TW201843362A - Method of fabricating fiber masterbatch and fiber - Google Patents

Method of fabricating fiber masterbatch and fiber Download PDF

Info

Publication number
TW201843362A
TW201843362A TW106114851A TW106114851A TW201843362A TW 201843362 A TW201843362 A TW 201843362A TW 106114851 A TW106114851 A TW 106114851A TW 106114851 A TW106114851 A TW 106114851A TW 201843362 A TW201843362 A TW 201843362A
Authority
TW
Taiwan
Prior art keywords
fiber
antibacterial agent
item
patent application
scope
Prior art date
Application number
TW106114851A
Other languages
Chinese (zh)
Inventor
柯達
簡稚珉
安大中
陳威宏
Original Assignee
財團法人紡織產業綜合研究所
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 財團法人紡織產業綜合研究所 filed Critical 財團法人紡織產業綜合研究所
Priority to TW106114851A priority Critical patent/TW201843362A/en
Priority to CN201711282665.6A priority patent/CN108796647A/en
Publication of TW201843362A publication Critical patent/TW201843362A/en

Links

Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/10Other agents for modifying properties
    • D01F1/103Agents inhibiting growth of microorganisms
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/20Compounding polymers with additives, e.g. colouring
    • C08J3/22Compounding polymers with additives, e.g. colouring using masterbatch techniques
    • C08J3/226Compounding polymers with additives, e.g. colouring using masterbatch techniques using a polymer as a carrier
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/28Formation of filaments, threads, or the like while mixing different spinning solutions or melts during the spinning operation; Spinnerette packs therefor
    • D01D5/30Conjugate filaments; Spinnerette packs therefor
    • D01D5/34Core-skin structure; Spinnerette packs therefor
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F8/00Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
    • D01F8/04Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
    • D01F8/06Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyolefin as constituent
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F8/00Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
    • D01F8/04Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
    • D01F8/12Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyamide as constituent
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F8/00Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
    • D01F8/04Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers
    • D01F8/14Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from synthetic polymers with at least one polyester as constituent
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2367/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2377/00Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2423/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2467/00Characterised by the use of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2477/00Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Textile Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Multicomponent Fibers (AREA)
  • Artificial Filaments (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)

Abstract

A method of fabricating fiber masterbatch and fiber are provided. The method of fabricating fiber masterbatch includes wet grinding an additive and an antibacterial agent, and then heating and mixing the additive and the antibacterial agent, so the additive coats the antibacterial agent evenly. Afterwards, blending the antibacterial agent evenly coated by the additive with a polymer substrate to form the fiber masterbatch, wherein the antibacterial agent is dispersed evenly in the polymer substrate.

Description

纖維母粒的製造方法及纖維Manufacturing method of fiber masterbatch and fiber

本發明是有關於一種纖維母粒的製造方法及纖維,且特別是有關於一種使用較低含量的抗菌劑即可有效地達成抗菌機制之纖維母粒的製造方法及纖維。The present invention relates to a method and a fiber for manufacturing a fiber masterbatch, and more particularly, to a method and a fiber for manufacturing a fiber masterbatch that can effectively achieve an antibacterial mechanism by using a relatively low content of an antibacterial agent.

隨著生活水準的提升,人類對於居家環境與個人衛生的要求也越來提高。近年來,已開發各種具有抗菌功效的商品,且產品的抗菌功能性為業界不斷創新與發展的主要目標。在各種具有抗菌作用的產品中,抗菌纖維為受到高度重視的商品之一,其機制主要是使纖維含有抗菌劑進而使纖維具有抗菌特性。With the improvement of living standards, human beings' requirements for home environment and personal hygiene are also increasing. In recent years, various antibacterial products have been developed, and the antibacterial functionality of the products is the main goal of continuous innovation and development in the industry. Among various products with antibacterial effect, antibacterial fiber is one of the products that are highly valued. The mechanism is mainly to make the fiber contain an antibacterial agent so as to make the fiber have antibacterial properties.

在習知的抗菌纖維製程中,所使用的抗菌劑粒徑約為900 nm,在纖維有效濃度較高(約為0.9 wt%)時,才能夠有效地達成滅菌機制。然而,若需達到較高的纖維有效濃度,則需使用較大量的抗菌劑,因此,導致抗菌纖維的成本提高。基於上述,如何在較低的纖維有效濃度下仍能夠有效地達成滅菌機制,減少滅菌劑用量,進而降低抗菌纖維成本,為目前所需研究的重要課題。In the conventional antibacterial fiber manufacturing process, the particle size of the antibacterial agent used is about 900 nm, and the sterilization mechanism can be effectively achieved only when the effective fiber concentration is high (about 0.9 wt%). However, if a higher effective fiber concentration is required, a larger amount of antibacterial agent needs to be used, and therefore, the cost of the antibacterial fiber is increased. Based on the above, how to effectively achieve a sterilization mechanism at a lower effective fiber concentration, reduce the amount of sterilant, and thus reduce the cost of antibacterial fibers, is an important subject for current research.

本發明提供一種纖維母粒的製造方法及纖維,使用較低含量的抗菌劑即可有效地達成抗菌機制。The invention provides a method and a fiber for manufacturing a fiber masterbatch, and an antibacterial mechanism can be effectively achieved by using a low content of an antibacterial agent.

