:   根據本發明的例示性實施例之非織纖維素纖維織物可用於製造擦巾,諸如嬰兒擦巾、廚房用擦巾、濕巾、化妝擦巾、衛生擦巾、醫療擦巾、清潔擦巾、拋光擦巾(汽車用、家具用)、灰塵擦巾、工業用擦巾、除塵機擦巾、拖把擦巾。   根據本發明的例示性實施例的非織纖維素纖維織物也可能用於製造過濾器。例如,這種過濾器可以是空氣過濾器、HVAC、空調過濾器、煙道氣過濾器、液體過濾器、咖啡過濾器、茶袋、咖啡袋、食物過濾器、水淨化過濾器、血液過濾器、香煙過濾器、座艙過濾器、濾油器、筒式過濾器、真空過濾器、真空吸塵器濾袋、濾塵器、液壓過濾器、廚房過濾器、風扇過濾器、水分交換過濾器、花粉過濾器、HEVAC/HEPA/ULPA過濾器、啤酒過濾器、牛奶過濾器、液體冷卻劑過濾器、及果汁過濾器。   在又另一實施例中,非織纖維素纖維織物可用於製造吸收性衛生產品。其實例是收集層、保健衛生用透氣織物(coverstock)、吸收性覆蓋物、分佈層、衛生護墊、覆面材、背板、腿箍、可沖洗性產品、墊、護理墊、拋棄式內褲、訓練褲、面罩、美容面膜、卸妝墊、毛巾、尿布、及用於釋放活性組分(諸如紡織品柔軟劑)的洗衣烘乾機用紙。   在又另一實施例中,非織纖維素纖維織物可用於製造醫療應用產品。例如,這種醫療應用產品可以是拋棄式帽子、長袍、口罩及鞋套、傷口護理產品、無菌包裝產品、保健衛生用透氣織物產品、敷料材料、單向服裝、滲析產品、鼻條、牙板黏著劑、拋棄式內褲、帷簾、纏繞及包裝、海綿、敷料及擦布、床用織物、經皮藥物遞送、壽衣、看護墊、手術包(procedure pack)、加熱包、造口袋襯墊、固定貼片、及培育箱墊。   在又另一實施例中,非織纖維素纖維織物可用於製造地工織物。這可涉及農作物生產保護覆蓋層、毛細氈、水淨化、灌溉控制、瀝青覆蓋層、土壤穩定、排水、沉積及侵蝕控制、池塘襯墊、含浸基、排水道襯墊、地面穩定、坑襯、種子毯、雜草控制織物、溫室陰影、根袋、及生物可降解植物盆。也可將非織纖維素纖維織物用於植物箔(例如為植物提供光保護及/或機械保護、及/或為植物或土壤提供糞便或種子)。   在另一實施例中,非織纖維素纖維織物可用於製造衣服。例如,可在這種織物的基礎上製造裏襯、衣服絕緣及保護、手提包組件、鞋組件、帶襯墊、工業帽/鞋、拋棄式工作服、衣服及鞋袋、以及熱絕緣。   在又另一實施例中,非織纖維素纖維織物可用於製造用於建築技術的產品。例如,可使用這種織物製造屋面及瓷磚墊層、石板瓦墊層(underslating)、隔熱及隔音、房屋包層(house wrap)、石膏板飾面、管道包層、混凝土模塑層、地基及地面穩定、垂直排水系統、舖蓋板、屋頂氈、噪音削減、強化體、密封材料、及阻尼材料(機械的)。   在又另一實施例中,非織纖維素纖維織物可用於製造汽車產品。實例是座艙過濾器、靴子襯墊、置物架、隔熱罩、貨架裝飾、模製罩蓋襯墊、靴底覆蓋層、濾油器、頂棚襯墊、後置物架、裝飾織物、安全氣囊、消音器墊、絕緣材料、車罩、底部填料(underpadding)、汽車腳墊、磁帶、背襯及簇絨地毯、座套、門飾、針刺地毯、及汽車地毯背襯。   根據本發明的例示性實施例製造的織物的另一個應用領域是居家裝飾用品,諸如家具、結構、手臂及背部的絕緣體、墊子加厚、防塵罩、襯墊、縫合加強件、邊緣裝飾材料、床架結構、被褥背襯、彈簧包層、床墊墊子組件、床墊罩、窗簾、牆面覆蓋物、地毯背襯、燈罩、床墊組件、彈簧絕緣體、密封件、枕頭緹花、及床墊緹花。   在又另一實施例中,非織纖維素纖維織物可用於製造工業產品。這可涉及電子產品、軟磁碟襯墊、電纜絕緣、研磨料、絕緣膠帶、輸送帶、噪音吸收層、空調、電池隔板、酸性系統、防滑氈去污機、食品包層、膠帶、香腸腸衣、乳酪腸衣、人造皮革、採油臂架(boom)及套袋(sock)、以及造紙毛氈。   根據本發明的例示性實施例的非織纖維素纖維織物亦適用於製造與休閒及旅行相關的產品。這種應用的實例是睡袋、帳篷、行李箱、手袋、購物袋、航空頭靠、CD保護套、枕頭套、及三明治包裝。   本發明的例示性實施例的又另一個應用領域關於學校及辦公室產品。例如,應提及書套、郵寄信封、地圖、標誌及三角旗、毛巾、及旗幟。   附圖中的插圖是示意性的。在不同的圖中,類似或相同的元件或特徵提供相同的參考標記。   圖1根據本發明的例示性實施例繪示裝置100,用於製造由萊賽爾紡絲溶液104直接形成的非織纖維素纖維織物102。萊賽爾紡絲溶液104藉由凝聚流體106至少部分地凝聚,以轉化成部分形成的纖維素纖維108。藉由裝置100,可執行根據本發明的例示性實施例之萊賽爾溶液噴紡法。在本申請案的上下文中,用語「萊賽爾溶液噴紡法」可具體涵蓋可得到離散長度之基本上無末端長絲或纖維108、或獲得離散長度之無末端長絲及纖維的混合物的方法。如下面進一步描述的,根據本發明的例示性實施例,提供了各自具有孔口126的噴嘴,纖維素溶液或萊賽爾紡絲溶液104透過該噴嘴與氣流(gas stream或gas flow)146一起噴出,以用於製造非織纖維素纖維織物102。   從圖1可看出,木漿110、其他纖維素系原料等可經由計量單元113供應至儲槽114。來自水容器112的水亦經由計量單元113供應至儲槽114。因此,在下面進一步詳細描述的控制單元140的控制下,計量單元113可定義要供應至儲槽114的水及木漿110的相對量。容納在溶劑容器116中的溶劑(諸如N-甲基-嗎啉N-氧化物;NMMO)可在濃縮單元118中濃縮,然後可在混合單元119中與水及木漿110、或其他纖維素系的原料之混合物以可確定的相對量混合。亦可藉由控制單元140來控制混合單元119。因此,以可調整的相對量將水-木漿110介質溶解在溶解單元120的濃縮溶劑中,從而獲得萊賽爾紡絲溶液104。水性萊賽爾紡絲溶液104可以是由包含木漿110及溶劑(例如85質量%至95質量%)的纖維素(例如5質量%至15質量%)所組成的蜂蜜黏稠性介質。   將萊賽爾紡絲溶液104送至纖維形成單元124(其可實施為或可包含多個紡絲束或噴射嘴122)。例如,噴射嘴122的孔口126的數目可大於50,特別是大於100。在一個實施例中,纖維形成單元124(其可包含多個紡嘴或噴射嘴122)的所有孔口126可具有相同的大小及/或形狀。或者,一個噴射嘴122的不同孔口126及/或不同噴射嘴122(其可連續配置以用於形成多層織物)的孔口126的大小及/或形狀可以是不同的。   當萊賽爾紡絲溶液104通過噴射嘴122的孔口126時,其被分成多個平行的萊賽爾紡絲溶液104股。垂直定向的氣流(亦即,經定向實質上平行於紡絲方向)迫使萊賽爾紡絲溶液104轉換成愈來愈長及愈來愈細的股,可藉由在控制單元140的控制下改變製程條件來調整股。氣流可從孔口126至纖維支撐單元132將萊賽爾紡絲溶液104沿其至少一部分路徑加速。   當萊賽爾紡絲溶液104通過噴射嘴122移動並進一步向下時,萊賽爾紡絲溶液104之長且細的股與非溶劑凝聚流體106進行交互作用。凝聚流體106有利地實施為蒸氣霧,例如水霧。藉由一或多個凝聚單元128控制凝聚流體106的製程相關性質,從而為凝聚流體106提供可調整的性質。依次藉由控制單元140控制凝聚單元128。較佳地,各個凝聚單元128是設置在各個噴嘴或孔口126之間,用於個別調整正在生產的織物102之各層的性質。較佳地,各噴射嘴122可具有兩個經配置的凝聚單元128,每側各一個。個別的噴射嘴122可因此設置有萊賽爾紡絲溶液104的個別部分,其也可調整成具有不同層的製造織物102的不同可控制性質。   當與凝聚流體106(例如水)進行交互作用時,萊賽爾紡絲溶液104的溶劑濃度降低,使得凝聚流體的纖維素例如木漿110(或其他原料)至少部分地凝聚為長且細的纖維素纖維108(其可能仍含有殘餘的溶劑和水)。   在從擠出的萊賽爾紡絲溶液104初始形成單根纖維素纖維108期間或之後,纖維素纖維108沉積在纖維支撐單元132上,纖維支撐單元132在此實施為具有平面纖維容納表面的輸送帶。纖維素纖維108形成非織纖維素纖維織物102(在圖1中僅示意性地繪示)。非織纖維素纖維織物102是由連續的且實質上無末端之長絲或纖維108所組成。   雖然未在圖1中示出,但可至少部分地再回收藉由凝聚單元128凝聚並且在洗滌單元180中洗滌而移除的萊賽爾紡絲溶液104的溶劑。   當沿著纖維支撐單元132輸送時,可藉由供應洗滌液之洗滌單元180洗滌非織纖維素纖維織物102以移除殘餘溶劑,然後可將其乾燥。彼可藉由任意的但有利的進一步加工單元134進一步加工。例如,這種進一步加工可涉及水纏結、針扎、含浸、用加壓蒸汽進行蒸汽處理、壓延等。   纖維支撐單元132亦可將非織纖維素纖維織物102輸送至捲取機136,非織纖維素纖維織物102可作為實質上無末端片材收集在捲取機136上。然後可將非織纖維素纖維織物102作為卷材(roll-good)運送至製造基於非織纖維素纖維織物102的產品(諸如擦巾或紡織品)之實體。   如圖1所示,所述的製程可藉由控制單元140(諸如處理器、部分的處理器、或複數個處理器)來控制。控制單元140經配置以用於控制圖1中所示的各種單元的操作,特別是一或多種計量單元113、混合單元119、纖維形成單元124、(多個)凝聚單元128、進一步加工單元134、溶解單元120、洗滌單元180等。因此,控制單元140(例如,藉由執行電腦可執行程式碼、及/或藉由執行由使用者定義的控制命令)可精確地並靈活地定義製程參數,根據該製程參數製造非織纖維素纖維織物102。在此上下文中的設計參數是沿著孔口126的氣流、凝聚流體106的性質、纖維支撐單元132的驅動速度、萊賽爾紡絲溶液104的組成、溫度及/或壓力等。另外的設計參數(為了調整非織纖維素纖維織物102的性質,該等參數是可調整的)是孔口126的數目、及/或相互距離、及/或幾何配置,萊賽爾紡絲溶液104的化學組成及濃度等。因此,如下所述,可適當地調整非織纖維素纖維織物102的性質。這種可調整的性質(參見以下的詳細描述)可涉及一或多種下列性質:纖維108的直徑及/或直徑分佈、纖維108之間合併的量及/或區域、纖維108的純度位準、多層織物102性質、織物102的光學性質、織物102的流體滯留及/或流體釋放性質、織物102的機械穩定性、織物102表面的光滑度、纖維108的截面形狀等。   雖然未示出,但是各紡絲噴射嘴122可包含聚合物溶液入口,經由該聚合物溶液入口將萊賽爾紡絲溶液104供應至噴射嘴122。經由空氣入口,可將氣流146施加至萊賽爾紡絲溶液104。從噴射嘴122內部的交互作用室開始並且由噴射嘴殼體界定,萊賽爾紡絲溶液104通過各個孔口126向下移動或加速(藉由氣流146將萊賽爾紡絲溶液104向下拉),並且在氣流146的影響下橫向地縮小,使得當萊賽爾紡絲溶液104與氣流146一起在凝聚流體106的環境中向下移動時,形成持續變細的纖維素長絲或纖維素纖維108。   因此,參考圖1所述的製造方法所涉及的製程可包括將萊賽爾紡絲溶液104(其也可表示為纖維素溶液)成形以形成液體股或潛在長絲,該液體股或潛在長絲是由氣流146拉伸並且顯著地直徑減小及長度增加。在纖維支撐單元132上形成網之前或期間,也可能涉及藉由凝聚流體106部分地凝聚潛在長絲或纖維108(或其預成型體)。使長絲或纖維108形成網狀織物102、洗滌、乾燥,並且可根據需要進一步加工(參見進一步加工單元134)。例如可將長絲或纖維108收集在例如旋轉滾筒或帶上,藉此形成網。   由於所述的製造製程,特別是所用溶劑的選擇,纖維108具有小於5ppm的銅含量及/或具有小於2ppm的鎳含量。這有利地提高了織物102的純度。   根據本發明的例示性實施例之萊賽爾溶液噴紡網(亦即,非織纖維素纖維織物102)較佳地展現出一或多種下列性質:   (i)網的乾重是5至300g/m²,較佳的是10-80g/m²   (ii)分別根據標準WSP120.6或DIN29073(特別是在本專利申請的優先權日有效的最新版本中),網的厚度是0.05至10.0mm,較佳的是0.1至2.5mm   (iii)分別根據EN29073-3或ISO9073-3(特別是在本專利申請的優先權日有效的最新版本中),MD的網之特定強度範圍是0.1至3.0Nm²/g,較佳的是0.4至2.3Nm²/g   (iv)分別根據EN29073-3或ISO9073-3(特別是在本專利申請的優先權日有效的最新版本中),網的平均伸度範圍是0.5至100%,較佳的是4至50%   (v)網的MD/CD強度比值為1至12   (vi)根據DIN 53814(特別是在本專利申請的優先權日有效的最新版本中),網的水滯留是1至250%,較佳的是30至150%   (vii)根據DIN 53923(特別是在本專利申請的優先權日有效的最新版本中),網的保水容量範圍是90至2000%,較佳的是400至1100%   (viii)根據分解標準EN 15587-2及ICP-MS標準EN 17294-2,特別測得銅含量低於5ppm及鎳含量低於2ppm之金屬殘留位準。   最佳地,萊賽爾溶液噴紡網展現出以上所提及的所有所述特性(i)至(viii)。   如所述的,生產非織纖維素纖維織物102的製程較佳地包含下列各者:   (a)通過至少一個噴射嘴122的孔口126,將包含溶解於NMMO中的纖維素溶液(參見參考符號104)擠出,從而形成萊賽爾紡絲溶液104的長絲   (b)藉由氣流(參見參考符號146)將萊賽爾紡絲溶液104的所述長絲拉伸   (c)使所述長絲與蒸汽霧(參見參考符號106)(較佳地含有水)接觸,從而至少部分地沉澱所述纖維108。因此,在形成網或非織纖維素纖維織物102之前,使長絲或纖維108至少部分地沉澱   (d)收集及沉澱所述長絲或纖維108,以形成網或非織纖維素纖維織物102   (e)移除洗滌管線中的溶劑(參見洗滌單元180)   (f)任意地經由水纏結、針扎等進行接合(參見進一步加工單元134)   (g)乾燥及收卷。   可藉由合併、交纏絡、氫鍵結、物理接合(諸如水纏結或針扎)、及/或化學鍵結而結合非織纖維素纖維織物102的成分。   為了進一步加工,可將非織纖維素纖維織物102與一或多層相同的及/或其他的材料合併,諸如(未示出)合成聚合物層、纖維素短纖漿、纖維素或合成聚合物纖維的非織網、雙組分纖維、纖維素紙漿網(諸如氣流成網或濕法成網紙漿)、高強度纖維網或織物、疏水材料、高性能纖維(諸如耐熱材料或阻燃劑材料)、賦予改變的機械性質的層至最終產品(諸如聚丙烯或聚酯層)、可生物降解材料(例如,來自聚乳酸之膜、纖維、或網)、及/或高散裝材料。   也可合併非織纖維素纖維織物102的數個可分辨之層,參見例如圖7。   非織纖維素纖維織物102可基本上僅由纖維素組成。或者,非織纖維素纖維織物102可包含纖維素及一或多種其他纖維材料的混合物。此外,非織纖維素纖維織物102可包含雙組分纖維材料。非織纖維素纖維織物102中的纖維材料可至少部分地包含改質物質。改質物質可以是選自由例如下列所組成的群組:聚合物樹脂、無機樹脂、無機顏料、抗菌產品、奈米粒子、洗劑、阻燃劑產品、吸收性改進添加劑(諸如超吸收性樹脂)、離子交換樹脂、碳化合物(諸如活性炭、石墨、導電性碳)、X-射線對比物質、發光顏料、及染料。   最後,由萊賽爾紡絲溶液104直接製造的纖維素非織網或非織纖維素纖維織物102,使得有機會實現不可能經由短纖維路徑得到的加值網性能。這包括有機會形成均勻的輕質網、製造微纖維產品、以及製造形成網的連續長絲或纖維108。再者,與短纖維網相比,不再需要數個製造程序。再者,根據本發明的例示性實施例之非織纖維素纖維織物102是可生物降解的,並且由可持續採購的原物料(亦即,木漿110等)製造。此外,在純度及吸收性方面具有優勢。除此之外,具有可調整的機械強度、剛度、及柔軟度。此外,根據本發明的例示性實施例之非織纖維素纖維織物102,可製造成每單位面積的低重量(例如,10至30g/m²)。以此種技術可製造直徑小至(或不超過)5µm,特別是不大於3µm的非常細之長絲。此外,根據本發明的例示性實施例之非織纖維素纖維織物102,可用各種網的美學形成,例如,以平坦的類爽脆膜(crispy film-like)的方式、以類似紙(paper-like)的方式,或以柔軟的類撓性紡織品(soft flexible textile-like)的方式。藉由調整所述製程的製程參數,更可精確地調整非織纖維素纖維織物102的剛度及機械剛性、或可撓性及柔軟度。這可例如藉由調整合併位置的數目、層數、或藉由後處理(諸如針扎、水纏結、及/或壓延)來調整。特別有可能製造具有低至10g/m2 或更低之相對低的基礎重量的非織纖維素纖維織物102,以獲得具有非常小的直徑(例如,低至3至5µm、或更低的)的長絲或纖維108等。   圖2、圖3及圖4顯示根據本發明的例示性實施例之非織纖維素纖維織物102的實驗捕捉影像,其中藉由相應的製程控制完成單根纖維108的合併。圖2至圖4中的卵形標記顯示多個纖維108彼此整體連接的這種合併區域。在這種合併點處,二或更多個纖維108可互連以形成整體結構。   圖5及圖6顯示根據本發明的例示性實施例之非織纖維素纖維織物102的實驗捕捉影像(其中已完成纖維108的膨潤),其中圖5顯示呈乾燥非膨潤狀態的纖維織物102,而圖6顯示呈潮濕膨潤狀態的纖維織物102。可在圖5及圖6的兩種狀態下測量孔洞直徑,並且可互相比較。當計算30次測量的平均值時,藉由纖維108在水介質中的膨潤,可測得孔洞大小減小至其初始直徑的47%。   圖7顯示根據本發明的例示性實施例之非織纖維素纖維織物102的實驗捕捉影像,其中藉由相應的製程設計(亦即,多個紡嘴的連續配置)完成了纖維108的兩個疊置層200、202的形成。在圖7中兩個單獨的但連接的層200、202以水平線表示。例如,可藉由沿機器方向連續配置n個紡嘴或噴射嘴122來製造n層織物102(n≥2)。   以下將更詳細地描述本發明的具體例示性實施例:   圖8顯示示意性繪圖,其將用於解釋當調整纖維108的截面的真圓度以偏離圓形截面時,可促進纖維108的明確彎曲。   為了解釋所述現象,圖8中以直的無力施加(force fee)的狀態(上圖)及纖維108遭受彎曲的狀態(下圖)顯示纖維108。當纖維108具有完美的圓柱形截面時,即使極小的彎曲力也可能引起纖維108沿著非可預測的彎曲軸彎曲。因此,在實際應用中,不可能預測或確定方向,具有完美圓柱形截面的纖維108束將沿著該方向經受彎曲。然而,當纖維108的真圓度顯著偏離一值時(亦即,纖維108的截面偏離真圓,例如形狀為卵形(特別是橢圓形)),從而定義出較佳彎曲軸,沿著該軸可用比在與其垂直方向上更簡單的方式(或用較小的力)實現彎曲。例如,與以較長的長軸作為彎曲線相比,具有較短的短軸作為彎曲線的較小力可使具有卵形-橢圓形截面的纖維108彎曲。   將所述現象應用於根據本發明的例示性實施例之織物102的纖維設計,設計具有圓形截面的這種織物102的纖維108允許可預測地定義纖維108的較佳彎曲軸。當萊賽爾紡絲溶液104的長絲沉積在纖維支撐單元132上以藉由凝聚形成纖維108時,彼等將以可預測的且不僅是統計的方式,沿著纖維支撐單元132的纖維容納表面,以一定程度的順序排列。因此,藉由定義纖維108的截面以偏離圓形對稱幾何,可精確地定義織物102的機械性質。因此,由於纖維108之顯著的非圓形真圓度的定義,可在非織纖維素纖維織物102中引入可預測性。最後,藉由製造製程的相應調整,調整根據本發明的例示性實施例之非織纖維素纖維織物102的至少一些纖維108與圓柱形幾何的偏差,允許精確地定義織物102的機械性質,特別是允許獲得具有高機械強度的織物102。   圖9顯示根據本發明的例示性實施例之非織纖維素纖維織物102的實驗捕捉影像,繪示出具有偏離圓形的截面形狀之纖維108。   較佳地,沿著至少部分的纖維108縱向延伸,至少10%的纖維108具有不大於50%的真圓度之非圓形截面形狀。由於纖維108的顯著子集與圓柱形幾何的這種強烈偏差,可在織物102中定義一定程度的規則性。這允許微調所獲得的織物102的機械性質。在非織標準WSP90.3的基礎上,用「織物手感測試儀」測量的織物102的光滑度可在2mNm2 /g與70mNm2 /g之間的寬範圍內自由調整,因為藉由至少一些纖維108的非圓形真圓度設計,可精確地定義所期望的機械強度。   由於上述參考圖1之織物102的製造製程,纖維108僅具有小於5ppm之非常小的銅含量及/或僅具有小於2ppm之非常小的鎳含量。因此,可製造具有非常小的重金屬污染物之織物102,確保織物102的生物相容性並且當織物102與人體皮膚物理接觸時防止過敏反應。   圖10顯示根據本發明的例示性實施例之非織纖維素纖維織物102的實驗捕捉影像,其中具有偏離圓形的截面形狀之纖維108是經部分加撚的。   在圖10的實施例中,一些纖維108是經加撚的。因此,這些纖維108沿其至少部分的縱向延伸,形成略微螺旋的結構。這種纖維加撚使得到的非織纖維素纖維織物102具有機械強度,同時允許織物100的一些彈性調整。具體而言,具有偏離一的真圓度、經加撚、並在合併位置204處彼此合併之纖維108的組合為織物102提供了某種程度的可撓性。   圖11顯示根據本發明的另一例示性實施例之非織纖維素纖維織物102的實驗捕捉影像,由三個具有不同纖維108的直徑的堆疊層202、200、200組成。根據圖11,中間夾層200具有比上方及下方的兩個外層200、202顯著更小的纖維108的直徑。   圖11中顯示的多層織物102特別適用於諸如醫療應用、農業紡織品等的應用。例如,活性物質可儲存在內層200中,其顯示出高毛細管作用。外層200、202可根據剛性及表面觸覺來設計。這對於清潔及醫療應用是有利的。對於農業應用,纖維層設計可根據蒸發性質及/或根部滲透而特別地配置。   在另一個應用中,圖11中顯示的多層織物102可用作面膜,其中中間層200可具有特別顯著的流體保持能力。覆蓋層200、202可經配置以用於調整流體釋放性質。各層200、200、202的纖維108的直徑可用作用於調整這些功能的設計參數。   因此,在圖11中顯示的纖維108位於三種不同的可分辨之層200、202中。不同的層200、202之纖維108在層200、202之間的合併位置204處整體合併。再者,至少一些纖維108設置有具有不大於90%的真圓度之非圓形截面,其在各層200、202中提供一定程度的順序,並強化織物102。   圖12顯示根據本發明的例示性實施例,如何計算具有偏離圓形截面的截面之纖維108的真圓度的值作為纖維108的截面之內切圓280與外接圓282的半徑之間的比值。   最小外接圓282定義為包圍圖12中所繪示的纖維108之截面的整個真圓度輪廓的最小圓。最大內切圓280定義為內切圖12中所繪示的纖維108之截面的整個真圓度輪廓的最大圓。在本申請案的上下文中,真圓度可定義為內切圓280的半徑r除以外接表面282的半徑R之間的比值。真圓度可由所得百分比值表示。在本實例中,R≈2r及纖維108的真圓度因此是約0.5或50%。為了比較,圓柱形纖維108滿足條件R=r,並且真圓度為1或100%。   圖13根據本發明的例示性實施例,繪示用於製造非織纖維素纖維織物102之裝置100的一部分,該非織纖維素纖維織物是由無末端纖維素纖維108之兩個堆疊的層200、202所組成。鑑於輸送帶式纖維支撐單元132的可移動纖維容納表面,圖13左手側的上游噴射嘴122產生纖維108之層202。其他纖維108的層200是由下游噴射嘴122產生(在圖13的右手側)並且附接至先前形成的層202的上主表面,從而獲得織物102的雙層200、202。   根據圖13,控制單元140(控制噴射嘴122及凝聚單元128)經配置以用於調整製程參數,使得至少部分的纖維108在層200、202之間的合併位置204處整體合併。   儘管未在圖13中示出,但是例如藉由水纏結、針扎、及/或含浸,可在收集到纖維支撐單元132上之後進一步加工纖維108。   又參考圖13中所繪示的實施例,可提供一或多個另外的噴嘴桿或噴射嘴122,並且可沿著纖維支撐單元132的輸送方向連續配置。可配置多個噴射嘴122使得纖維108的另外的層200可沉積在先前形成的層202的頂部上(較佳地在層202及/或層200的纖維108的凝聚或固化製程完全完成之前),其可觸發合併。當適當地調整製程參數時,這可能在多層織物102的性質方面具有有利的效果:   可觸發根據圖13之織物102的纖維108之間的意欲合併,以便進一步增加織物102的機械穩定性。在此上下文中,合併可以是接觸纖維108的長絲之支撐接觸點黏附,特別是在完成一或兩個纖維108的凝聚製程之前經合併。例如,可藉由流體流(例如,氣流或水流)增加待合併的萊賽爾紡絲溶液104的兩個長絲之間的接觸壓力來促進合併。藉由採取這種措施,一方面可增加層200、202之一者的不同長絲或纖維108之間的黏附,及/或另一方面可增加層200、202之間的黏附。   根據圖13的裝置100(其經配置以用於製造多層織物102),實施大量的製程參數,這些參數可用於調整合併因子、設計纖維108以及纖維層200、202的形狀及/或直徑、或直徑分佈。這是多個噴射嘴122的連續配置的結果,各噴射嘴122可用可單獨調整的製程參數操作。當多個噴射嘴122的孔口126不同地且以非圓形方式成形時,亦可形成具有偏離圓的截面之纖維108的織物102。這種纖維108可以是卵形、橢圓形、長方形、三角形、多邊形,具有尖銳的及/或圓形的邊緣等。   對於根據圖13的裝置100,特別可製造由至少兩層200、202(較佳地大於兩層)組成的織物102。藉由多層織物102之明確的層分離,稍後也可將多層織物102分成不同的個別層200、202或不同的多層部分。根據本發明的例示性實施例,一層200、202的纖維108的層內黏附以及相鄰層200、202之間的纖維108的層間黏附(例如藉由合併及/或藉由摩擦產生接觸)可適當地且單獨地調整。當調整製程參數使得當纖維108的一層200放置在其頂部時,已經完成另一層202的纖維108的凝聚或固化,可特別地獲得對於各單獨的層200、202相應的單獨控制。   例如,根據圖13調整用於調整合併的製程參數,包含沿著可移動纖維支撐單元132連續配置具有孔口126的多個噴射嘴122,在纖維支撐單元132上沉積纖維108的第一層202,以及在層200、202之間的界面處所有纖維108已經完成凝聚之前,在第一層202上沉積纖維108的第二層200。因此,織物102的纖維108之不同者可位於不同的可分辨之層200、202中,然而可藉由形成合併位置204來將其合併。換言之,不同的層200、202之纖維108可在層200、202之間的一或多個合併位置204處整體合併。   圖14根據本發明的又另一例示性實施例,繪示用於製造非織纖維素纖維織物102之裝置100的部件,其中藉由控制單元140來控制製程以觸發具有偏離圓形真圓度(藉由在凝聚期間向纖維108施加橫向力)的真圓度的纖維108之間合併位置的形成。   更具體地,紡絲溶液變形單元270設置在裝置100中,該裝置100經配置成在凝聚完成之前向萊賽爾紡絲溶液104的長絲施加變形力。這種變形力可使長絲從圓形截面變形成非圓形截面。從細節274可看出,顯示出纖維108的凝聚完成之前織物102的一部分,在凝聚完成之前藉由將成形流體流272引導至萊賽爾紡絲溶液104的長絲來施加溶液變形力。成形流體272可以是氣流及/或液流,在纖維108從其中沉澱之前,將成形流體從紡絲溶液變形單元270引導至萊賽爾紡絲溶液104的長絲。由成形流體272施加至萊賽爾紡絲溶液104的長絲上的壓力,使長絲從例如時質上圓形的截面形狀變形成橢圓形或扁平形狀,如細節274所示。當成形流體272施加到萊賽爾紡絲溶液104的長絲上的壓力保持到凝聚或沉澱完成時,纖維108將自動形成具有非圓形截面的相應形狀。當成形流體272包含水或由水組成時,成形壓力的施加可與來自萊賽爾紡絲溶液104的纖維108的凝聚的沉澱協同地合併,所述合併至少部分地由隨後的水性成形流體272觸發。   圖15根據本發明的又另一例示性實施例,繪示用於製造非織纖維素纖維織物102之裝置100的部件,該部件具有孔口126,該孔口126被塑形以形成具有偏離圓形真圓度之真圓度的纖維108。   附加地或替代地根據圖14所採用的規則,用於確定織物102的至少部分的纖維108小於1的真圓度,圖15的噴射嘴122的孔口126設置有非圓形形狀。在所示的實施例中,預見到交替列的橢圓形孔口126,其具有各自的主軸,或者沿著共同的對準軸236(亦即,根據圖15的水平方向,比較奇數列的孔口126)定向,或者沿著平行的對準軸238(亦即,根據圖15的垂直方向,比較偶數列的孔口126)而定向。然而,所屬技術領域中具有通常知識將清楚地理解,所示的孔口126的圖案僅是例示性的,並且根據本發明的其他例示性實施例可實施許多其他圖案的非圓形孔口126。   圖16顯示根據本發明的例示性實施例之非織纖維素纖維織物102的示意圖,繪示出具有偏離圓形的截面形狀之纖維108,結果,纖維108大致上沿著優先方向290配置或排列。換言之,纖維108在織物102內經各向異性地排列從而大致上界定出一個優先排列方向290,相較於其他方向,較大部分的纖維108沿著該優先排列方向排列。根據圖16,顯示出織物102的數個纖維108,其全部具有非圓形的橢圓形截面。因此,當纖維108沉積在纖維支撐單元132上時,纖維108較佳地圍繞排列方向290彎曲。從圖16可看出,一些纖維108在凝聚之前在合併位置204處合併,而其他纖維108在交叉位置264處彼此交叉而不合併,亦即,僅經歷相互的摩擦力。   更一般地,提供具有非圓形無末端纖維108的非織纖維素纖維織物102使得剛性及均勻性增加。儘管根據其中一個纖維108沉積在纖維支撐單元132上的每個個別製程具有統計性影響,但是可藉由以非圓形截面配置至少部分的纖維108來定義纖維108的可預測較佳的沉積方向。藉由以足夠小的真圓度製造至少部分的纖維108,可獲得均勻性及剛性中的至少一者的相應增加。當同時觸發至少部分的纖維108之間的合併時,這對於增加織物102的穩定性特別有力。在真圓度值或截面形狀方面,藉由調整根據本發明的例示性實施例之織物102的纖維108的性質,使織物102相對於特定應用的功能化變得可能。具體而言,這使得可在給定的克重(grammage)下設計具有更高機械強度的織物102,或者在給定的機械強度下獲得更低的克重。可在織物102的對應於纖維支撐單元132的纖維容納平面的平面中,一或兩個垂直方向上獲得這種強化的機械穩定性。非常有利地,根據本發明的例示性實施例,可根據萊賽爾紡絲溶液的結構製造這種織物102,從而可保證所獲得的織物102具有非常低污染的重金屬雜質。因此,所獲得的非織纖維素纖維織物102具有非常高的純度,使得所獲得的織物102或基於其製造的產品不易引起使用者的過敏反應。   根據較佳的實施例,實施了用於產生萊賽爾紡絲溶液104的長絲的一或多個噴嘴桿或噴射嘴122,其中這些長絲接著被拉伸、捲曲、並沉積在纖維支撐單元132的纖維容納表面上。在此拉伸製程期間及/或當尚未凝聚的萊賽爾紡絲溶液104的長絲沉積在纖維支撐單元132上時,可藉由空氣渦度或擾流觸發或促進二或更多個纖維108之間合併位置204的形成。   這種合併製程可在形成無末端纖維108的化學製程的凝聚期間於不同時間點發生。彼等也可以不同的強度進行調整,並且可使用不同的介質(諸如水或空氣)進行促進。藉由相應的調整,可控制長絲的凝聚及/或成形,以及在所述的接觸或合併位置204處的黏附。結果,可調整各式各樣的合併效果:一方面,可形成具有非常低的合併黏附傾向之織物102;另一方面,可控制該製程,從而獲得極強的合併,使得纖維108失去其形狀,並且傾向於呈現類面狀膜結構。   在纖維108或其尚未完全凝聚的預成型體的沉積製程期間,可能涉及統計的或隨機的製程。這通常會導致無末端長絲或纖維108的任意結構。特別是當輸送裝置(亦即,纖維支撐單元132)的傳輸速度明顯小於在纖維支撐單元132的纖維容納表面上向下移動的長絲的速度時,可能會發生纖維108的長絲任意定向。換言之,當長絲在纖維支撐單元132上向下移動時,由於從纖維支撐單元132施加到長絲的反作用力,可能發生長絲或纖維108的非可預測的或偽隨機沉積方向。以上已經參考圖8描述了此現象。   然而,如以上參考圖8所述,藉由以符合具有90%或更低的真圓度值的非圓形截面配置至少部分的纖維108,本發明的例示性實施例可克服纖維108的隨機沉積行為的這種純粹統計。當纖維108從圓柱形截面偏離到足夠的程度時,可定義纖維108的一或多個主要沉積方向或者用於相應設計及定向的纖維組108,從而增加織物102的均勻性及特性的可預測性。描述性地說並且指的是纖維108的橢圓形截面,這種橢圓形纖維108較佳地會在較小的截面維度的方向上(亦即,沿著橢圓的短軸)向下彎曲或扭結。由於這種現象,對製造的纖維108的截面形狀的控制偏離圓形形狀,允許定義織物102中的纖維108之一個或多個優先排列方向。   為了產生低於90%、較佳是低於50%之真圓度的纖維108,可用例如吹氣或產生水刀(water jet)的方式,對纖維108之尚未凝聚的預成型體施加壓力。也可將這種壓力施加到纖維108之預成型體的兩個相對表面上,以使纖維變平。例如,當從0°及180°的方向施加壓力時,纖維108之較佳的扁平化或卵形化(ovalization)沿著90°至270°軸發生。   為了產生低於90%、較佳是低於50%之真圓度的纖維108,附加地或替代地,可提供具有卵形(或更普遍地非圓形)噴嘴截面之噴射嘴122的孔口126。   在所述用於形成具有非圓形截面的纖維108之機構的框架中,可應用下列一或多個選項:   a)在纖維支撐單元132的高傳輸速度下,織物102在MD方向上的輸送導致平均纖維排列的隱含聚焦(可從傳輸速度與沈積向量相加得到)。特別是當傳輸速度與沉積速度處於相同的數量級或甚至更大時,可實現織物102在MD方向上的纖維排列的有效定向。與圓形截面相比,由於纖維108的截面拉伸或扁平化修改,在CD方向上對沉積的纖維108進行定義的橫截面控制,並且在傳輸速度為零時可得到在CD方向上增加的纖維定向。因此,可測定傳輸速度下的平均值或中間值以及CD沉積增強,在該增強處沒有獲得纖維108的優先排列方向。換言之,在這樣的條件下,甚至可獲得完美的均勻性。然而,應該提到的是,在一些實施例中,沉積速度可比傳輸速度更高,特別是數量級的高。   b)目前認為,根據a)中描述的原理已經對相對較少數目的纖維108進行修改,得到更鄰近的纖維108也較佳地在CD方向上定向。這可用暴風雨中的森林之類比(analogy)來解釋。斷裂的第一棵樹觸發了沿著斷裂方向的類多米諾骨牌(domino-like)森林通道。   c)藉由修改纖維108的截面形狀,可在織物102中產生根據本發明的例示性實施例之基於摩擦的夾緊效果。這導致像錐形工具容器中那樣的自抑制(self-inhibition)。與圓形截面相比,纖維108的截面形狀的偏差相對較小,已經可獲得這種效果。圓形截面到卵形橫截面的過渡能夠形成相對於另一個纖維108(也具有非圓形截面或具有圓形截面)的這種自抑制系統。   又參考圖13中所繪示的實施例,可提供一或多個另外的噴嘴桿或噴射嘴122,並且可沿著纖維支撐單元132的輸送方向連續配置。可配置多個噴射嘴122使得纖維108的另外的層200可沉積在先前形成的層202的頂部上(較佳地在層202及/或層200的纖維108的凝聚或固化製程完全完成之前),其可觸發層間合併。當適當地調整製程參數時,這可能在多層織物102的性質方面具有有利的效果:   一方面,第一沉積層202可沉積在作為纖維支撐單元132的傳送帶(諸如輸送帶)上。在這樣的實施例中,纖維支撐單元132可實施為釋放機構及空氣抽吸開口(未示出)的有序結構。在纖維108的長絲的統計分佈中,這可能具有在沒有氣流存在的區域中可發現更高的材料濃度的效果。這種(特別是微觀的)材料密度變化可認為是從機械角度來看的穿孔,其作用是非織纖維素纖維織物102的均勻性扭曲(特別是由於其抑制圖案的傾向)。在氣流或液體流(例如水)穿透非織纖維素纖維織物102的位置處,可在非織纖維素纖維織物102中形成孔洞。藉由這種流體流(其中流體可以是氣體或液體),可增加所製造的非織纖維素纖維織物102的拉伸強度。不希望受到特定理論的束縛,目前據信第二層200可認為是第一層202的增強層,其補償了層202的均勻性降低。此機械穩定性的提高可藉由纖維直徑變化(特別是單根纖維108的纖維間直徑變化及/或纖維內縱向直徑變化)進一步改善。當施加更深的(特別是單點)壓力(例如由空氣或水提供)時,纖維108的截面形狀可進一步刻意地扭曲,其可有利地導致進一步增加的機械穩定性。   另一方面,可觸發根據圖13之織物102的纖維108之間的意欲合併,以便進一步增加織物102的機械穩定性。在此上下文中,合併可以是接觸纖維108的長絲的支撐接觸點黏附,特別是在完成一或兩個纖維108的凝聚製程之前經合併。例如,可藉由流體流(例如,氣流或水流)增加接觸壓力來促進合併。藉由採取這種措施,一方面可增加層200、202之一者的長絲或纖維108之間的凝聚強度,及/或另一方面可增加層200、202之間的凝聚強度。   根據圖13的裝置100(其經配置以用於製造多層織物102),實施大量的製程參數,這些參數可用於設計纖維108以及纖維層200、202的形狀及/或直徑、或直徑分佈。這是多個噴射嘴122的連續配置的結果,各噴射嘴122可用可單獨調整的製程參數操作。   根據本發明的例示性實施例之織物102的高機械強度,亦由所述製造製程的下列性質得到:首先,使用由纖維素材料製成的無末端纖維108,因為無末端纖維108(與短纖維相比)具有較少的干擾過渡,使得單根纖維108具有較高的承載能力。其次,可製造高度純淨的這種纖維108,因為相應織物102之與製程相關的重金屬含量非常小。第三,支撐可在水刺製造方法中實施的網或其他載體結構(網支撐系統)的載體塵格的特定設計,允許控制織物102的剛性。具體而言,可藉由(例如空氣及/或水誘導的)合併而顯著增加織物102的穩定性,從而允許獲得具有高負載能力的類仿生結構。   藉由適當的製程控制,可為單根長絲提供鑽頭,該鑽頭也可保持在容易製造的織物102中。由此,可形成加撚纖維108,其可藉由相應的彈簧效應而具有增加的拉伸性。同時,可限制包含加撚纖維108的織物102的彈性。這可用於進一步增加織物102的穩定性。特別是在纖維108彎曲時,具有隨著彎曲半徑增加而彈性降低的效果。當實施適當的氣流渦度或擾流時,可設計具有進一步增加的穩定性之加撚纖維108的織物102。   在纖維支撐單元132的光滑平坦的纖維容納表面上,卵形纖維108或長絲較佳地在其寬邊上停留。這對所製造的織物102的性質具有強烈的影響,因為這涉及有序效果。具體而言,這允許製造具有相對小的厚度及相對高的密度的織物102。   較佳地,根據本發明的例示性實施例之織物102,是由圓形纖維108及非圓形纖維108二者組成。可藉由使用具有圓形及非圓形孔口126的混合噴射嘴122,及/或藉由製程參數的永久、循環、或重複修改來製造相應的織物102。   在本發明的例示性實施例中,可實施至少2個、特別是至少3個、更特別是至少4個、特別是多達10個連續配置的噴射嘴122,以用於製造織物102。各噴射嘴122可包含多個孔口126。各噴射嘴122可選擇性地具有圓形及/或非圓形孔126。   藉由調整萊賽爾紡絲溶液104的長絲的凝聚及/或拉伸條件,還可製造織物102,其中在剖面圖中非圓形纖維部分垂直於或至少實質上垂直於織物102的表面而經定向。這導致織物102的穩定黏附及固化。   這允許獲得一或多個下列優點:以相對低的克重製造高鬆散織物102;具有可調整性質輪廓的可識別層結構;織物102在上主表面及下主表面上的可調整性質;水平排列的卵形纖維108允許在減小的縱向及橫向伸度下獲得高拉伸強度;可在很寬的範圍內調整克重,例如,8g/m2 至250g/m2 。   在本發明的另一例示性實施例中,非織纖維素纖維織物102用於可生物降解的產品。在生物降解後,沒有黏合劑材料或黏著劑材料殘留。具體而言,沒有大量的重金屬形成這種可生物降解的產品的部件。藉由相應製程設計,可防止來自織物102的非所欲微粒磨損。   根據本發明的例示性實施例,可以這樣的方式獲得與無末端纖維108的圓形截面的定義偏差,使得截面形狀沿著這種纖維108的縱向延伸變化。這也可藉由將纖維108彎曲超過其彈性極限來實現,從而發生從彈性彎曲狀態到塑性彎曲狀態的過渡。藉由隨後固定彎曲的纖維108(例如藉由水纏結)可強化這種效果。當撕裂非織纖維素纖維織物102時,其結果是在某些環或梭眼結構處,在撕裂期間引導另一個無末端纖維108透過該結構,直徑不再適合且在小的形狀變化時已經產生自抑制。這增加織物102整體的撕裂強度。這在無末端纖維108的實施方面是特別相關的,其中這種藉由真圓度與一個纖維的偏差所促進的自抑制效果比短纖維更強。   非常有利地,纖維108的截面與圓形截面的偏差可與纖維直徑變化(特別是纖維內厚度變化及/或纖維間厚度變化)合併。此合併使織物102的機械穩定性獲得特別顯著的增加。   總之,根據本發明的例示性實施例尤其可進行下列調整中的一或多者:   - 低均勻纖維直徑可獲得織物102的高光滑度   - 具有低直徑纖維及相對小的速度的多層織物102可允許以低織物密度獲得高織物厚度(caliper)   - 功能化層的等吸收曲線可允許獲得均勻的濕度及流體容納行為,以及在流體釋放方面的均勻行為   - 也可使單層200、202不同地功能化,從而獲得具有異向性性質的產品(例如,用於芯吸、油容納、水容納、除塵力、粗糙度)。   最後,應注意上述實施例在說明而非限制本發明,並且所屬技術領域中具有通常知識者將能夠設計許多替代實施例,而不脫離由所附申請專利範圍所定義的本發明之範籌。在申請專利範圍中,括號中的任何參考符號不應解釋為限制申請專利範圍的範疇。詞語「包含(comprising)」及「包含(comprises)」等,不排除除了在任何申請專利範圍或說明書中作為整體列出的元件或步驟之外的元件或步驟的存在。元件的單數參考不排除這類元件的複數參考,反之亦然。在列舉了若干方法的設備申請專利範圍中,這些方法中的若干個可藉由同一個軟體或硬體項目來實施。在相互不同的申請專利範圍附屬項中敘述某些措施的純粹事實,並不表示這些措施的組合不能使用以獲益。   以下,在下表中描述並顯示用於產生合併因子變化的實例。當使用恆定紡絲溶液(亦即,具有恆定稠度的紡絲溶液)特別是萊賽爾紡絲溶液及恆定氣流(例如空氣通過量)時,纖維素纖維織物中的不同合併因子可藉由改變凝聚噴霧流來實現。因此,可觀察到凝聚噴霧流與合併因子之間的關係,亦即,合併行為的趨勢(凝聚噴霧流越高,合併因子越低)。MD在此表示機器方向,並且CD表示橫向。柔軟度(由已知的具體手感測量技術描述,在非織標準WSP90.3的基礎上,用所謂的「織物手感測試儀」測量,特別是在本專利申請案優先權日有效的最新版本)將依循上述的合併趨勢。強度(以Fmax描述)(例如分別根據EN29073-3及ISO9073-3,特別是在本專利申請案優先權日有效的最新版本)也會依循所述的合併趨勢。因此,所得非織纖維素纖維織物的柔軟度及強度可根據合併的程度(如合併因子所規定)調整。Hereinafter, additional exemplary embodiments of nonwoven cellulosic fiber fabrics, methods of making nonwoven cellulosic fiber fabrics, devices, products or composites for making nonwoven cellulosic fiber fabrics, and methods of use are described. In an embodiment, at least 3%, in particular at least 5%, more particularly at least 10% of the fibers have a non-circular cross-sectional shape of no more than 90% roundness. Even more specifically, it is possible that at least 10%, at least 20%, at least 30%, at least 50%, or at least 80% of the fibers have no more than 90%, no more than 80%, no more than 70%, no more than 60%, no A non-circular cross-sectional shape of greater than 50%, or no more than 30% roundness. The higher the amount of fiber deviating from the circular cross-sectional shape, the higher the deviation of the manufactured fiber fabric from the isotropic mechanical behavior, and the more remarkable the adjustability of the mechanical properties of the fabric. In an embodiment, at least 1%, at least 10%, at least 20%, at least 30%, at least 50%, or at least 80% of the fibers have no more than 80%, in particular no more than 70%, more particularly no more than 50 The non-circular cross-sectional shape of % roundness. Even more specifically, it is possible that at least 1% of the fibers have a non-circular cross-sectional shape of no more than 60%, no more than 50%, no more than 40%, or no more than 10% roundness. The higher the amount of fiber deviating from at least a portion of the circular cross-sectional shape, the higher the deviation of the manufactured fiber fabric from the isotropic mechanical behavior, and the more remarkable the adjustability of the mechanical properties of the fabric. For example, by adjusting the number and/or shape of the orifices, the percentage of fibers having a non-circular cross-sectional shape having a corresponding roundness value can be adjusted, through which the lyocell spinning solution is shot, the lyocell spinning The silk solution forms fibers after agglomeration. Additionally or alternatively, the non-circular shape having the corresponding true roundness value can be adjusted, for example by adjusting the number of filaments of the lyocell spinning solution which is subjected to mechanical impact for changing the cross-sectional shape prior to coagulation. The percentage of fiber in the cross-sectional shape. In the embodiment, on the basis of the non-woven standard WSP90.3, the smoothness and specific hand feeling of the fabric were measured at 2 mNm by "Handle-O-Meter". 2 /g and 70mNm 2 The range between /g. By varying the process parameters of the manufacturing process, the smoothness can thus be varied over a wide range. When designing fibers having a non-circular cross section or a non-cylindrical geometry, sufficient and unambiguous stability of the fabric may have been ensured. The smoothness of the surface (even very high smoothness) can then be freely adjusted without the stability of the fabric being compromised. Based on the non-woven standard WSP90.3, the smoothness of the fabric mentioned can be measured using a "fabric hand tester" (commercially available from Thwing-Albert Instrument Co., Philadelphia, PA). To determine the smoothness of the fabric, the pivot arm of the "Fabric Hand Tester" was lowered and a sample of the fabric (eg, having a square dimension of 10 cm x 10 cm) was pressed into the adjustable parallel slit. The force required to press the sample into the slit is measured. During this procedure, bending and friction are applied to the sample. The measured average value in the CD direction and the MD direction corresponds to the average force required to press the sample through the slit. Average force (for example expressed in mN) and the basis weight of the fabric (for example in g/m 2 The ratio between the expressed) gives the smoothness value (measured as a specific hand) to mNm 2 /g indicates that it represents the smoothness of the fabric material. In an embodiment, the fibers have a copper content of less than 5 ppm and/or have a nickel content of less than 2 ppm. The ppm values mentioned in this application are all about mass (rather than volume). In addition, heavy metal contamination of fibers or fabrics may not exceed 10 ppm for individual chemical elements. Due to the use of lyocell spinning solution as the basis for the formation of endless fiber-based fabrics (especially when referring to solvents such as N-methyl-morpholine N-oxide; NMMO), the fabric has heavy metals such as copper or nickel ( The contamination that may cause an allergic reaction to the user may remain very small. Due to the concept of directly merging fibers under certain conditions that can be adjusted by process control, no additional materials (such as glue or the like) need to be introduced in the process for interconnecting the fibers. This makes the contamination of the fabric very low. In an embodiment, at least a portion (particularly at least 10%, more particularly at least 20%) of the fibers are integrally combined at the merged location. In the context of this application, the term "merging" may specifically denote the integral interconnection of different fibers at each of the combined locations, which results in the formation of an integrally joined fibrous structure comprised of previously separated fibrous preforms. Combining can be expressed as establishing a fiber-fiber bond during the agglomeration of one, some, or all of the combined fibers. The interconnected fibers can be strongly bonded to one another at each of the merged locations without the need for different additional materials (e.g., separate adhesives) to form a common structure. Separating the combined fibers may require breaking the fiber network or its components. According to the described embodiment, a nonwoven cellulosic fiber fabric is provided in which some or all of the fibers are integrally joined to each other by merging. The merging can be triggered by corresponding control of the process parameters of the method of making the nonwoven cellulosic fabric. Specifically, the agglomeration of the filaments can be triggered (or at least completed) after the first contact between the filaments of the lyocell spinning solution that is not yet in the solid state of the precipitate. Thus, the interaction between these filaments (when they are still in solution phase, and then or later by coagulation to convert them to a solid phase) allows for proper adjustment of the coalescence characteristics. Consolidation is a powerful parameter that can be used to fine tune the properties of the fabric being manufactured. Specifically, the greater the mechanical stability of the network, the higher the density of the merged locations. It is also possible to adjust areas of high mechanical stability and other areas of low mechanical stability by uneven distribution of the combined positions on the fabric volume. For example, separating the fabric into individual components can be precisely defined locally in a mechanically weak region with a small number of merged locations. In a preferred embodiment, the incorporation of fibers can be triggered by direct contact of the different fiber preforms in direct contact with each other prior to agglomeration in the form of a lyocell spinning solution. By this coacervation process, a single material of the fiber is coprecipitated to form a merged position. In an embodiment, the merged or merged locations are comprised of the same material as the combined fibers. Thus, the combined position can be formed by the cellulosic material produced directly by the agglomeration of the lyocell spinning solution. This not only makes it possible to provide a fiber joining material alone (such as an adhesive or a binder), but also keeps the fabric clean and made of a single material. The formation of fibers having a non-circular cross section and the formation of fibers by combining interconnects can be accomplished by a single common process. The reason for this is the formation of merged positions between fibers (such as merged or merged lines) and the formation of fibers with a deviation from the perfect circular diameter section, both of which can be used in the lyocell spinning solution before the agglomeration is completed. Mechanical force is applied to the filaments to achieve. However, the filaments of the lyocell spinning solution may be mechanically affected while still in the liquid phase. Descriptively, on the one hand, applying mechanical pressure to the filaments of the lyocell spinning solution which is still liquid or viscous (usually present in the presence of a honey-like consistency) promotes the formation of cylindrical filaments (eg ovals (especially Elliptical)) Non-circular cross-sectional shape to reduce roundness. At the same time, the application of such mechanical pressure on the filaments which are still liquid or viscous lyocell spinning solutions and physical contact with each other triggers the formation of a merged position between the fibers upon agglomeration. In an embodiment, the different ones of the fibers are at least partially located in different layers that are distinguishable (i.e., exhibit visible separation or interface regions between the layers). For example, different mechanical properties at the interface between the layers and between the layers can be adjusted by individual adjustments in the true roundness values of the fibers of the layers. More specifically, the fibers of the different layers are integrally joined at at least one merged location between the layers. Thus, different ones of the fibers that are at least partially located in different distinguishable layers (which may or may not be identical with respect to one or more parameters, such as consolidation factors, fiber thickness, etc.) may be integrally joined at at least one merged location . For example, two (or more) different layers of fabric can be formed by continuously aligning two (or more) nozzles having orifices through which the lyocell spinning solution is extruded for use in Coagulation and fiber formation. When such a configuration is combined with a mobile fiber support unit, such as a conveyor belt having a fiber receiving surface, the first layer of fibers is formed on the fiber support unit by the first spray nozzle, and when the mobile fiber support unit reaches the first The second spray nozzle forms a second layer of fibers on the first layer when the nozzles are in position. The process parameters of this method can be adjusted such that merge points are formed between the first layer and the second layer. In particular, the second layer of fibers being formed has not been fully cured or solidified by coacervation, and may, for example, still have a solid state that is still in the liquid lyocell solution phase and is not yet fully cured. The outer skin or surface area. When such pre-fiber structures are in contact with each other and then fully solidified into a solid fiber state, this causes two merged fibers to be formed at the interface between the different layers. The greater the number of merged locations, the higher the interconnect stability between the fabric layers. Therefore, the control combination allows control of the rigidity of the connection between the fabric layers. For example, the consolidation can be controlled by adjusting the degree of cure or agglomeration before the pre-fibrous structure of each layer reaches the fiber support plate on the underlayer or pre-fibrous structure. Unwanted separation of the layers can be prevented by combining the fibers of the different layers at the interface therebetween. In the absence of a merge point between the layers, it is possible to peel one layer