本發明的纖維母粒的製造方法包括以下步驟。將助劑及抗菌劑進行濕式研磨,再將助劑及抗菌劑加熱攪拌,以使助劑均勻包覆抗菌劑。之後,將經助劑均勻包覆的抗菌劑與高分子基材進行混練,以形成纖維母粒,其中經助劑均勻包覆的抗菌劑均勻分散於高分子基材中。The method for producing a fiber masterbatch of the present invention includes the following steps. The auxiliary agent and the antibacterial agent are wet-ground, and the auxiliary agent and the antibacterial agent are heated and stirred to uniformly coat the auxiliary agent with the antibacterial agent. After that, the antibacterial agent uniformly coated with the auxiliary agent is mixed with the polymer base material to form a fiber masterbatch, and the antibacterial agent uniformly coated with the auxiliary agent is uniformly dispersed in the polymer base material.

在本發明的一實施例中,進行濕式研磨後,抗菌劑的粒徑為200 nm至300 nm。In one embodiment of the present invention, the particle size of the antibacterial agent is 200 nm to 300 nm after wet grinding.

在本發明的一實施例中,以30℃至150℃的溫度對助劑及抗菌劑進行加熱攪拌步驟。In an embodiment of the present invention, the auxiliary agent and the antibacterial agent are heated and stirred at a temperature of 30 ° C. to 150 ° C.

在本發明的一實施例中,加熱攪拌步驟的攪拌速率為30 rpm至3000 rpm,且攪拌時間為100分鐘至140分鐘。In an embodiment of the present invention, the stirring rate of the heating and stirring step is 30 rpm to 3000 rpm, and the stirring time is 100 minutes to 140 minutes.

在本發明的一實施例中,以纖維母粒的總重量計,抗菌劑的含量為0.3 wt%至30 wt%,助劑的含量為0.1 wt%至3 wt%。In an embodiment of the present invention, based on the total weight of the fiber masterbatch, the content of the antibacterial agent is 0.3 wt% to 30 wt%, and the content of the auxiliary agent is 0.1 wt% to 3 wt%.

在本發明的一實施例中,高分子基材包括聚醯胺類樹脂、聚烯烴類樹脂、聚酯類樹脂或其組合。In one embodiment of the present invention, the polymer substrate includes a polyamide resin, a polyolefin resin, a polyester resin, or a combination thereof.

在本發明的一實施例中,助劑包括聚醚矽氧烷共聚合物、聚丙烯酸鈉鹽溶液及具有環氧乙烷基的非離子型聚醚溶液中的至少兩者。In one embodiment of the present invention, the auxiliary agent includes at least two of a polyether siloxane copolymer, a sodium polyacrylate solution, and a non-ionic polyether solution having an ethylene oxide group.

在本發明的一實施例中,抗菌劑是由有機物及無機物組成。In one embodiment of the present invention, the antibacterial agent is composed of an organic substance and an inorganic substance.

在本發明的一實施例中,有機物包括吡啶類聚合物、銨鹽類聚合物、磺醯胺類聚合物、二碘甲基類聚合物、咪唑類聚合物、雙胍類聚合物或其組合。In an embodiment of the present invention, the organic substance includes a pyridine polymer, an ammonium salt polymer, a sulfonamide polymer, a diiodomethyl polymer, an imidazole polymer, a biguanide polymer, or a combination thereof.

在本發明的一實施例中,無機物包括鋅的氧化物、矽的氧化物、鈣的氧化物或其組合。In one embodiment of the present invention, the inorganic substance includes zinc oxide, silicon oxide, calcium oxide, or a combination thereof.

本發明的纖維使用含有抗菌劑的纖維母粒經由芯鞘型複合紡絲製程所製成,其中含有抗菌劑的纖維母粒是由上述纖維母粒的製造方法製成。The fiber of the present invention is made by using a fiber-sheath composite fiber containing an antibacterial agent through a core-sheath composite spinning process, and the fiber mother particle containing the antibacterial agent is made by the above-mentioned method for producing a fiber mother particle.

在本發明的一實施例中,纖維的芯鞘比例為70/30至80/20。In one embodiment of the present invention, the core-sheath ratio of the fiber is 70/30 to 80/20.

在本發明的一實施例中,抗菌劑在纖維中的纖維有效濃度為0.1 wt%至0.2 wt%。In an embodiment of the present invention, the effective fiber concentration of the antibacterial agent in the fiber is 0.1 wt% to 0.2 wt%.

在本發明的一實施例中,纖維的纖維細度為70丹/24條。In one embodiment of the present invention, the fiber fineness of the fibers is 70 deniers / 24 strands.

在本發明的一實施例中,纖維母粒構成所述纖維的鞘層。In one embodiment of the present invention, the fiber masterbatch constitutes a sheath of the fiber.

基於上述,在本發明纖維母粒的製造方法中,將助劑及抗菌劑進行濕式研磨,進行濕式研磨後,抗菌劑的粒徑為200 nm至300 nm。如此一來,將上述纖維母粒製成芯鞘型抗菌纖維時,能夠使細化的抗菌劑均勻分散於纖維的鞘層,因此,抗菌劑在纖維中的纖維有效濃度為0.1 wt%至0.2 wt%,仍能夠有效地達成抗菌機制,進而減少滅菌劑用量,以降低抗菌纖維成本。Based on the above, in the method for producing a fiber masterbatch according to the present invention, the auxiliary agent and the antibacterial agent are wet-milled, and after the wet grinding, the particle diameter of the antibacterial agent is 200 nm to 300 nm. In this way, when the fiber masterbatch is made into a core-sheath type antibacterial fiber, the refined antibacterial agent can be uniformly dispersed in the sheath layer of the fiber. Therefore, the effective fiber concentration of the antibacterial agent in the fiber is 0.1 wt% to 0.2 wt%, still can effectively achieve the antibacterial mechanism, and then reduce the amount of sterilant to reduce the cost of antibacterial fibers.