of fiber from the other. In accordance with an exemplary embodiment of the present invention, the degree of adhesion between the fibers and/or between the layers can be gradually adjusted between "uncombined fibers or layers" and "fully combined fibers or layers." As a result, partial adhesion, particularly between different layers, can be controlled and adjusted to functionalize the fabric based on the product from which the fabric is made. For example, such (especially multilayer) fabrics can be used to make a package that provides a slight adhesion that allows the packaged product to be properly handled through its weak adhering members. To determine the aforementioned combination factor of the fabric (which may also be expressed as an area combining factor), the following assay procedure can be performed: a square sample of the fabric can be optically analyzed. A circle is drawn around each merged position of the fibers that intersect at least one diagonal of the square sample, the circle having a diameter that must remain entirely inside the square sample. The size of the circle is determined such that the circle encompasses the merged area between the merged fibers. Calculate the arithmetic mean of the diameters of the determined circles. The consolidation factor is calculated as the ratio between the average diameter value of the square sample and the diagonal length, and can be expressed as a percentage. In an embodiment, at least a portion of the fibers are twisted. The twisting of fibers is a more powerful tool for designing fiber networks. For example, twisted fibers can have higher mechanical stability than fully straight fibers. Likewise, the formation of twisted fiber groups (e.g., twisted combined fibers) can significantly improve the mechanical stability of the fabric in a similar manner because the twisted filaments have significantly higher mechanical properties than the corresponding number of single filaments. stability. For example, the twisted fibers can be made by rotating or rotating the filaments of the lyocell spinning solution during the stretching phase (i.e., prior to coagulation or precipitation). In particular, the application of vorticity, i.e., prior to agglomeration, the perturbation around the filaments of the lyocell spinning solution can be used to form twisted fibers. In an embodiment, the fibers are anisotropically aligned within the fabric to substantially define at least one preferential alignment direction, with a larger portion of the fibers being aligned along the at least one preferentially aligned direction than the other directions. In such an embodiment, the set of fibers or all of the fibers of the fabric may be adjusted in fiber shape to deviate from the circular cross-section such that when the fibers are deposited on the fiber support unit, they are substantially or preferably along one or The plurality of major directions are aligned because their preferred bending axes are determined by the deviation of the individual fiber fillets. By taking such measures, a certain degree of order can be introduced into the fabric which results in non-isotripic properties of the fabric being manufactured. In an embodiment, adjusting the process parameters includes applying a force to the filaments of the lyocell spinning solution prior to completion of the agglomeration. Descriptively, when a compressive force is applied to a viscous and thus flowable filament of a lyocell spinning solution prior to conversion to a solid phase, the filament can be deformed, for example, from a cylindrical cross-sectional shape, for example Oval (especially elliptical) cross-sectional shape. The fiber deformation force can be applied in a direction perpendicular to the longitudinal extension of the fiber or fiber portion in the analysis. When the filaments of the lyocell spinning solution are agglomerated while being in this deformed shape, fibers having a roundness of less than 1 are obtained. In an embodiment, the force is applied by directing a forming fluid (which may be a liquid and/or a gas) to the filaments of the lyocell spinning solution prior to completion of the agglomeration. Such a forming fluid may be a forming gas such as air or a forming liquid such as water. When a forming gas is used, a precisely defined mechanical force is applied to the filaments that have not been agglomerated without causing agglomeration. When a forming liquid is used, the precisely defined mechanical force is also suitable for filaments which have not yet agglomerated, while at the same time triggering agglomeration by diluting the lyocell spinning solution with a (particularly aqueous) liquid. In such an embodiment, the deformation and agglomeration can be performed simultaneously. In an embodiment, the pressure increase referred to by the gas or liquid (i.e., fluid) flow can be configured such that each fluid stream is antiparallel at a location with the fibers being formed interposed therebetween. As a result, a local asymmetric pressure increase occurs, which affects the fiber. At the same time, this phenomenon does not further affect the process of making fibers. In an embodiment, at least some of the apertures are non-circular, in particular oval (especially elliptical) or polygonal. Preferably, the openings in the spray plate of the fiber-forming unit defining the orifices may have substantially the same roundness as the fibers consisting of the precipitated lyocell spinning solution ejected through the individual orifices ( Especially the shape of no more than 90%). In one embodiment, the first portion of the aperture has a circular opening and the second portion of the aperture has a non-circular opening. Therefore, the shape design of the orifice also allows to some extent to define the shape of the fiber produced. In an embodiment, the adjustments are used to adjust the combined process parameters, including forming at least a partial merged position after the lyocell spinning solution has exited the orifice and before the lyocell spinning solution reaches the fiber support unit. When moving down, this can be achieved, for example, by triggering the interaction between the strands of the lyocell spinning solution through different orifices by extrusion. For example, the gas flow can be adjusted in terms of strength and direction such that different strands or filaments of the spinning solution (not yet fully agglomerated) are forced to interact with each other in the transverse direction before reaching the fiber support unit. The gas flow can also be operated near or in a turbulent state to promote interaction between the various preforms of the fibers. Thus, prior to agglomeration, the individual preforms of the fibers can contact each other to form a merged location. In an embodiment, adjusting the process parameters for adjusting the combination includes forming at least a partial merged position after the lyocell spinning solution triggers at least a portion of fiber agglomeration upon deposition onto the fiber support unit to the fiber support unit . In such an embodiment, the coacervation procedure can be intentionally delayed (which can be adjusted by the corresponding operation of the agglomeration unit, particularly by adjusting the properties of the coalescing fluid and the supply location accordingly). More specifically, the coacervation procedure can be delayed until the spinning solution has reached the fiber support plate. In such an embodiment, the preform of the fiber is still deposited on the fiber support plate prior to coagulation, thereby again contacting the other preforms of the fiber prior to coagulation. It is thus possible to force the spinning solutions of the different strands or preforms to flow into contact with each other and thereafter only to trigger or complete the agglomeration. Therefore, agglomeration after initial contact between different fiber preforms that are still in a non-agglomerated state is an effective measure for forming a merged position. In an embodiment, adjusting the process parameters for adjusting the combination includes continuously configuring a plurality of spray nozzles having orifices along the movable fiber support unit, depositing a first layer of fibers on the fiber support unit, and between the layers A second layer of fibers is deposited on the first layer before at least a portion of the fibers at the interface have been agglomerated. For each layer to be formed, the process parameters for operating the respective spray nozzles can be adjusted to achieve layer-specific agglomeration behavior. The layer-specific agglomeration behavior of the different layers can be adjusted such that a merged location is formed within the respective layers and preferably between adjacent layers. More specifically, process control can be adjusted by promoting agglomeration of the two layers only after initial contact between the spinning solutions associated with the different layers to form a merged position between the two adjacent layers. In an embodiment, the method further comprises further processing the fibers and/or fabric after collection on the fiber support unit, but preferably still forming the nonwoven cellulosic fiber fabric having the endless fibers in situ. Such an in-situ process can be such that the process is performed prior to the manufacture (especially substantially endless) of the fabric being stored (eg, rolled up by a winder) for transport to a product manufacturing destination. For example, such further processing can involve hydroentanglement. The water entanglement can be expressed as a bonding process of a wet or dry web, and the resulting bonded fabric is a non-woven fabric. Water entanglement can use a fine high pressure water jet that penetrates the web, impacts the fiber support unit (especially the conveyor belt) and bounces, causing the fibers to become entangled. The corresponding compression of the fabric allows the fabric to be more compact and mechanically more stable. In addition to or in addition to hydroentangling, the fibers may be steam treated with pressurized steam. Additionally or alternatively, such further processing or post processing may involve needle punching the fabric being manufactured. The needle stick system can be used to bond fibers of fabric or mesh. As the needle passes through the web, some of the fibers can be forced through the web and the fibers are left as the needle is withdrawn to produce the needle-punched fabric. If sufficient fibers are properly displaced, the web can be converted into a fabric by the consolidation effect of these fiber plungers. Yet another further processing or post-treatment of the web or fabric is an impregnation treatment. Impregnating the network of endless fibers can involve applying one or more chemicals (e.g., softeners, hydrophobic agents, antistatic agents, etc.) to the fabric. Yet another further processing is calendering. Calendering can be expressed as a processing process for treating the fabric, and a calender can be used to smooth, coat, and/or compress the fabric. The nonwoven cellulosic fiber fabric in accordance with an exemplary embodiment of the present invention may also be combined with one or more other materials (e.g., in situ or in a subsequent process) to form a composite in accordance with an illustrative embodiment of the present invention. Exemplary materials that can be combined with the fabric used to form such a composite can be selected from the group consisting of, but not limited to, the following materials or combinations thereof: fluff pulp, fiber suspension, wet-laid nonwoven, Airlaid non-woven fabrics, spunbonded webs, meltblown webs, carded spunlaced webs, or needled webs, or other sheet-like structures made of various materials. In embodiments, the joining between different materials may be by, but not limited to, one or a combination of the following processes: combining, hydroentangling, needling, hydrogen bonding, thermal bonding, bonding through a binder, Fit, and/or calender. In the following, an illustrative advantageous product comprising or using a non-woven cellulosic fiber fabric according to an exemplary embodiment of the invention is summarized: a mesh (100% cellulosic fibrous web, or for example comprising two or more fibers or by two or more a network of multiple fibers, or chemically modified fibers, or with incorporated materials such as antimicrobial materials, ion exchange materials, activated carbon, nanoparticles, lotions, pharmaceutical or flame retardants, or bicomponent fibers. The particular use of the fibers can be as follows: Non-woven cellulosic fabrics according to exemplary embodiments of the present invention can be used to make wipes, such as baby wipes, kitchen wipes, wipes, make-up wipes, sanitary wipes Towels, medical wipes, cleaning wipes, polishing wipes (for cars, furniture), dust wipes, industrial wipes, duster wipes, mop wipes. Non-woven cellulosic fabrics in accordance with exemplary embodiments of the present invention may also be used to make filters. For example, such filters may be air filters, HVAC, air conditioning filters, flue gas filters, liquid filters, coffee filters, tea bags, coffee bags, food filters, water purification filters, blood filters, Cigarette filter, cabin filter, oil filter, cartridge filter, vacuum filter, vacuum cleaner filter bag, dust filter, hydraulic filter, kitchen filter, fan filter, moisture exchange filter, pollen filter, HEVAC/HEPA/ULPA filters, beer filters, milk filters, liquid coolant filters, and juice filters. In yet another embodiment, a non-woven cellulosic fiber fabric can be used to make an absorbent hygiene product. Examples thereof are a collecting layer, a coverstock for health care, an absorbent covering, a distribution layer, a sanitary pad, a facing material, a back sheet, a leg cuff, a rinsable product, a pad, a care pad, a disposable pant, Training pants, face masks, cosmetic masks, make-up pads, towels, diapers, and laundry dryer papers for releasing active ingredients such as textile softeners. In yet another embodiment, a nonwoven cellulosic fiber fabric can be used to make a medical application product. For example, such medical application products can be disposable hats, robes, masks and shoe covers, wound care products, aseptic packaging products, breathable fabric products for health care, dressing materials, one-way garments, dialysis products, nose strips, dental plates Adhesives, disposable underpants, drapes, wraps and wraps, sponges, dressings and wipes, bed fabrics, transdermal drug delivery, shrouds, nursing pads, procedure packs, heating packs, pouch liners, Fixed patch, and incubator pad. In yet another embodiment, a nonwoven cellulosic fiber fabric can be used to make a geotextile. This may involve crop production protection coverings, felting, water purification, irrigation control, asphalt covering, soil stabilization, drainage, sedimentation and erosion control, pond liners, impregnation, drainage liners, ground stabilization, pit lining, Seed blankets, weed control fabrics, greenhouse shades, root bags, and biodegradable plant pots. Non-woven cellulosic fiber fabrics can also be used in vegetable foils (e.g., to provide photoprotection and/or mechanical protection to plants, and/or to provide feces or seeds to plants or soil). In another embodiment, a nonwoven cellulosic fiber fabric can be used to make a garment. For example, linings, garment insulation and protection, handbag components, shoe components, padded, industrial hats/shoes, disposable overalls, clothing and shoe bags, and thermal insulation can be made on the basis of such fabrics. In yet another embodiment, a nonwoven cellulosic fiber fabric can be used to make a product for use in construction technology. For example, such fabrics can be used to make roofing and tile cushions, underslating, insulation and sound insulation, house wrap, gypsum board finishes, pipe cladding, concrete molding layers, foundations And ground stabilization, vertical drainage systems, paving covers, roofing felts, noise reduction, reinforcements, sealing materials, and damping materials (mechanical). In yet another embodiment, the nonwoven cellulosic fiber fabric can be used to make automotive products. Examples are cabin filters, boot pads, racks, heat shields, shelf trims, molded cover liners, shoe covers, oil filters, ceiling liners, rear shelves, upholstery fabrics, airbags, Silencer pads, insulation, car covers, underpadding, car mats, tapes, backings and tufted carpets, seat covers, door trims, needled carpets, and car carpet backings. Another field of application for fabrics made in accordance with exemplary embodiments of the present invention is home furnishings, such as furniture, construction, arm and back insulation, mat thickening, dust covers, cushions, stitching reinforcements, edge trim materials, Bed frame structure, bedding backing, spring cladding, mattress mat assembly, mattress cover, curtain, wall covering, carpet backing, lampshade, mattress assembly, spring insulator, seal, pillow crepe, and bed Pad flower. In yet another embodiment, a nonwoven cellulosic fiber fabric can be used to make an industrial product. This can involve electronics, floppy disk gaskets, cable insulation, abrasives, insulating tapes, conveyor belts, noise absorbing layers, air conditioners, battery separators, acid systems, non-slip felt decontamination machines, food cladding, tape, sausage casings. , cheese casings, artificial leather, booms and socks, and paper felts. Non-woven cellulosic fabrics in accordance with exemplary embodiments of the present invention are also suitable for use in the manufacture of products related to leisure and travel. Examples of such applications are sleeping bags, tents, luggage, handbags, shopping bags, aviation headrests, CD cases, pillow cases, and sandwich packages. Yet another field of application of the exemplary embodiments of the present invention pertains to school and office products. For example, mention should be made of book covers, mailing envelopes, maps, signs and pennants, towels, and flags. The inset in the drawings is schematic. In the different figures, similar or identical elements or features are provided with the same reference numerals. 1 illustrates a device 100 for fabricating a nonwoven cellulosic fabric 102 formed directly from a lyocell spinning solution 104, in accordance with an illustrative embodiment of the present invention. The lyocell spinning solution 104 is at least partially agglomerated by a coalescing fluid 106 to be converted to partially formed cellulosic fibers 108. By the apparatus 100, a lyocell solution spray spinning method according to an exemplary embodiment of the present invention can be performed. In the context of the present application, the term "Lysel solution spinning" may specifically encompass a method of obtaining discrete lengths of substantially endless filaments or fibers 108, or obtaining discrete lengths of endless filaments and fibers. . As further described below, in accordance with an exemplary embodiment of the present invention, nozzles each having an orifice 126 through which a cellulose solution or lyocell spinning solution 104 is passed along with a gas stream or gas flow 146 are provided. Sprayed for use in the manufacture of nonwoven cellulosic fabric 102. As can be seen from FIG. 1, the wood pulp 110, other cellulose-based raw materials, and the like can be supplied to the storage tank 114 via the metering unit 113. Water from the water container 112 is also supplied to the reservoir 114 via the metering unit 113. Thus, metering unit 113 may define the relative amount of water and wood pulp 110 to be supplied to storage tank 114 under the control of control unit 140, described in further detail below. The solvent (such as N-methyl-morpholine N-oxide; NMMO) contained in the solvent container 116 can be concentrated in the concentration unit 118, and then in the mixing unit 119 with water and wood pulp 110, or other cellulose. The mixture of materials of the system is mixed in a determinable relative amount. The mixing unit 119 can also be controlled by the control unit 140. Therefore, the water-wood pulp 110 medium is dissolved in the concentrated solvent of the dissolution unit 120 in an adjustable relative amount, thereby obtaining the lyocell spinning solution 104. The aqueous lyocell spinning solution 104 may be a honey viscous medium composed of cellulose (for example, 5 mass% to 15 mass%) containing wood pulp 110 and a solvent (for example, 85% by mass to 95% by mass). The lyocell spinning solution 104 is sent to a fiber forming unit 124 (which may be implemented as or may include a plurality of spinning bundles or spray nozzles 122). For example, the number of orifices 126 of the spray nozzle 122 can be greater than 50, particularly greater than 100. In one embodiment, all of the apertures 126 of the fiber forming unit 124 (which may include a plurality of spouts or spray nozzles 122) may have the same size and/or shape. Alternatively, the size and/or shape of the apertures 126 of the different apertures 126 of one spray nozzle 122 and/or different spray nozzles 122 (which may be continuously configured for forming a multilayer fabric) may be different. When the lyocell spinning solution 104 passes through the orifice 126 of the spray nozzle 122, it is divided into a plurality of parallel lyocell spinning solutions 104 strands. The vertically oriented gas flow (i.e., oriented substantially parallel to the spinning direction) forces the lyocell spinning solution 104 to be converted into increasingly longer and thinner strands, under the control of the control unit 140 Change process conditions to adjust stocks. The gas stream can accelerate the lyocell spinning solution 104 along at least a portion of its path from the orifice 126 to the fiber support unit 132. The long and thin strands of the lyocell spinning solution 104 interact with the non-solvent agglomerating fluid 106 as the lyocell spinning solution 104 moves through the spray nozzle 122 and further down. The coalescing fluid 106 is advantageously implemented as a vapor mist, such as a water mist. The process-related properties of the coalescing fluid 106 are controlled by one or more coalescing units 128 to provide tunable properties to the coalescing fluid 106. The agglomeration unit 128 is sequentially controlled by the control unit 140. Preferably, each agglomeration unit 128 is disposed between each nozzle or orifice 126 for individually adjusting the properties of the layers of fabric 102 being produced. Preferably, each spray nozzle 122 can have two configured agglomeration units 128, one on each side. The individual spray nozzles 122 can thus be provided with individual portions of the lyocell spinning solution 104, which can also be tailored to different controllable properties of the fabric 102 having different layers. When interacting with the coalescing fluid 106 (e.g., water), the solvent concentration of the lyocell spinning solution 104 is reduced such that the agglomerated fluid cellulose, such as wood pulp 110 (or other material), at least partially coalesces into long and thin Cellulose fibers 108 (which may still contain residual solvent and water). During or after the initial formation of the individual cellulose fibers 108 from the extruded lyocell spinning solution 104, the cellulose fibers 108 are deposited on the fiber support unit 132, which is here embodied as having a planar fiber receiving surface. conveyor. Cellulose fibers 108 form a nonwoven cellulosic fabric 102 (shown only schematically in Figure 1). The nonwoven cellulosic fabric 102 is comprised of continuous and substantially endless filaments or fibers 108. Although not shown in FIG. 1, the solvent of the lyocell spinning solution 104 which is agglomerated by the agglomeration unit 128 and washed in the washing unit 180 can be at least partially recovered. When transported along the fiber support unit 132, the nonwoven cellulosic fabric 102 can be washed by the washing unit 180 that supplies the washing liquid to remove residual solvent, which can then be dried. The further processing can be further processed by any further advantageous processing unit 134. For example, such further processing can involve hydroentanglement, needle sticking, impregnation, steam treatment with pressurized steam, calendering, and the like. The fiber support unit 132 can also transport the nonwoven cellulosic fabric 102 to the coiler 136, which can be collected onto the coiler 136 as a substantially endless sheet. The nonwoven cellulosic fibrous web 102 can then be shipped as a roll-good to an entity that produces a product based on the nonwoven cellulosic fabric 102, such as a wipe or textile. As shown in FIG. 1, the process can be controlled by a control unit 140, such as a processor, a portion of a processor, or a plurality of processors. Control unit 140 is configured for controlling the operation of the various units shown in FIG. 1, particularly one or more metering units 113, mixing unit 119, fiber forming unit 124, agglomeration unit(s) 128, further processing unit 134 The dissolution unit 120, the washing unit 180, and the like. Thus, control unit 140 can accurately and flexibly define process parameters (eg, by executing computer executable code, and/or by executing user-defined control commands), and manufacturing non-woven cellulose based on the process parameters Fiber fabric 102. The design parameters in this context are the gas flow along the orifice 126, the nature of the coalescing fluid 106, the drive speed of the fiber support unit 132, the composition of the lyocell spinning solution 104, temperature and/or pressure, and the like. Additional design parameters (the parameters are adjustable for adjusting the properties of the nonwoven cellulosic fabric 102) are the number of orifices 126, and/or mutual distance, and/or geometric configuration, the lyocell spinning solution. The chemical composition and concentration of 104. Therefore, the properties of the nonwoven cellulose fiber fabric 102 can be appropriately adjusted as described below. Such adjustable properties (see detailed description below) may relate to one or more of the following properties: diameter and/or diameter distribution of fibers 108, combined amounts and/or regions between fibers 108, purity levels of fibers 108, The properties of the multilayer fabric 102, the optical properties of the fabric 102, the fluid retention and/or fluid release properties of the fabric 102, the mechanical stability of the fabric 102, the smoothness of the surface of the fabric 102, the cross-sectional shape of the fibers 108, and the like. Although not shown, each of the spinning nozzles 122 may include a polymer solution inlet through which the lyocell spinning solution 104 is supplied to the spray nozzle 122. Gas stream 146 can be applied to lyocell spinning solution 104 via an air inlet. Starting from the interaction chamber inside the spray nozzle 122 and defined by the spray nozzle housing, the lyocell spinning solution 104 is moved or accelerated downward through each orifice 126 (the lyocell spinning solution 104 is pulled down by the gas stream 146) And laterally shrinking under the influence of gas stream 146 such that as the lyocell spinning solution 104 moves down with the gas stream 146 in the environment of the cohesive fluid 106, a continuously thinned cellulose filament or cellulose is formed. Fiber 108. Thus, the process involved in the method of manufacture described with reference to FIG. 1 can include shaping a lyocell spinning solution 104 (which can also be represented as a cellulose solution) to form a liquid strand or potential filament, the liquid strand or potential length The filaments are stretched by the gas stream 146 and are significantly reduced in diameter and increased in length. Prior to or during formation of the web on the fiber support unit 132, it may also involve partially agglomerating the potential filaments or fibers 108 (or preforms thereof) by the coalescing fluid 106. The filaments or fibers 108 are formed into a web fabric 102, washed, dried, and further processed as needed (see further processing unit 134). For example, filaments or fibers 108 can be collected, for example, on a rotating drum or belt, thereby forming a web. Due to the described manufacturing process, particularly the choice of solvent used, the fibers 108 have a copper content of less than 5 ppm and/or a nickel content of less than 2 ppm. This advantageously increases the purity of the fabric 102. The lyocell solution spunlace (i.e., non-woven cellulosic fabric 102) in accordance with an exemplary embodiment of the present invention preferably exhibits one or more of the following properties: (i) The dry weight of the web is 5 to 300 g. /m2, preferably 10-80 g/m2 (ii) according to standard WSP 120.6 or DIN 29073 (especially in the latest version valid on the priority date of this patent application), the thickness of the mesh is 0.05 to 10.0 mm, Preferably, 0.1 to 2.5 mm (iii) according to EN 29073-3 or ISO 9073-3 (especially in the latest version valid on the priority date of the present patent application), the MD has a specific intensity range of 0.1 to 3.0 Nm 2 . /g, preferably 0.4 to 2.3 Nm2/g (iv) according to EN29073-3 or ISO9073-3, respectively (especially in the latest version valid on the priority date of this patent application), the average stretch range of the net is 0.5 to 100%, preferably 4 to 50% (v) mesh MD/CD intensity ratio of 1 to 12 (vi) according to DIN 53814 (especially in the latest version valid on the priority date of this patent application) The water retention of the net is from 1 to 250%, preferably from 30 to 150% (vii) according to DIN 53923 (especially the latest version valid on the priority date of this patent application) The water retention capacity of the net is 90 to 2000%, preferably 400 to 