為讓本發明的上述特徵和優點能更明顯易懂,下文特舉實施例,並配合所附圖式作詳細說明如下。In order to make the above features and advantages of the present invention more comprehensible, embodiments are hereinafter described in detail with reference to the accompanying drawings.

圖1為依照本發明一實施例之纖維母粒的製造方法之流程示意圖。以下,將以圖1詳細描述依照本發明一實施例之纖維母粒的製造方法。FIG. 1 is a schematic flowchart of a method for manufacturing a fiber masterbatch according to an embodiment of the present invention. Hereinafter, a method for manufacturing a fiber masterbatch according to an embodiment of the present invention will be described in detail with reference to FIG. 1.

請參照圖1。首先,進行步驟S110,將助劑及抗菌劑進行濕式研磨,再將助劑及抗菌劑加熱攪拌,以使助劑均勻包覆抗菌劑。此處所述的「均勻包覆」,較佳例如是使助劑於抗菌劑的表面上形成厚度大致上具有均一性的披覆層。Please refer to Figure 1. First, step S110 is performed, the auxiliary agent and the antibacterial agent are wet-milled, and then the auxiliary agent and the antibacterial agent are heated and stirred to uniformly coat the auxiliary agent with the antibacterial agent. The "uniform coating" described herein is preferably a coating layer having an approximately uniform thickness on the surface of the antibacterial agent.

在本實施例中,抗菌劑例如是由有機物及無機物組成,其中有機物可包括吡啶類聚合物、銨鹽類聚合物、磺醯胺類聚合物、二碘甲基類聚合物、咪唑類聚合物、雙胍類聚合物或其組合,無機物可包括鋅的氧化物、矽的氧化物、鈣的氧化物或其組合。然而,本發明並不以此為限。另一方面,助劑可包括聚醚矽氧烷共聚合物(作用為潤濕劑,TEGO-270)、聚丙烯酸鈉鹽溶液(作用為分散、潤濕及降黏,TEGO-715)及具有環氧乙烷基的非離子型聚醚溶液(作用為分散、潤濕及降黏,TEGO-760)中的至少兩者,其中聚醚矽氧烷共聚合物例如是可溶於有機溶劑(例如是乙醇)的粉體。In this embodiment, the antibacterial agent is composed of an organic substance and an inorganic substance. The organic substance may include a pyridine polymer, an ammonium salt polymer, a sulfonamide polymer, a diiodomethyl polymer, and an imidazole polymer. , Biguanide polymers or a combination thereof, the inorganic substance may include zinc oxide, silicon oxide, calcium oxide or a combination thereof. However, the present invention is not limited to this. On the other hand, auxiliaries may include polyether siloxane copolymers (acting as wetting agents, TEGO-270), polyacrylic acid sodium salt solution (acting as dispersion, wetting, and viscosity reduction, TEGO-715) and having At least two of ethylene oxide-based non-ionic polyether solutions (dispersing, wetting, and viscosity reduction, TEGO-760). The polyether siloxane copolymer is, for example, soluble in organic solvents ( For example, ethanol) powder.

在步驟S110中,助劑可對於粉體進行潤濕及脫泡作用,以獲得更分散穩定的粒子。藉由步驟S110加入助劑的濕式研磨,可改善粉體浸入時間、提高研磨效率,同時減少氣泡產生及優化研磨效果。更詳細而言,可使用抗菌劑、水及助劑作為研磨配方以進行濕式研磨,其中以研磨配方的總重量計,抗菌劑的添加量例如是20 wt%,水的添加量例如是77%,助劑的添加量例如是3 wt%。具點而言,助劑可採用配方1:聚醚矽氧烷共聚合物2 wt%及聚丙烯酸鈉鹽溶液1 wt%;或者,配方2:聚丙烯酸鈉鹽溶液1 wt%及具有環氧乙烷基的非離子型聚醚溶液2 wt%。將上述含有抗菌劑、水及助劑的研磨配方在25℃下進行濕式研磨約30分鐘後,可使抗菌劑的粒徑由約900 nm降至例如200 nm至300 nm。In step S110, the auxiliary agent can perform wetting and defoaming on the powder to obtain more dispersed and stable particles. The wet grinding with the auxiliary agent added in step S110 can improve the powder immersion time, improve the grinding efficiency, and at the same time reduce the generation of air bubbles and optimize the grinding effect. In more detail, an antibacterial agent, water, and an auxiliary agent can be used as a grinding formula for wet grinding. The total amount of the antibacterial agent is 20 wt% based on the total weight of the grinding formula, and the amount of water is 77. %, And the additive amount is, for example, 3 wt%. To be specific, the auxiliary agent can use Formula 1: polyether siloxane copolymer 2 wt% and polyacrylate sodium salt solution 1 wt%; or Formula 2: polyacrylate sodium salt solution 1 wt% and epoxy Ethyl-based non-ionic polyether solution 2 wt%. After the above grinding formula containing the antibacterial agent, water, and auxiliary agent is wet-milled at 25 ° C. for about 30 minutes, the particle size of the antibacterial agent can be reduced from about 900 nm to, for example, 200 nm to 300 nm.