1100% (viii) according to the decomposition standard EN 15587-2 and the ICP-MS standard EN 17294-2, the copper content is specifically determined to be lower than A metal residual level of 5 ppm and a nickel content of less than 2 ppm. Most preferably, the lyocell solution sprayed web exhibits all of the properties (i) to (viii) mentioned above. As noted, the process for producing the nonwoven cellulosic fibrous web 102 preferably comprises the following: (a) comprising a cellulose solution dissolved in NMMO through the orifice 126 of at least one of the spray nozzles 122 (see reference). Symbol 104) is extruded to form filaments of the lyocell spinning solution 104. (b) The filaments of the lyocell spinning solution 104 are drawn (c) by a gas stream (see reference numeral 146). The filaments are contacted with a vapor mist (see reference numeral 106), preferably containing water, to at least partially precipitate the fibers 108. Thus, prior to forming the web or nonwoven cellulosic fabric 102, the filaments or fibers 108 are at least partially precipitated (d) to collect and precipitate the filaments or fibers 108 to form a web or nonwoven cellulosic fabric 102. (e) removing the solvent in the washing line (see washing unit 180) (f) arbitrarily joining by hydroentanglement, needle sticking or the like (see further processing unit 134) (g) drying and winding. The components of the nonwoven cellulosic fibrous web 102 can be bonded by combining, intertwining, hydrogen bonding, physical bonding (such as hydroentanglement or needle sticking), and/or chemical bonding. For further processing, the nonwoven cellulosic fibrous web 102 may be combined with one or more layers of the same and/or other materials, such as (not shown) synthetic polymer layers, cellulosic fluff pulp, cellulose or synthetic polymers. Nonwoven webs of fibers, bicomponent fibers, cellulose pulp webs (such as airlaid or wet laid pulp), high strength webs or fabrics, hydrophobic materials, high performance fibers (such as heat resistant materials or flame retardant materials) a layer that imparts altered mechanical properties to a final product (such as a layer of polypropylene or polyester), a biodegradable material (eg, a film from a polylactic acid, a fiber, or a mesh), and/or a high bulk material. Several distinguishable layers of nonwoven cellulosic fabric 102 may also be combined, see for example Figure 7. The nonwoven cellulosic fabric 102 can consist essentially of only cellulose. Alternatively, the nonwoven cellulosic fibrous web 102 can comprise a mixture of cellulose and one or more other fibrous materials. Additionally, the nonwoven cellulosic fiber web 102 can comprise a bicomponent fiber material. The fibrous material in the nonwoven cellulosic fibrous web 102 can comprise, at least in part, a modifying material. The modifying substance may be selected from the group consisting of, for example, a polymer resin, an inorganic resin, an inorganic pigment, an antibacterial product, a nanoparticle, a lotion, a flame retardant product, an absorption improving additive such as a superabsorbent resin. ), ion exchange resins, carbon compounds (such as activated carbon, graphite, conductive carbon), X-ray contrast materials, luminescent pigments, and dyes. Finally, the cellulosic nonwoven web or nonwoven cellulosic fabric 102 made directly from the lyocell spinning solution 104 provides an opportunity to achieve value-added web properties that are not possible via the short fiber path. This includes the opportunity to form a uniform lightweight web, manufacture microfiber products, and fabricate continuous filaments or fibers 108 that form a web. Furthermore, several manufacturing processes are no longer required compared to short fiber webs. Further, the nonwoven cellulose fiber fabric 102 according to an exemplary embodiment of the present invention is biodegradable and is manufactured from a continuously sourced raw material (i.e., wood pulp 110, etc.). In addition, it has advantages in terms of purity and absorption. In addition, it has adjustable mechanical strength, stiffness, and softness. Further, the nonwoven cellulose fiber fabric 102 according to an exemplary embodiment of the present invention can be manufactured to have a low weight per unit area (for example, 10 to 30 g/m 2 ). Very fine filaments having a diameter as small as (or not more than) 5 μm, in particular not more than 3 μm, can be produced by this technique. Further, the nonwoven cellulose fiber fabric 102 according to an exemplary embodiment of the present invention may be formed by the aesthetics of various nets, for example, in a flat crispy film-like manner, with paper-like paper. Like), or in a soft flexible textile-like manner. The stiffness and mechanical rigidity, or flexibility and softness of the nonwoven cellulosic fibrous web 102 can be more precisely adjusted by adjusting the process parameters of the process. This can be adjusted, for example, by adjusting the number of merged locations, the number of layers, or by post-processing such as needle sticking, hydroentangling, and/or calendering. Particularly possible to manufacture as low as 10g/m 2 Or a lower basis weight of the nonwoven cellulosic fabric 102 to obtain filaments or fibers 108 having a very small diameter (e.g., as low as 3 to 5 [mu]m or less). 2, 3 and 4 show experimental captured images of a nonwoven cellulosic fabric 102 in accordance with an exemplary embodiment of the present invention, wherein the merging of individual fibers 108 is accomplished by corresponding process control. The oval marks in Figures 2 through 4 show such merged regions in which the plurality of fibers 108 are integrally connected to one another. At this merge point, two or more fibers 108 can be interconnected to form a unitary structure. Figures 5 and 6 show experimental captured images of the nonwoven cellulosic fabric 102 (where the swelling of the fibers 108 have been completed) in accordance with an exemplary embodiment of the present invention, wherein Figure 5 shows the fibrous web 102 in a dry, non-swellable state, While Figure 6 shows the fibrous web 102 in a wet, swollen state. The hole diameters can be measured in the two states of Figs. 5 and 6, and can be compared with each other. When the average of 30 measurements was calculated, the hole size was reduced to 47% of its original diameter by the swelling of the fiber 108 in the aqueous medium. Figure 7 shows an experimental captured image of a nonwoven cellulosic fibrous web 102 in accordance with an exemplary embodiment of the present invention, wherein two of the fibers 108 are completed by a corresponding process design (i.e., a continuous configuration of a plurality of spinning nozzles). The formation of stacked layers 200, 202. In Figure 7, two separate but connected layers 200, 202 are indicated by horizontal lines. For example, the n-layer fabric 102 (n ≥ 2) can be manufactured by continuously arranging n spun nozzles or spray nozzles 122 in the machine direction. Specific exemplary embodiments of the present invention will be described in more detail below: Figure 8 shows a schematic drawing that will be used to explain the clarification of the fibers 108 when adjusting the roundness of the cross-section of the fibers 108 to deviate from the circular cross-section. bending. To explain the phenomenon, the fiber 108 is shown in Fig. 8 in a state of a straight forceless force (top) and a state in which the fiber 108 is subjected to bending (bottom). When the fiber 108 has a perfect cylindrical cross section, even a very small bending force may cause the fiber 108 to bend along an unpredictable bending axis. Therefore, in practical applications, it is impossible to predict or determine the direction, and the bundle of fibers 108 having a perfectly cylindrical cross section will undergo bending in this direction. However, when the roundness of the fiber 108 deviates significantly from a value (i.e., the cross-section of the fiber 108 deviates from a true circle, such as an oval shape (especially an elliptical shape), thereby defining a preferred bending axis, along the The shaft can be bent in a simpler manner (or with a smaller force) than in its vertical direction. For example, a smaller force having a shorter short axis as a curved line may bend the fiber 108 having an oval-elliptical cross section as compared to a longer major axis as the curved line. Applying the phenomenon to the fiber design of the fabric 102 in accordance with an exemplary embodiment of the present invention, designing the fibers 108 of such a fabric 102 having a circular cross-section allows for a predictable definition of the preferred bending axis of the fibers 108. When the filaments of the lyocell spinning solution 104 are deposited on the fiber support unit 132 to form the fibers 108 by agglomeration, they will be accommodated along the fibers of the fiber support unit 132 in a predictable and not only statistical manner. The surfaces are arranged in a certain order. Thus, by defining the cross-section of the fiber 108 to deviate from the circular symmetry geometry, the mechanical properties of the fabric 102 can be precisely defined. Thus, predictability can be introduced into the nonwoven cellulosic fabric 102 due to the significant non-circular roundness definition of the fibers 108. Finally, the deviation of at least some of the fibers 108 from the cylindrical geometry of the nonwoven cellulosic fabric 102 in accordance with an exemplary embodiment of the present invention is adjusted by corresponding adjustments in the manufacturing process, allowing for precise definition of the mechanical properties of the fabric 102, particularly It is allowed to obtain the fabric 102 having high mechanical strength. Figure 9 shows an experimental captured image of a nonwoven cellulosic fabric 102 in accordance with an illustrative embodiment of the invention, depicting fibers 108 having a cross-sectional shape that deviates from a circle. Preferably, along at least a portion of the length of the fibers 108, at least 10% of the fibers 108 have a non-circular cross-sectional shape of no more than 50% roundness. Due to this strong deviation of the significant subset of fibers 108 from the cylindrical geometry, a degree of regularity can be defined in the fabric 102. This allows fine tuning of the mechanical properties of the fabric 102 obtained. Based on the non-woven standard WSP90.3, the smoothness of the fabric 102 measured by the "fabric feel tester" can be 2mNm. 2 /g and 70mNm 2 The wide range between /g is freely adjustable because the desired mechanical strength can be precisely defined by the non-circular roundness design of at least some of the fibers 108. Due to the manufacturing process described above with reference to fabric 102 of Figure 1, fiber 108 has only a very small copper content of less than 5 ppm and/or has a very small nickel content of less than 2 ppm. Thus, fabric 102 having very small heavy metal contaminants can be made, ensuring biocompatibility of fabric 102 and preventing allergic reactions when fabric 102 is in physical contact with human skin. Figure 10 shows an experimental captured image of a nonwoven cellulosic fibrous web 102 in accordance with an exemplary embodiment of the present invention, wherein the fibers 108 having a cross-sectional shape that deviates from a circle are partially twisted. In the embodiment of Figure 10, some of the fibers 108 are twisted. Thus, the fibers 108 extend along at least a portion of their longitudinal direction to form a slightly helical structure. This fiber twisting imparts mechanical strength to the resulting nonwoven cellulosic fabric 102 while allowing some elastic adjustment of the fabric 100. In particular, the combination of fibers 108 having a true roundness offset from one, twisted, and merged with one another at merged location 204 provides a degree of flexibility to fabric 102. 11 shows an experimental captured image of a nonwoven cellulosic fabric 102 in accordance with another exemplary embodiment of the present invention, consisting of three stacked layers 202, 200, 200 having different diameters of fibers 108. According to Figure 11, the intermediate interlayer 200 has a significantly smaller diameter of the fibers 108 than the two outer layers 200, 202 above and below. The multilayer fabric 102 shown in Figure 11 is particularly suitable for applications such as medical applications, agricultural textiles, and the like. For example, the active material can be stored in the inner layer 200, which exhibits a high capillary action. The outer layers 200, 202 can be designed based on stiffness and surface feel. This is advantageous for cleaning and medical applications. For agricultural applications, the fiber layer design can be specifically configured depending on the nature of the evaporation and/or the penetration of the roots. In another application, the multilayer fabric 102 shown in Figure 11 can be used as a mask, wherein the intermediate layer 200 can have a particularly significant fluid retention capability. The cover layers 200, 202 can be configured for adjusting fluid release properties. The diameter of the fibers 108 of each layer 200, 200, 202 can be used as a design parameter for adjusting these functions. Thus, the fibers 108 shown in Figure 11 are located in three different distinguishable layers 200, 202. The fibers 108 of the different layers 200, 202 are integrally merged at the merged location 204 between the layers 200, 202. Further, at least some of the fibers 108 are provided with a non-circular cross section having a true roundness of no more than 90%, which provides a degree of order in the layers 200, 202 and strengthens the fabric 102. Figure 12 shows how the value of the true circularity of a fiber 108 having a section offset from a circular cross section is calculated as the ratio between the inscribed circle 280 of the section of the fiber 108 and the radius of the circumscribed circle 282, in accordance with an exemplary embodiment of the present invention. . The minimum circumscribed circle 282 is defined as the smallest circle that encompasses the entire true roundness profile of the section of the fiber 108 depicted in FIG. The maximum inscribed circle 280 is defined as the largest circle of the entire true roundness profile of the section of the fiber 108 depicted in FIG. In the context of the present application, the roundness can be defined as the ratio between the radius r of the inscribed circle 280 divided by the radius R of the outer surface 282. The roundness can be expressed by the resulting percentage value. In the present example, the roundness of R≈2r and fiber 108 is thus about 0.5 or 50%. For comparison, the cylindrical fiber 108 satisfies the condition R = r and has a roundness of 1 or 100%. Figure 13 illustrates a portion of an apparatus 100 for making a nonwoven cellulosic fabric 102 that is composed of two stacked layers 200 of endless cellulosic fibers 108, in accordance with an illustrative embodiment of the present invention. And 202 are composed. In view of the movable fiber receiving surface of the conveyorized fiber support unit 132, the upstream spray nozzle 122 on the left hand side of Figure 13 produces a layer 202 of fibers 108. The layer 200 of the other fibers 108 is produced by the downstream spray nozzle 122 (on the right hand side of Figure 13) and attached to the upper major surface of the previously formed layer 202, thereby obtaining the double layers 200, 202 of the fabric 102. According to FIG. 13, control unit 140 (control spray nozzle 122 and agglomeration unit 128) is configured for adjusting process parameters such that at least a portion of fibers 108 are integrally merged at merged locations 204 between layers 200, 202. Although not shown in FIG. 13, the fibers 108 may be further processed after being collected onto the fiber support unit 132, such as by water entanglement, needle sticking, and/or impregnation. Referring again to the embodiment illustrated in FIG. 13, one or more additional nozzle bars or spray nozzles 122 may be provided and may be continuously disposed along the direction of transport of the fiber support unit 132. A plurality of spray nozzles 122 can be configured such that an additional layer 200 of fibers 108 can be deposited on top of the previously formed layer 202 (preferably before the agglomeration or curing process of the fibers 108 of layer 202 and/or layer 200 is fully completed) , which triggers the merge. This may have an advantageous effect on the properties of the multilayer fabric 102 when the process parameters are properly adjusted: The intended combination between the fibers 108 of the fabric 102 according to Figure 13 may be triggered to further increase the mechanical stability of the fabric 102. In this context, the combination may be adhesion of the contact points of the filaments contacting the fibers 108, particularly prior to completion of the coacervation process of the one or two fibers 108. For example, the merging can be facilitated by increasing the contact pressure between the two filaments of the lyocell spinning solution 104 to be combined by a fluid stream (e.g., a gas stream or a stream of water). By taking such measures, on the one hand the adhesion between the different filaments or fibers 108 of one of the layers 200, 202 can be increased, and/or on the other hand the adhesion between the layers 200, 202 can be increased. According to apparatus 100 of FIG. 13 (which is configured for use in fabricating multilayer fabric 102), a number of process parameters are implemented that can be used to adjust the combination factor, design fiber 108, and shape and/or diameter of fiber layers 200, 202, or Diameter distribution. This is the result of a continuous configuration of the plurality of spray nozzles 122, each of which can be operated with individually adjustable process parameters. When the apertures 126 of the plurality of spray nozzles 122 are formed differently and in a non-circular manner, a fabric 102 having fibers 108 that are offset from the cross section may also be formed. Such fibers 108 may be oval, elliptical, rectangular, triangular, polygonal, having sharp and/or rounded edges, and the like. For the device 100 according to Fig. 13, a fabric 102 consisting of at least two layers 200, 202 (preferably more than two layers) can be produced in particular. By the distinct layer separation of the multilayer fabric 102, the multilayer fabric 102 can later be divided into different individual layers 200, 202 or different multilayer portions. In-layer adhesion of the fibers 108 of the layers 200, 202 and interlayer adhesion of the fibers 108 between adjacent layers 200, 202 (eg, by merging and/or by friction), in accordance with an exemplary embodiment of the present invention Adjust appropriately and separately. When the process parameters are adjusted such that when the layer 200 of fibers 108 is placed on top of it, the agglomeration or solidification of the fibers 108 of the other layer 202 has been completed, and corresponding individual control for each individual layer 200, 202 can be specifically obtained. For example, adjusting the process parameters for adjusting the merge according to FIG. 13 includes continuously configuring a plurality of spray nozzles 122 having apertures 126 along the movable fiber support unit 132 to deposit a first layer 202 of fibers 108 on the fiber support unit 132. The second layer 200 of fibers 108 is deposited on the first layer 202 before all of the fibers 108 have completed agglomeration at the interface between the layers 200, 202. Thus, the different fibers 108 of the fabric 102 can be located in different distinguishable layers 200, 202, however they can be combined by forming merge locations 204. In other words, the fibers 108 of the different layers 200, 202 can be integrally merged at one or more merge locations 204 between the layers 200, 202. Figure 14 illustrates components of an apparatus 100 for fabricating a nonwoven cellulosic fabric 102 in accordance with yet another exemplary embodiment of the present invention, wherein the process is controlled by the control unit 140 to trigger a deviation from roundness. The formation of the merged position between the rounded fibers 108 (by applying a lateral force to the fibers 108 during agglomeration). More specifically, the spinning solution warping unit 270 is disposed in the apparatus 100 that is configured to apply a deforming force to the filaments of the lyocell spinning solution 104 prior to completion of the agglomeration. This deformation force causes the filaments to change from a circular cross section to a non-circular cross section. As can be seen from detail 274, a portion of the fabric 102 is shown prior to completion of agglomeration of the fibers 108, and the solution deformation force is applied by directing the forming fluid stream 272 to the filaments of the lyocell spinning solution 104 prior to completion of the agglomeration. The forming fluid 272 can be a gas stream and/or a liquid stream that is directed from the spinning solution warping unit 270 to the filaments of the lyocell spinning solution 104 before the fibers 108 are deposited therefrom. The pressure exerted by the forming fluid 272 on the filaments of the lyocell spinning solution 104 causes the filaments to change from, for example, a circular cross-sectional shape to an elliptical or flat shape, as shown in detail 274. When the pressure applied to the filaments of the lyocell spinning solution 104 by the forming fluid 272 is maintained until coagulation or precipitation is complete, the fibers 108 will automatically form a corresponding shape having a non-circular cross section. When the forming fluid 272 comprises or consists of water, the application of the forming pressure can be synergistically combined with the agglomerated precipitation of the fibers 108 from the lyocell spinning solution 104, at least in part by the subsequent aqueous forming fluid 272. trigger. Figure 15 illustrates a component of an apparatus 100 for making a nonwoven cellulosic fibrous web 102 having an aperture 126 shaped to form a deviation, in accordance with yet another exemplary embodiment of the present invention. The roundness of the roundness of the fiber 108. Additionally or alternatively, in accordance with the rules employed in FIG. 14, for determining that at least a portion of the fibers 108 of the fabric 102 are less than one round, the apertures 126 of the spray nozzles 122 of FIG. 15 are provided with a non-circular shape. In the illustrated embodiment, alternating rows of elliptical apertures 126 are contemplated that have respective major axes, or along a common alignment axis 236 (i.e., according to the horizontal direction of Figure 15, comparing odd columns of holes) Ports 126) are oriented or oriented along parallel alignment axes 238 (i.e., according to the vertical direction of Figure 15, comparing even rows of apertures 126). However, it will be clearly understood in the ordinary skill in the art that the illustrated pattern of apertures 126 is merely exemplary, and that many other patterns of non-circular apertures 126 may be implemented in accordance with other exemplary embodiments of the present invention. . 16 shows a schematic view of a nonwoven cellulosic fabric 102 in accordance with an illustrative embodiment of the invention, showing fibers 108 having a cross-sectional shape that deviates from a circle, with the result that fibers 108 are generally disposed or aligned along a preferential direction 290. . In other words, the fibers 108 are anisotropically aligned within the fabric 102 to define a preferentially aligned direction 290 in which a larger portion of the fibers 108 are aligned relative to the other directions. According to Fig. 16, a plurality of fibers 108 of the fabric 102 are shown, all of which have a non-circular elliptical cross section. Thus, when the fibers 108 are deposited on the fiber support unit 132, the fibers 108 are preferably curved about the alignment direction 290. As can be seen from Figure 16, some of the fibers 108 merge at the merged location 204 prior to agglomeration, while the other fibers 108 cross each other at the intersection 264 without merging, i.e., only experiencing mutual friction. More generally, providing a nonwoven cellulosic fabric 102 having non-circular endless fibers 108 provides increased rigidity and uniformity. Although each individual process of depositing one of the fibers 108 on the fiber support unit 132 has a statistical effect, the predictable better deposition direction of the fibers 108 can be defined by configuring at least a portion of the fibers 108 in a non-circular cross-section. . By producing at least a portion of the fibers 108 with a sufficiently small roundness, a corresponding increase in at least one of uniformity and rigidity can be obtained. This is particularly powerful for increasing the stability of the fabric 102 when simultaneously merging between at least a portion of the fibers 108. Functionality of the fabric 102 relative to a particular application is made possible by adjusting the properties of the fibers 108 of the fabric 102 in accordance with an exemplary embodiment of the present invention in terms of roundness or cross-sectional shape. In particular, this makes it possible to design a fabric 102 having a higher mechanical strength at a given grammage, or to obtain a lower grammage at a given mechanical strength. This enhanced mechanical stability can be obtained in one or two perpendicular directions in the plane of the fabric 102 corresponding to the fiber receiving plane of the fiber support unit 132. Very advantageously, according to an exemplary embodiment of the present invention, such a fabric 102 can be manufactured according to the structure of a lyocell spinning solution, thereby ensuring that the obtained fabric 102 has very low-contamination heavy metal impurities. Therefore, the obtained non-woven cellulose fiber fabric 102 has a very high purity, so that the obtained fabric 102 or a product based thereon is less likely to cause an allergic reaction to the user. According to a preferred embodiment, one or more nozzle bars or spray nozzles 122 for producing filaments of the lyocell spinning solution 104 are implemented, wherein the filaments are then drawn, crimped, and deposited on a fiber support. The fiber of unit 132 is received on the surface. During the stretching process and/or when filaments of the lyocell spinning solution 104 that have not yet agglomerated are deposited on the fiber support unit 132, two or more fibers may be triggered or promoted by air vorticity or turbulence The formation of the merged position 204 is between 108. This merging process can occur at different points in time during the agglomeration of the chemical process that forms the endless fibers 108. They can also be adjusted with different intensities and can be promoted using different media such as water or air. The coacervation and/or shaping of the filaments, as well as the adhesion at the contact or merged locations 204, can be controlled by corresponding adjustments. As a result, a wide variety of combined effects can be adjusted: on the one hand, a fabric 102 having a very low tendency to merge and stick can be formed; on the other hand, the process can be controlled to obtain a strong combination, causing the fibers 108 to lose their shape. And tend to present a planar membrane structure. During the deposition process of the fibers 108 or preforms that have not yet fully agglomerated, a statistical or random process may be involved. This typically results in any structure without end filaments or fibers 108. In particular, when the conveying speed of the conveying device (i.e., the fiber supporting unit 132) is significantly smaller than the speed of the filament moving downward on the fiber receiving surface of the fiber supporting unit 132, the arbitrary orientation of the filaments of the fiber 108 may occur. In other words, when the filaments are moved downward on the fiber supporting unit 132, an unpredictable or pseudo-random deposition direction of the filaments or fibers 108 may occur due to the reaction force applied from the fiber supporting unit 132 to the filaments. This phenomenon has been described above with reference to FIG. However, as described above with reference to FIG. 8, an exemplary embodiment of the present invention can overcome the randomness of the fibers 108 by arranging at least a portion of the fibers 108 in a non-circular cross-section having a true roundness value of 90% or less. This pure statistic of sedimentary behavior. When the fibers 108 are offset from the cylindrical cross-section to a sufficient extent, one or more major deposition directions of the fibers 108 or groups of fibers 108 for corresponding design and orientation may be defined to increase the uniformity and properties of the fabric 102. Sex. Descriptively and referring to the elliptical cross-section of the fibers 108, such elliptical fibers 108 preferably bend or kink downwardly in the direction of the smaller cross-sectional dimension (i.e., along the minor axis of the ellipse). . Because of this phenomenon, control of the cross-sectional shape of the fabricated fibers 108 deviates from the circular shape, allowing one or more preferentially aligned directions of the fibers 108 in the fabric 102 to be defined. To produce a fiber 108 having a roundness of less than 90%, preferably less than 50%, pressure can be applied to the un-agglomerated preform of the fiber 108 by, for example, blowing or creating a water jet. This pressure can also be applied to the two opposing surfaces of the preform of fibers 108 to flatten the fibers. For example, when pressure is applied from 0° and 180°, the preferred flattening or ovalization of the fibers 108 occurs along the 90° to 270° axis. In