在步驟S110中,例如是以30℃至150℃的溫度對助劑及抗菌劑進行加熱攪拌步驟,加熱攪拌步驟的攪拌速率例如是30 rpm至3000 rpm,且攪拌時間例如是100分鐘至140分鐘。藉由步驟S110的加熱攪拌步驟,除了能夠將抗菌漿料的水分蒸乾之外,更能夠使助劑均勻披覆於抗菌劑表面,以達成潤滑分散的效果。在進行圖1的步驟S110之後,進行步驟S120混練造粒之前,可對經助劑均勻包覆的抗菌劑進行物料乾燥製程,其中乾燥時間例如是12小時至24小時(隔夜乾燥),乾燥溫度例如是80℃至100℃,較佳為85℃。In step S110, for example, the auxiliary agent and the antibacterial agent are heated and stirred at a temperature of 30 ° C to 150 ° C. The stirring rate of the heating and stirring step is, for example, 30 rpm to 3000 rpm, and the stirring time is, for example, 100 minutes to 140 minutes. . Through the heating and stirring step of step S110, in addition to being able to evaporate the moisture of the antibacterial slurry, the auxiliary agent can be evenly coated on the surface of the antibacterial agent to achieve the effect of lubricating and dispersing. After step S110 in FIG. 1 and before step S120 for kneading and granulation, a material drying process may be performed on the antibacterial agent uniformly coated with the auxiliary agent, wherein the drying time is, for example, 12 hours to 24 hours (overnight drying), and the drying temperature For example, it is 80 ° C to 100 ° C, and preferably 85 ° C.

之後,請繼續參照圖1,進行步驟S120,將經助劑均勻包覆的抗菌劑與高分子基材進行混練,以形成纖維母粒,其中經助劑均勻包覆的抗菌劑均勻分散於高分子基材中。After that, please continue to refer to FIG. 1 and perform step S120 to knead the antibacterial agent uniformly coated with the auxiliary agent and the polymer base material to form a fiber masterbatch, in which the antibacterial agent uniformly coated with the auxiliary agent is uniformly dispersed in high Molecular substrate.

在本實施例中,高分子基材可包括聚醯胺類樹脂、聚烯烴類樹脂、聚酯類樹脂或其組合。然而,本發明並不以此為限。另外,混練溫度例如是220℃至240℃。經混練後所形成之纖維母粒的直徑例如是2 mm至3 mm,長度例如是2.5 mm至3.5 mm。以纖維母粒的總重量計,抗菌劑的含量例如是0.3 wt%至30 wt%,所述助劑的含量例如是0.1 wt%至3 wt%。In this embodiment, the polymer substrate may include a polyamide-based resin, a polyolefin-based resin, a polyester-based resin, or a combination thereof. However, the present invention is not limited to this. The kneading temperature is, for example, 220 ° C to 240 ° C. The fiber masterbatch formed after kneading has a diameter of, for example, 2 mm to 3 mm, and a length of, for example, 2.5 mm to 3.5 mm. The content of the antibacterial agent is, for example, 0.3 wt% to 30 wt% based on the total weight of the fiber masterbatch, and the content of the auxiliary agent is, for example, 0.1 wt% to 3 wt%.

本發明亦提出一種纖維,使用含有抗菌劑的纖維母粒經由芯鞘型複合紡絲製程所製成,其中纖維母粒是由上述實施例之纖維母粒的製造方法製成。更詳細而言,含有抗菌劑的纖維母粒構成纖維的鞘層,常規耐隆則構成纖維的芯層,纖維的芯鞘比例例如是70/30至80/20,纖維細度例如是70丹/24條,且抗菌劑在纖維中的纖維有效濃度例如是0.1 wt%至0.2 wt%。The present invention also proposes a fiber, which is prepared by using a fiber-sheath-type composite spinning process using fiber masterbatch containing an antibacterial agent, wherein the fiber masterbatch is made by the manufacturing method of the fiber masterbatch of the above embodiment. In more detail, the fiber masterbatch containing the antibacterial agent constitutes the sheath layer of the fiber, and the conventional resistant nylon constitutes the core layer of the fiber. 24, and the effective fiber concentration of the antibacterial agent in the fiber is, for example, 0.1 wt% to 0.2 wt%.

由於在上述實施例之纖維母粒的製造方法中,將助劑及抗菌劑進行濕式研磨,以使濕式研磨後抗菌劑的粒徑由約900 nm降低為例如200 nm至300 nm,因此,能夠使細化的抗菌劑均勻地分散於纖維的鞘層。如此一來,即使抗菌劑在纖維中的纖維有效濃度例如是低至0.1 wt%至0.2 wt%,仍能夠有效地達成抗菌機制,進而減少滅菌劑用量,以降低抗菌纖維成本。In the manufacturing method of the fiber masterbatch of the above embodiment, the auxiliary agent and the antibacterial agent are wet-ground so that the particle size of the antibacterial agent after wet grinding is reduced from about 900 nm to, for example, 200 nm to 300 nm. It is possible to uniformly disperse the fine antibacterial agent in the sheath of the fiber. In this way, even if the effective fiber concentration of the antibacterial agent in the fiber is, for example, as low as 0.1 wt% to 0.2 wt%, the antibacterial mechanism can still be effectively achieved, thereby reducing the amount of sterilant and reducing the cost of the antibacterial fiber.

在本實施例中,抗菌纖維的紡絲條件如下:擠壓機溫度例如是250℃/255℃/260℃/265℃,箱體溫度例如是265℃,紡絲泵例如是19.2 cc/rpm,紡絲速度例如是3000 m/min,延伸倍率例如是2.8。In this embodiment, the spinning conditions of the antibacterial fiber are as follows: the extruder temperature is, for example, 250 ° C / 255 ° C / 260 ° C / 265 ° C, the box temperature is, for example, 265 ° C, and the spinning pump is, for example, 19.2 cc / rpm, The spinning speed is, for example, 3000 m / min, and the draw ratio is, for example, 2.8.