order to produce a fiber 108 having a roundness of less than 90%, preferably less than 50%, additionally or alternatively, a hole having a spray nozzle 122 having an oval (or more generally non-circular) nozzle cross section may be provided Port 126. In the frame of the mechanism for forming the fibers 108 having a non-circular cross section, one or more of the following options may be applied: a) transport of the fabric 102 in the MD direction at a high transport speed of the fiber support unit 132 An implicit focus that results in an average fiber arrangement (which can be obtained by adding the transfer rate to the deposition vector). In particular, when the transport speed is on the same order of magnitude or even greater than the deposition speed, an effective orientation of the fiber arrangement of the fabric 102 in the MD direction can be achieved. The defined cross-sectional control of the deposited fibers 108 in the CD direction is achieved as compared to the circular cross-section due to the cross-sectional stretching or flattening modification of the fibers 108, and an increase in the CD direction is obtained at a transmission speed of zero. Fiber orientation. Therefore, the average or intermediate value at the transport speed and the CD deposition enhancement can be determined, at which the preferential alignment direction of the fibers 108 is not obtained. In other words, even under such conditions, perfect uniformity can be obtained. However, it should be mentioned that in some embodiments, the deposition rate can be higher than the transmission speed, especially on the order of magnitude. b) It is currently believed that a relatively small number of fibers 108 have been modified in accordance with the principles described in a), resulting in more adjacent fibers 108 also preferably oriented in the CD direction. This can be explained by the analogy of the forest in the storm. The broken first tree triggers a domino-like forest passage along the direction of the fracture. c) By modifying the cross-sectional shape of the fibers 108, a friction-based clamping effect in accordance with an exemplary embodiment of the present invention can be produced in the fabric 102. This results in self-inhibition as in a conical tool container. This effect is already obtained by the relatively small deviation of the cross-sectional shape of the fiber 108 compared to the circular cross section. The transition from a circular cross section to an oval cross section can form such a self-suppressing system relative to the other fiber 108 (also having a non-circular cross section or having a circular cross section). Referring again to the embodiment illustrated in FIG. 13, one or more additional nozzle bars or spray nozzles 122 may be provided and may be continuously disposed along the direction of transport of the fiber support unit 132. A plurality of spray nozzles 122 can be configured such that an additional layer 200 of fibers 108 can be deposited on top of the previously formed layer 202 (preferably before the agglomeration or curing process of the fibers 108 of layer 202 and/or layer 200 is fully completed) , which triggers the merging of layers. This may have an advantageous effect on the properties of the multilayer fabric 102 when the process parameters are properly adjusted: In one aspect, the first deposited layer 202 may be deposited on a conveyor belt (such as a conveyor belt) that is the fiber support unit 132. In such an embodiment, the fiber support unit 132 can be implemented as an ordered structure of a release mechanism and an air suction opening (not shown). In the statistical distribution of the filaments of the fibers 108, this may have the effect of finding higher material concentrations in areas where no gas flow is present. This (especially microscopic) change in material density can be considered a perforation from a mechanical point of view, which acts to distort the uniformity of the nonwoven cellulosic fabric 102 (especially due to its tendency to inhibit the pattern). Holes may be formed in the nonwoven cellulosic fibrous web 102 at a location where the gas stream or liquid stream (e.g., water) penetrates the nonwoven cellulosic fibrous web 102. By such a fluid flow, wherein the fluid can be a gas or a liquid, the tensile strength of the nonwoven fiber fabric 102 produced can be increased. Without wishing to be bound by a particular theory, it is presently believed that the second layer 200 can be considered a reinforcing layer of the first layer 202 which compensates for the reduced uniformity of the layer 202. This increase in mechanical stability can be further improved by variations in fiber diameter (especially variations in the interfiber diameter of the individual fibers 108 and/or changes in the longitudinal diameter within the fibers). When a deeper (particularly a single point) pressure is applied (e.g., provided by air or water), the cross-sectional shape of the fibers 108 can be further deliberately distorted, which can advantageously result in further increased mechanical stability. On the other hand, the intended combination between the fibers 108 of the fabric 102 according to Fig. 13 can be triggered to further increase the mechanical stability of the fabric 102. In this context, the combination may be adhesion of the support contacts of the filaments contacting the fibers 108, particularly prior to completion of the coacervation process of the one or two fibers 108. For example, the merging can be facilitated by increasing the contact pressure by a fluid stream (eg, a gas stream or a stream of water). By taking such measures, on the one hand, the cohesive strength between the filaments or fibers 108 of one of the layers 200, 202 can be increased, and/or on the other hand the cohesive strength between the layers 200, 202 can be increased. According to the apparatus 100 of FIG. 13 (which is configured for use in the manufacture of the multilayer fabric 102), a number of process parameters are implemented that can be used to design the shape and/or diameter, or diameter distribution of the fibers 108 and the fibrous layers 200, 202. This is the result of a continuous configuration of the plurality of spray nozzles 122, each of which can be operated with individually adjustable process parameters. The high mechanical strength of the fabric 102 in accordance with an exemplary embodiment of the present invention is also obtained by the following properties of the manufacturing process: First, endless fibers 108 made of cellulosic material are used because of the endless fibers 108 (and short The fibers have less interference transitions, resulting in a single fiber 108 having a higher load carrying capacity. Secondly, such a high purity fiber 108 can be produced because the heavy metal content associated with the process of the corresponding fabric 102 is very small. Third, the specific design of the carrier dust that supports the mesh or other carrier structure (web support system) that can be implemented in the spunlace manufacturing process allows for control of the stiffness of the fabric 102. In particular, the stability of the fabric 102 can be significantly increased by merging (e.g., air and/or water induced), thereby allowing for the acquisition of a bionic-like structure with high load capacity. With proper process control, a single filament can be provided with a drill bit that can also be retained in fabric 102 that is easy to manufacture. Thereby, twisted fibers 108 can be formed which can have increased stretchability by corresponding spring effects. At the same time, the elasticity of the fabric 102 comprising the twisted fibers 108 can be limited. This can be used to further increase the stability of the fabric 102. In particular, when the fiber 108 is bent, there is an effect that the elasticity decreases as the bending radius increases. When a suitable airflow vorticity or turbulence is implemented, the fabric 102 of the twisted fibers 108 with further increased stability can be designed. On the smooth, flat fiber receiving surface of the fiber support unit 132, the oval fibers 108 or filaments preferably rest on their wide sides. This has a strong influence on the properties of the fabric 102 produced, as this involves an orderly effect. In particular, this allows the manufacture of fabric 102 having a relatively small thickness and a relatively high density. Preferably, fabric 102 in accordance with an exemplary embodiment of the present invention is comprised of both circular fibers 108 and non-circular fibers 108. The corresponding fabric 102 can be made by using a hybrid spray nozzle 122 having circular and non-circular apertures 126, and/or by permanent, cyclic, or repeated modification of process parameters. In an exemplary embodiment of the invention, at least 2, in particular at least 3, more particularly at least 4, in particular up to 10, consecutively configured spray nozzles 122 may be implemented for fabricating fabric 102. Each spray nozzle 122 can include a plurality of orifices 126. Each spray nozzle 122 can optionally have a circular and/or non-circular aperture 126. The fabric 102 can also be manufactured by adjusting the agglomeration and/or stretching conditions of the filaments of the lyocell spinning solution 104, wherein the non-circular fiber portions are perpendicular or at least substantially perpendicular to the surface of the fabric 102 in cross-section. And oriented. This results in stable adhesion and solidification of the fabric 102. This allows one or more of the following advantages to be achieved: a high-loose fabric 102 is produced at a relatively low gram weight; an identifiable layer structure having an adjustable property profile; an adjustable property of the fabric 102 on the upper major surface and the lower major surface; The aligned oval fibers 108 allow for high tensile strength at reduced longitudinal and lateral elongation; the grammage can be adjusted over a wide range, for example, 8 g/m 2 Up to 250g/m 2 . In another exemplary embodiment of the invention, the nonwoven cellulosic fabric 102 is used in a biodegradable product. After biodegradation, no adhesive material or adhesive material remains. In particular, there is not a significant amount of heavy metals forming part of such biodegradable products. Unwanted particle wear from the fabric 102 can be prevented by corresponding process design. In accordance with an exemplary embodiment of the present invention, a defined deviation from the circular cross-section of the endless fibers 108 can be obtained in such a manner that the cross-sectional shape varies along the longitudinal extension of such fibers 108. This can also be achieved by bending the fiber 108 beyond its elastic limit, resulting in a transition from a resiliently curved state to a plastically bent state. This effect can be enhanced by subsequently fixing the curved fibers 108 (e.g., by water entanglement). When tearing the nonwoven cellulosic fibrous web 102, the result is that at some of the loop or fusiole structure, another endless fiber 108 is guided through the structure during tearing, the diameter is no longer suitable and varies in small shapes. Self-inhibition has already occurred. This increases the overall tear strength of the fabric 102. This is particularly relevant in the implementation of the endless fibers 108, wherein this self-inhibiting effect promoted by the deviation of the roundness from one fiber is stronger than that of the short fibers. Very advantageously, the deviation of the cross-section of the fiber 108 from the circular cross-section can be combined with a change in fiber diameter (especially a change in thickness within the fiber and/or a change in thickness between fibers). This combination results in a particularly significant increase in the mechanical stability of the fabric 102. In summary, in accordance with an exemplary embodiment of the present invention, one or more of the following adjustments can be made in particular: - low uniform fiber diameter to achieve high smoothness of fabric 102 - multilayer fabric 102 having low diameter fibers and relatively low speed Allowing high fabric caliper with low fabric density - The equal absorption curve of the functionalized layer allows for uniform humidity and fluid containment behavior, as well as uniform behavior in terms of fluid release - also allows the single layer 200, 202 to be differently Functionalized to obtain products with anisotropic properties (eg, for wicking, oil containment, water containment, dust removal, roughness). In the end, it should be noted that the above-described embodiments are illustrative and not limiting, and that those skilled in the art will be able to devise various alternative embodiments without departing from the scope of the invention as defined by the appended claims. In the scope of the patent application, any reference signs in parentheses shall not be construed as limiting the scope of the patent application. The words "comprising" and "comprises", etc., do not exclude the presence of the elements or steps in addition to the elements or steps listed as a whole in the scope of the claims. A singular reference to an element does not exclude the plural reference of the element, and vice versa. In the scope of the patent application for a number of methods, several of these methods can be implemented by the same software or hardware project. The mere fact that certain measures are recited in mutually different patent application scopes does not mean that a combination of these measures cannot be used. Below, examples for generating merge factor changes are described and shown in the table below. When a constant spinning solution (i.e., a spinning solution having a constant consistency), particularly a lyocell spinning solution, and a constant gas flow (e.g., air throughput) are used, the different combining factors in the cellulosic fiber fabric can be changed by Condensed spray flow to achieve. Therefore, the relationship between the condensed spray stream and the combination factor can be observed, that is, the tendency of the combined behavior (the higher the condensed spray stream, the lower the combination factor). MD here denotes the machine direction, and CD denotes the lateral direction. Softness (described by known specific hand measurement techniques, based on the non-woven standard WSP90.3, measured by the so-called "fabric hand tester", especially the latest version valid on the priority date of this patent application) The above combined trend will be followed. The intensity (described as Fmax) (for example, according to EN29073-3 and ISO9073-3, respectively, especially the latest version valid on the priority date of this patent application) will also follow the combined trend. Thus, the softness and strength of the resulting nonwoven cellulosic fiber fabric can be adjusted according to the degree of combination (as defined by the combination factor).

100‧‧‧裝置100‧‧‧ device

102‧‧‧(非織纖維素纖維)織物102‧‧‧ (non-woven cellulose fiber) fabric

104‧‧‧萊賽爾紡絲溶液104‧‧‧Lysel spinning solution

106‧‧‧凝聚流體106‧‧‧Condensate fluid

108‧‧‧纖維108‧‧‧Fiber

110‧‧‧木漿110‧‧‧ Wood pulp

112‧‧‧水容器112‧‧‧ water container

113‧‧‧計量單元113‧‧‧Measuring unit

114‧‧‧儲槽114‧‧‧ storage tank

116‧‧‧溶劑容器116‧‧‧ solvent container

118‧‧‧濃縮單元118‧‧‧Concentration unit

119‧‧‧混合單元119‧‧‧Mixed unit

120‧‧‧溶解單元120‧‧‧Dissolution unit

122‧‧‧噴射嘴122‧‧‧ spray nozzle

124‧‧‧纖維形成單元124‧‧‧Fiber forming unit

126‧‧‧孔口126‧‧ ‧ orifice

128‧‧‧凝聚單元128‧‧‧aggregation unit

132‧‧‧纖維支撐單元132‧‧‧Fiber support unit

134‧‧‧進一步加工單元134‧‧‧ further processing unit

136‧‧‧捲取機136‧‧‧Winding machine

140‧‧‧控制單元140‧‧‧Control unit

146‧‧‧氣流146‧‧‧ airflow

180‧‧‧洗滌單元180‧‧‧Washing unit

200‧‧‧層200‧‧ layers

202‧‧‧層202‧‧‧ layer

204‧‧‧合併位置204‧‧‧ merged location

236‧‧‧共同對齊軸236‧‧‧Common alignment axis

238‧‧‧平行對齊軸238‧‧‧Parallel alignment axis

264‧‧‧交叉位置264‧‧‧ cross location

270‧‧‧變形單元270‧‧‧Transformation unit

272‧‧‧成形流體272‧‧‧Forming fluid

274‧‧‧細節274‧‧‧Details

280‧‧‧內切圓280‧‧‧Inscribed circle

282‧‧‧外接圓282‧‧‧ circumscribed circle

290‧‧‧優先排列方向290‧‧‧Priority direction

R‧‧‧內切圓半徑R‧‧‧ inscribed circle radius

r‧‧‧外接圓半徑r‧‧‧Circular radius

以下將參考實施例的實例更詳細地描述本發明,但是本發明不限於此:   圖1根據本發明的例示性實施例,繪示用於製造由萊賽爾紡絲溶液直接形成的非織纖維素纖維織物的裝置,該萊賽爾紡絲溶液是藉由凝聚流體而凝聚。   圖2至圖4顯示根據本發明的例示性實施例之非織纖維素纖維織物的實驗捕捉影像,其中藉由特定的製程控制完成單根纖維的合併。   圖5及圖6顯示根據本發明的例示性實施例之非織纖維素纖維織物的實驗捕捉影像(其中已完成纖維的膨潤),其中圖5顯示呈乾燥非膨潤狀態的纖維織物,而圖6顯示呈潮濕膨潤狀態的纖維織物。   圖7顯示根據本發明的例示性實施例之非織纖維素纖維織物的實驗捕捉影像,其中藉由實施兩個串聯噴嘴的特定製程完成了纖維的兩個疊置層的形成。   圖8顯示示意性繪圖,表示當調整纖維截面的真圓度以偏離圓形截面時,可促進纖維的明確彎曲。   圖9顯示根據本發明的例示性實施例之非織纖維素纖維織物的實驗捕捉影像,繪示出具有偏離圓形的截面形狀之纖維。   圖10顯示根據本發明的例示性實施例之非織纖維素纖維織物的實驗捕捉影像,其中具有偏離圓形的截面形狀之纖維是經部分加撚的。   圖11顯示根據本發明的例示性實施例之非織纖維素纖維織物的實驗捕捉影像,由三個具有不同纖維直徑的堆疊層組成。   圖12顯示根據本發明的例示性實施例,如何計算具有偏離圓形截面的截面之纖維的真圓度作為纖維的截面之內切圓與外接圓之間的比值。   圖13根據本發明的另一例示性實施例,繪示用於製造非織纖維素纖維織物之裝置,其中控制製程以觸發纖維之間合併位置的形成。   圖14根據本發明的又另一例示性實施例,繪示用於製造非織纖維素纖維織物之裝置的部件,其中控制製程以觸發具有偏離圓形真圓度(藉由在凝聚期間向橢圓形無末端纖維施加橫向力)的真圓度的纖維之間合併位置的形成。   圖15根據本發明的又另一例示性實施例,繪示用於製造非織纖維素纖維織物之裝置的部件,該部件具有孔口,該孔口被塑形以形成具有偏離圓形真圓度之真圓度的纖維,並導致織物的機械性強化。   圖16是根據本發明的例示性實施例之非織纖維素纖維織物的示意圖,繪示出具有偏離圓形的截面形狀之纖維,結果,纖維大致上沿著優先方向配置。The invention will be described in more detail hereinafter with reference to examples of the embodiments, but the invention is not limited thereto: FIG. 1 is a diagram showing the production of non-woven fibers directly formed from a lyocell spinning solution according to an exemplary embodiment of the invention. A device for a plain fiber fabric in which the lyocell spinning solution is agglomerated by a coagulation fluid. 2 through 4 show experimental captured images of a nonwoven cellulosic fiber fabric in accordance with an exemplary embodiment of the present invention, wherein the incorporation of individual fibers is accomplished by a particular process control. 5 and 6 show experimental captured images of a nonwoven cellulosic fiber fabric in which swelled fibers have been completed, in accordance with an exemplary embodiment of the present invention, wherein Figure 5 shows a fibrous web in a dry, non-swellable state, and Figure 6 A fibrous fabric showing a moist swelling state. Figure 7 shows an experimental captured image of a nonwoven cellulosic fiber fabric in accordance with an exemplary embodiment of the present invention in which the formation of two superposed layers of fibers is accomplished by a particular process of performing two tandem nozzles. Figure 8 shows a schematic plot showing that when the roundness of the cross section of the fiber is adjusted to deviate from the circular cross section, a clear bend of the fiber can be promoted. Figure 9 shows an experimental captured image of a nonwoven cellulosic fiber fabric in accordance with an illustrative embodiment of the invention, depicting fibers having a cross-sectional shape that deviates from a circle. Figure 10 shows an experimental captured image of a nonwoven cellulosic fiber fabric in accordance with an exemplary embodiment of the present invention, wherein fibers having a cross-sectional shape that deviates from a circle are partially twisted. Figure 11 shows an experimental captured image of a nonwoven cellulosic fiber fabric in accordance with an exemplary embodiment of the present invention, consisting of three stacked layers having different fiber diameters. Figure 12 shows how the roundness of a fiber having a section deviating from a circular cross section is calculated as the ratio between the inscribed circle of the cross section of the fiber and the circumscribed circle, in accordance with an exemplary embodiment of the present invention. Figure 13 illustrates an apparatus for making a nonwoven cellulosic fiber fabric in accordance with another exemplary embodiment of the present invention, wherein the process is controlled to trigger the formation of a merged position between the fibers. Figure 14 illustrates, in accordance with yet another exemplary embodiment of the present invention, a component of an apparatus for making a nonwoven cellulosic fibrous fabric, wherein the process is controlled to trigger a deviation from rounded roundness (by ellipting during agglomeration) The shape of the merged position between the fibers of the roundness of the shape of the endless fiber is applied. Figure 15 illustrates, in accordance with yet another exemplary embodiment of the present invention, a component of an apparatus for making a nonwoven cellulosic fibrous fabric having an aperture shaped to form a circle that is offset from a circle. The roundness of the fibers and the mechanical reinforcement of the fabric. Figure 16 is a schematic illustration of a nonwoven cellulosic fiber fabric in accordance with an illustrative embodiment of the present invention, showing fibers having a cross-sectional shape that deviates from a circle, with the result that the fibers are disposed generally along a preferential direction.

Claims (15)

一種非織纖維素纖維織物(102),特別是由萊賽爾紡絲溶液(104)直接製造,其中該織物(102)包含實質無末端纖維(108)之網絡,並且其中至少1%的該等纖維(108)具有不大於90%的真圓度(roundness)之非圓形截面形狀。A nonwoven cellulosic fibrous web (102), particularly produced directly from a lyocell spinning solution (104), wherein the fabric (102) comprises a network of substantially endless fibers (108), and wherein at least 1% of the The equal fibers (108) have a non-circular cross-sectional shape of no more than 90% roundness. 如申請專利範圍第1項的織物(102),其包含下列特徵之至少一者:   其中至少3%、特別是至少5%的該等纖維(108)具有不大於90%的真圓度之非圓形截面形狀;   其中至少1%的該等纖維(108)具有不大於80%、特別是不大於70%的真圓度之非圓形截面形狀。A fabric (102) according to claim 1 which comprises at least one of the following features: wherein at least 3%, in particular at least 5%, of said fibers (108) have a true roundness of no more than 90% A circular cross-sectional shape; wherein at least 1% of the fibers (108) have a non-circular cross-sectional shape of no more than 80%, particularly no more than 70% roundness. 如申請專利範圍第1或2項的織物(102),其包含下列特徵之至少一者:   其中該織物(102)的光滑度(經測量以作為具體手感)是在2mNm2 /g與70mNm2 /g之間的範圍;   其中該等纖維(108)具有小於5ppm的銅含量及/或具有小於2ppm的鎳含量;   其中至少部分的該等纖維(108)在合併位置(204)處整體合併。A fabric (102) according to claim 1 or 2, which comprises at least one of the following features: wherein the smoothness of the fabric (102) (measured as a specific hand) is at 2 mNm 2 /g and 70 mNm 2 The range between /g; wherein the fibers (108) have a copper content of less than 5 ppm and/or have a nickel content of less than 2 ppm; wherein at least a portion of the fibers (108) are integrally combined at the merged location (204). 如申請專利範圍第1至3項中任一項的織物(102),其中該等纖維(108)的不同纖維至少部分地位於不同的可分辨之層(200、202)中。The fabric (102) of any one of claims 1 to 3, wherein the different fibers of the fibers (108) are at least partially located in different distinguishable layers (200, 202). 如申請專利範圍第4項的織物(102),其包含下列特徵之至少一者:   其中不同的層(200、202)之纖維(108)在該等層(200、202)之間的至少一個合併位置(204)處整體合併;   其中不同的層(200、202)之纖維(108)具有相同的物理性質;   其中不同的層(200、202)之纖維(108)具有不同的物理性質。A fabric (102) according to claim 4, comprising at least one of the following features: wherein at least one of the fibers (108) of the different layers (200, 202) is between the layers (200, 202) The merged locations (204) are collectively integrated; wherein the fibers (108) of the different layers (200, 202) have the same physical properties; wherein the fibers (108) of the different layers (200, 202) have different physical properties. 如申請專利範圍第1至5項中任一項的織物(102),其中至少部分的該等纖維(108)是經撚合的(twisted)。The fabric (102) of any one of claims 1 to 5 wherein at least a portion of the fibers (108) are twisted. 如申請專利範圍第1至6項中任一項的織物(102),其中該等纖維(108)在該織物(102)內經各向異性地排列從而大致上界定出至少一個優先排列方向(290),相較於其他方向,較大部分的纖維(108)沿著該至少一個優先排列方向排列。The fabric (102) of any one of claims 1 to 6 wherein the fibers (108) are anisotropically aligned within the fabric (102) to define substantially at least one preferential orientation (290) ), a larger portion of the fibers (108) are aligned along the at least one preferentially aligned direction than in other directions. 一種直接由萊賽爾紡絲溶液(104)製造非織纖維素纖維織物(102)的方法,其中該方法包含:   將該萊賽爾紡絲溶液(104)經由至少一個具有孔口(126)的噴射嘴(122)在藉助氣流(146)下擠出而進入到凝聚流體(106)環境中,從而形成實質無末端纖維(108);   收集纖維支撐單元(132)上的該等纖維(108)從而形成該織物(102);   調整製程參數使得至少1%的該等纖維(108)具有不大於90%的真圓度之非圓形截面形狀。A method of making a nonwoven cellulosic fibrous web (102) directly from a lyocell spinning solution (104), wherein the method comprises: passing the lyocell spinning solution (104) via at least one orifice (126) The spray nozzle (122) is extruded under airflow (146) into the environment of the coalescing fluid (106) to form substantially endless fibers (108); the fibers on the fiber support unit (132) are collected (108) Thereby forming the fabric (102); adjusting the process parameters such that at least 1% of the fibers (108) have a non-circular cross-sectional shape of no more than 90% roundness. 如申請專利範圍第8項的方法,其中調整該製程參數包含在該凝聚完成之前,對該萊賽爾紡絲溶液(104)的長絲施力。The method of claim 8, wherein adjusting the process parameter comprises applying a force to the filament of the lyocell spinning solution (104) prior to completion of the agglomeration. 如申請專利範圍第9項的方法,其中在該凝聚完成之前,藉由將成形流體導向該萊賽爾紡絲溶液(104)的長絲來施力。The method of claim 9, wherein the forming fluid is directed to the filaments of the lyocell spinning solution (104) prior to completion of the agglomeration. 如申請專利範圍第8至10項中任一項的方法,其中該方法另外包含在該纖維支撐單元(132)上的收集之後,將該等纖維(108)及/或該織物(102)進一步原位(in situ)加工,特別是藉由下列所組成的群組之至少一種方式加工:水纏結、針扎、含浸、用加壓蒸汽進行蒸汽處理、及壓延。The method of any one of claims 8 to 10, wherein the method further comprises collecting the fibers (108) and/or the fabric (102) further after collection on the fiber support unit (132) In situ processing, in particular by at least one of the following group consisting of: water entanglement, needle sticking, impregnation, steam treatment with pressurized steam, and calendering. 一種用於直接由萊賽爾紡絲溶液(104)製造非織纖維素纖維織物(102)的裝置(100),其中該裝置(100)包含:   至少一個具有孔口(126)的噴射嘴(122),其經配置用於將該萊賽爾紡絲溶液(104)在藉助氣流(146)下擠出;   凝聚單元(128),其經配置用於為該擠出的萊賽爾紡絲溶液(104)提供凝聚流體(106)環境從而形成實質無末端纖維(108);   纖維支撐單元(132),其經配置用於收集該等纖維(108)從而形成該織物(102);   控制單元(140),其經配置用於調整製程參數,使得至少1%的該等纖維(108)具有不大於90%的真圓度之非圓形截面形狀。A device (100) for fabricating a nonwoven cellulosic fibrous web (102) directly from a lyocell spinning solution (104), wherein the device (100) comprises: at least one jet nozzle having an orifice (126) ( 122) configured to extrude the lyocell spinning solution (104) by means of a gas stream (146); a coalescing unit (128) configured to spin the extruded lyocell The solution (104) provides a cohesive fluid (106) environment to form substantially endless fibers (108); a fiber support unit (132) configured to collect the fibers (108) to form the fabric (102); (140), configured to adjust process parameters such that at least 1% of the fibers (108) have a non-circular cross-sectional shape of no more than 90% roundness. 如申請專利範圍第12項的裝置(100),其中至少部分的該等孔口(126)是非圓形的,特別是卵形的,更特別地是橢圓形的。A device (100) according to claim 12, wherein at least a portion of the apertures (126) are non-circular, in particular oval, more particularly elliptical. 一種使用如申請專利範圍第1至7項中任一項之非織纖維素纖維織物(102)的方法,其是用於由下列所組成的群組之至少一者:擦巾;烘乾機用紙(dryer sheet);過濾器;衛生產品;醫療應用產品;地工織物;農用織物;衣服;用於建築技術的產品;汽車產品;居家裝飾用品(furnishing);工業產品;與美容、休閒、運動或旅行相關的產品;以及與學校或辦公室相關的產品。A method of using a non-woven cellulose fiber fabric (102) according to any one of claims 1 to 7 which is for at least one of the group consisting of: a wipe; a dryer Dryer sheet; filter; sanitary product; medical application product; geotextile; agricultural fabric; clothing; product for construction technology; automotive product; home furnishing; industrial product; and beauty, leisure, Sports or travel related products; and products related to the school or office. 一種產品或複合物,其包含如申請專利範圍第1至7項中任一項的織物(102)。A product or composite comprising the fabric (102) of any one of claims 1 to 7.
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