以下,藉由實驗例來詳細說明上述實施例所提出之纖維母粒的製造方法及纖維。然而,下述實驗例並非用以限制本發明。實驗例 Hereinafter, the manufacturing method and fiber of the fiber masterbatch proposed by the said Example are demonstrated in detail by an experimental example. However, the following experimental examples are not intended to limit the present invention. Experimental example

為了證明本發明所提出的纖維母粒的製造方法基於濕式研磨製程降低抗菌劑的粒徑,而使後續製成的纖維在抗菌劑纖維有效濃度較低的情況下,也能夠有效地達成抗菌機制,以下特別作此實驗例。In order to prove that the manufacturing method of the fiber masterbatch according to the present invention reduces the particle size of the antibacterial agent based on the wet grinding process, so that the subsequent fibers can effectively achieve the antibacterial effect even when the effective concentration of the antibacterial fiber is low. Mechanism, this experimental example is made below.

必須說明的是,由於纖維母粒的製造方法已於上文中詳細地描述,因此,下文中有關纖維母粒的製備,為求方便說明故省略製備細節之敘述。抗菌纖維母粒的製備 It must be noted that, since the manufacturing method of the fiber masterbatch has been described in detail above, the preparation of the fiber masterbatch is hereinafter described, and the details of the preparation are omitted for the sake of convenience. Preparation of antibacterial fiber masterbatch

以抗菌劑、水及助劑作為研磨配方以進行濕式研磨,其中以研磨配方的總重量計,抗菌劑的添加量為20 wt%,水的添加量為77%,助劑的添加量為3 wt%(配方1:聚醚矽氧烷共聚合物2 wt%及聚丙烯酸鈉鹽溶液1 wt%;配方2:聚丙烯酸鈉鹽溶液1 wt%及具有環氧乙烷基的非離子型聚醚溶液2 wt%)。將上述含有抗菌劑、水及助劑的研磨配方在25℃下進行濕式研磨約30分鐘後,可使抗菌劑的粒徑由約955.5 nm降至約217 nm。之後,再將助劑及抗菌劑於90℃的攪拌溫度下以3000 rpm的攪拌速率加熱攪拌2小時,並於85℃的乾燥溫度下乾燥24小時,最後於220℃至240℃的混練溫度下進行混練,以形成纖維母粒。可紡性 評估 The antibacterial agent, water and auxiliary agent are used as a grinding formula for wet grinding. The total amount of the antibacterial agent is 20 wt%, the added amount of water is 77%, and the additive amount is based on the total weight of the grinding formula. 3 wt% (Formulation 1: Polyether siloxane copolymer 2 wt% and polyacrylate sodium salt solution 1 wt%; Formula 2: Polyacrylate sodium salt solution 1 wt% and non-ionic type with ethylene oxide group Polyether solution 2 wt%). After the above grinding formula containing the antibacterial agent, water, and auxiliary agent is wet-milled at 25 ° C. for about 30 minutes, the particle size of the antibacterial agent can be reduced from about 955.5 nm to about 217 nm. After that, the auxiliary agent and the antibacterial agent were heated and stirred at a stirring rate of 3000 rpm for 2 hours at a stirring temperature of 90 ° C, and then dried at a drying temperature of 85 ° C for 24 hours, and finally at a mixing temperature of 220 ° C to 240 ° C Kneading is performed to form a fiber masterbatch. Spinnability evaluation

對上述配方1及配方2的抗菌纖維母粒進行纖維紡絲,並量測其可紡性。配方1在一個小時的可紡性評估中,有3-5次的飄斷絲,而配方2只有1-2次飄斷絲。因此,以下將針對配方2的抗菌纖維母粒進行有關抗菌性的進一步評估。抗菌纖維有效濃度、纖維強度、纖維伸度、紡絲作業性及抗菌性評估 The antibacterial fiber masterbatches of Formula 1 and Formula 2 were subjected to fiber spinning, and their spinnability was measured. In the one-hour spinnability evaluation of Formula 1, there were 3-5 broken yarns, while Formula 2 had only 1-2 broken yarns. Therefore, the antibacterial properties of the antibacterial fiber masterbatch of Formula 2 will be further evaluated below. Evaluation of effective concentration of antibacterial fiber, fiber strength, fiber elongation, spinning workability and antibacterial property

依據以下表1中所列出的各組分與條件進行纖維紡絲,製成實例1至實例2及比較例1至比較例7的纖維,並將所製成的纖維進行抗菌纖維有效濃度、纖維強度、纖維伸度、紡絲作業性及抗菌性評估,評估結果列於表1中。Fiber spinning was performed according to the components and conditions listed in Table 1 below to prepare the fibers of Examples 1 to 2 and Comparative Examples 1 to 7, and the prepared fibers were subjected to an effective concentration of antibacterial fibers, The fiber strength, fiber elongation, spinning workability, and antibacterial properties were evaluated. The evaluation results are shown in Table 1.

抗菌纖維有效濃度藉由以下列式1計算。纖維強伸度是以ASTM 2256標準測試方式進行。紡絲作業性的判定:一個小時內之飄斷絲次數(◎:0次,○:1-2次,△:3-5次,X:6次以上)。抗菌性評估則是以AATCC-100標準測試方式偵測纖維對於金黃色葡萄球菌的滅菌率(%),並藉由以下式2計算抗菌率,其中立即沖刷的菌數是指對照組與樣品組和菌液一經接觸(培養0秒)就立即沖刷的菌數,而培養後的菌數是指樣品組培養18小時至24小時的菌數。(式1)(式2) 1 The effective concentration of the antibacterial fiber is calculated by the following formula 1. The fiber elongation is performed in accordance with the ASTM 2256 standard test method. Judgment of spinning workability: Number of broken yarns in one hour ((: 0 times, ○: 1-2 times, △: 3-5 times, X: 6 times or more). The antibacterial evaluation is based on the AATCC-100 standard test method to detect the sterilization rate (%) of the fiber against Staphylococcus aureus, and calculate the antibacterial rate by the following formula 2. The number of bacteria immediately washed out refers to the control group and the sample group The number of bacteria flushed immediately upon contact with the bacterial solution (0 second incubation), and the number of bacteria after culture refers to the number of bacteria in the sample group that is cultured for 18 to 24 hours. (Formula 1) (Formula 2) Table 1

如上方表1所示,實例1及實例2使用本發明之纖維母粒的製造方法製成的纖維母粒以製備芯鞘型複合纖維,由於經濕式研磨後的抗菌劑粒徑降至217.1 nm,以均勻分散於纖維的鞘層,因此,在纖維有效濃度低至0.12%或0.18%的情況下,仍能夠達到99.8及95.6%的滅菌率,有效地達成抗菌機制。如此一來,能夠減少滅菌劑用量,進而降低抗菌纖維成本。As shown in Table 1 above, Example 1 and Example 2 use the fiber masterbatch produced by the fiber masterbatch manufacturing method of the present invention to prepare a core-sheath composite fiber. The particle size of the antibacterial agent after wet grinding is reduced to 217.1 nm is uniformly dispersed in the sheath of the fiber. Therefore, even when the effective fiber concentration is as low as 0.12% or 0.18%, the sterilization rates of 99.8 and 95.6% can still be achieved, and the antibacterial mechanism can be effectively achieved. In this way, the amount of sterilant can be reduced, thereby reducing the cost of antibacterial fibers.

相較之下,比較例1所製成的纖維為單組份纖維,因此,抗菌劑不會均勻分散於纖維的表面。如此一來,即使抗菌劑的粒徑降至217.1 nm,在纖維有效濃度較低的情況下,無法有效地達成抗菌機制,抗菌率相當低。比較例2所製成的纖維為單組份纖維,因此,即使抗菌劑的粒徑降至217.1 nm,仍需要相當高的纖維有效濃度,才能夠達成抗菌機制,故無法解決抗菌纖維成本高昂的問題。In contrast, the fiber made in Comparative Example 1 was a single-component fiber, and therefore, the antibacterial agent was not uniformly dispersed on the surface of the fiber. In this way, even if the particle size of the antibacterial agent is reduced to 217.1 nm, when the effective fiber concentration is low, the antibacterial mechanism cannot be effectively achieved, and the antibacterial rate is quite low. The fiber made in Comparative Example 2 is a single-component fiber. Therefore, even if the particle size of the antibacterial agent is reduced to 217.1 nm, a relatively high effective fiber concentration is still needed to achieve the antibacterial mechanism, so the cost of antibacterial fibers cannot be solved. problem.

此外,如表1所示,由於比較例3及比較例4的抗菌劑粒徑為955.5 nm,其中並未實施本發明的濕式研磨製成以使抗菌劑粒徑降至217.1 nm,因此,即使同為芯鞘型複合纖維,較大粒徑的抗菌劑不易均勻分散於纖維的鞘層,故抗菌率相當低,無法達成抗菌機制。In addition, as shown in Table 1, since the particle size of the antibacterial agent in Comparative Examples 3 and 4 was 955.5 nm, and the wet grinding of the present invention was not performed to reduce the particle size of the antibacterial agent to 217.1 nm, Even if they are both core-sheath type composite fibers, antibacterial agents with larger particle diameters are not easily dispersed uniformly in the sheath of the fibers, so the antibacterial rate is quite low, and an antibacterial mechanism cannot be achieved.

另一方面,本發明的抗菌纖維不但是芯鞘型複合纖維,且芯鞘比例較佳為70/30至80/20,才能夠在低抗菌劑用量的情況下有效地達成抗菌機制。如表1所示,比較例5至比較例7的芯鞘比例並非70/30至80/20,因此,比較例5及比較例6的抗菌率相當低,比較例7則是基於芯鞘比例過於懸殊(90/10),鞘層無法包覆芯層,造成高分子熔體在出紡口後完全無法成絲。On the other hand, the antibacterial fiber of the present invention is not only a core-sheath type composite fiber, but also the core-sheath ratio is preferably 70/30 to 80/20, so that the antibacterial mechanism can be effectively achieved with a low amount of antibacterial agent. As shown in Table 1, the core-sheath ratio of Comparative Examples 5 to 7 is not 70/30 to 80/20. Therefore, the antibacterial rate of Comparative Examples 5 and 6 is quite low, and Comparative Example 7 is based on the core-sheath ratio. Too much disparity (90/10), the sheath layer cannot cover the core layer, resulting in the polymer melt being unable to form silk after spinning out.

基於上述,在本發明纖維母粒的製造方法中,將助劑及抗菌劑進行濕式研磨,進行濕式研磨後,抗菌劑的粒徑為200 nm至300 nm。如此一來,將上述纖維母粒製成鞘比例為70/30至80/20的抗菌芯鞘型複合纖維時,增加纖維的比表面積,能夠使細化的抗菌劑均勻分散於纖維的鞘層,因此,抗菌劑在纖維中的纖維有效濃度為0.1 wt%至0.2 wt%,仍能夠有效地達成抗菌機制,進而減少滅菌劑用量,以降低抗菌纖維成本。Based on the above, in the method for producing a fiber masterbatch according to the present invention, the auxiliary agent and the antibacterial agent are wet-milled, and after the wet grinding, the particle diameter of the antibacterial agent is 200 nm to 300 nm. In this way, when the above-mentioned fiber masterbatch is made into an antibacterial core-sheath composite fiber with a sheath ratio of 70/30 to 80/20, the specific surface area of the fiber is increased, and the refined antibacterial agent can be uniformly dispersed in the sheath of the fiber Therefore, the effective fiber concentration of the antibacterial agent in the fiber is 0.1 wt% to 0.2 wt%, and the antibacterial mechanism can still be effectively achieved, thereby reducing the amount of sterilant and reducing the cost of the antibacterial fiber.

雖然本發明已以實施例揭露如上,然其並非用以限定本發明,任何所屬技術領域中具有通常知識者,在不脫離本發明的精神和範圍內,當可作些許的更動與潤飾,故本發明的保護範圍當視後附的申請專利範圍所界定者為準。Although the present invention has been disclosed as above with the examples, it is not intended to limit the present invention. Any person with ordinary knowledge in the technical field can make some modifications and retouching without departing from the spirit and scope of the present invention. The protection scope of the present invention shall be determined by the scope of the attached patent application.

S110、S120‧‧‧步驟S110, S120‧‧‧step

圖1為依照本發明一實施例之纖維母粒的製造方法之流程示意圖。FIG. 1 is a schematic flowchart of a method for manufacturing a fiber masterbatch according to an embodiment of the present invention.

Claims (15)

一種纖維母粒的製造方法,包括: 將助劑及抗菌劑進行濕式研磨,再將所述助劑及所述抗菌劑加熱攪拌,以使所述助劑均勻包覆所述抗菌劑;以及 將經所述助劑均勻包覆的所述抗菌劑與高分子基材進行混練,以形成所述纖維母粒,其中經所述助劑均勻包覆的所述抗菌劑均勻分散於所述高分子基材中。A method for manufacturing a fiber masterbatch, comprising: wet grinding an auxiliary agent and an antibacterial agent, and heating and stirring the auxiliary agent and the antibacterial agent so that the auxiliary agent uniformly covers the antibacterial agent; and The antibacterial agent uniformly coated with the auxiliary agent is mixed with a polymer base material to form the fiber masterbatch, and the antibacterial agent uniformly coated with the auxiliary agent is uniformly dispersed in the polymer. Molecular substrate. 如申請專利範圍第1項所述的纖維母粒的製造方法,其中進行濕式研磨後,所述抗菌劑的粒徑為200 nm至300 nm。The method for manufacturing a fiber masterbatch according to item 1 of the scope of the patent application, wherein the particle size of the antibacterial agent is 200 nm to 300 nm after wet grinding. 如申請專利範圍第1項所述的纖維母粒的製造方法,其中以30℃至150℃的溫度對所述助劑及所述抗菌劑進行加熱攪拌步驟。The method for manufacturing a fiber masterbatch according to item 1 of the scope of patent application, wherein the auxiliary agent and the antibacterial agent are heated and stirred at a temperature of 30 ° C to 150 ° C. 如申請專利範圍第3項所述的纖維母粒的製造方法,其中所述加熱攪拌步驟的攪拌速率為30 rpm至3000 rpm,且攪拌時間為100分鐘至140分鐘。The method for manufacturing a fiber masterbatch according to item 3 of the scope of the patent application, wherein the stirring rate of the heating and stirring step is 30 rpm to 3000 rpm, and the stirring time is 100 minutes to 140 minutes. 如申請專利範圍第1項所述的纖維母粒的製造方法,其中以纖維母粒的總重量計,所述抗菌劑的含量為0.3 wt%至30 wt%,所述助劑的含量為0.1 wt%至3 wt%。The method for manufacturing a fiber masterbatch according to item 1 of the scope of the patent application, wherein the content of the antibacterial agent is 0.3 wt% to 30 wt% and the content of the auxiliary agent is 0.1 based on the total weight of the fiber masterbatch. wt% to 3 wt%. 如申請專利範圍第1項所述的纖維母粒的製造方法,其中所述高分子基材包括聚醯胺類樹脂、聚烯烴類樹脂、聚酯類樹脂或其組合。The method for manufacturing a fiber masterbatch according to item 1 of the scope of the patent application, wherein the polymer substrate includes a polyamide resin, a polyolefin resin, a polyester resin, or a combination thereof. 如申請專利範圍第1項所述的纖維母粒的製造方法,其中所述助劑包括聚醚矽氧烷共聚合物、聚丙烯酸鈉鹽溶液及具有環氧乙烷基的非離子型聚醚溶液中的至少兩者。The method for manufacturing a fiber masterbatch according to item 1 of the patent application scope, wherein the auxiliary agent includes a polyether siloxane copolymer, a sodium polyacrylate solution, and a non-ionic polyether having an ethylene oxide group. At least two of the solutions. 如申請專利範圍第1項所述的纖維母粒的製造方法,其中所述抗菌劑是由有機物及無機物組成。The method for producing a fiber masterbatch according to item 1 of the scope of patent application, wherein the antibacterial agent is composed of an organic substance and an inorganic substance. 如申請專利範圍第8項所述的纖維母粒的製造方法,其中所述有機物包括吡啶類聚合物、銨鹽類聚合物、磺醯胺類聚合物、二碘甲基類聚合物、咪唑類聚合物、雙胍類聚合物或其組合。The method for manufacturing a fiber masterbatch according to item 8 of the scope of the patent application, wherein the organic substance includes a pyridine polymer, an ammonium salt polymer, a sulfonamide polymer, a diiodomethyl polymer, and an imidazole Polymers, biguanide polymers, or combinations thereof. 如申請專利範圍第8項所述的纖維母粒的製造方法,其中所述無機物包括鋅的氧化物、矽的氧化物、鈣的氧化物或其組合。The method for manufacturing a fiber masterbatch according to item 8 of the scope of patent application, wherein the inorganic substance includes zinc oxide, silicon oxide, calcium oxide, or a combination thereof. 一種纖維,使用含有抗菌劑的纖維母粒經由芯鞘型複合紡絲製程所製成,其中所述纖維母粒是由如申請專利範圍第1項至第10項中任一項所述的纖維母粒的製造方法製成。A fiber manufactured by using a core-sheath composite spinning process using a fiber masterbatch containing an antibacterial agent, wherein the fiber masterbatch is a fiber according to any one of claims 1 to 10 It is made by the manufacturing method of a masterbatch. 如申請專利範圍第11項所述的纖維,其中所述纖維的芯鞘比例為70/30至80/20。The fiber according to item 11 of the scope of patent application, wherein the core-sheath ratio of the fiber is 70/30 to 80/20. 如申請專利範圍第11項所述的纖維,其中所述抗菌劑在所述纖維中的纖維有效濃度為0.1 wt%至0.2 wt%。The fiber according to item 11 of the scope of patent application, wherein the effective fiber concentration of the antibacterial agent in the fiber is 0.1 wt% to 0.2 wt%. 如申請專利範圍第11項所述的纖維,其中所述纖維的纖維細度為70丹/24條。The fiber according to item 11 of the scope of patent application, wherein the fiber fineness of the fiber is 70 deniers / 24 strands. 如申請專利範圍第11項所述的纖維,其中所述纖維母粒構成所述纖維的鞘層。The fiber according to item 11 of the patent application scope, wherein the fiber masterbatch constitutes a sheath of the fiber.
TW106114851A 2017-05-04 2017-05-04 Method of fabricating fiber masterbatch and fiber TW201843362A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
TW106114851A TW201843362A (en) 2017-05-04 2017-05-04 Method of fabricating fiber masterbatch and fiber
CN201711282665.6A CN108796647A (en) 2017-05-04 2017-11-29 Method for producing fiber masterbatch and fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW106114851A TW201843362A (en) 2017-05-04 2017-05-04 Method of fabricating fiber masterbatch and fiber

Publications (1)

Publication Number Publication Date
TW201843362A true TW201843362A (en) 2018-12-16

Family

ID=64095161

Family Applications (1)

Application Number Title Priority Date Filing Date
TW106114851A TW201843362A (en) 2017-05-04 2017-05-04 Method of fabricating fiber masterbatch and fiber

Country Status (2)

Country Link
CN (1) CN108796647A (en)
TW (1) TW201843362A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110409012B (en) * 2019-07-16 2021-11-23 福建百宏聚纤科技实业有限公司 Antibacterial polyester fiber and preparation method thereof
US20230172291A1 (en) * 2020-05-15 2023-06-08 Honeywell International Inc. Methods, apparatuses, and systems for providing personal protective equipment

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1680494A (en) * 2004-04-05 2005-10-12 上海铁贤科贸有限公司 Composite powder of nano photocatalyst/Tuomalin and its preparation
KR100559405B1 (en) * 2005-06-23 2006-03-10 이민화 Antimicrobial company and its manufacturing method
CN100521943C (en) * 2006-11-20 2009-08-05 北京崇高纳米科技有限公司 Inorganic/organic nano composite antibacterial agent and its fabric product application
CN105671682B (en) * 2014-11-17 2018-08-31 北京中纺优丝特种纤维科技有限公司 A kind of copper system anti-bacterial fibre and preparation method thereof
CN104963028B (en) * 2015-07-01 2017-04-26 义乌市惠航化纤科技有限公司 Antibacterial polyester fibers and preparation method for same

Also Published As

Publication number Publication date
CN108796647A (en) 2018-11-13

Similar Documents

Publication Publication Date Title
US11459699B2 (en) Antibacterial leather, preparation method and application thereof
CN103437146B (en) Nano-fabric finishing agent and its preparation method and application
CN101255614B (en) Inorganic solid phase combination powder, masterbatch and production method, fiber and production method
CN109706533B (en) Antibacterial and mildewproof polypropylene filament and preparation method thereof
CN102618962B (en) Antibacterial polyurethane fiber and preparation method thereof
CN105694438A (en) Nano inorganic antibacterial fiber masterbatch and preparation method thereof
CN101484630A (en) Stable suspensions containing microcapsules and process for their preparation
WO2018001003A1 (en) Processing technology for polyester functional fiber
CN113005556A (en) Antibacterial synthetic fiber added with rare earth oxide and preparation method and application thereof
CN108047531A (en) A kind of antibacterial matrices and preparation method thereof
CN111041606A (en) Durable antibacterial textile fiber and preparation method thereof
CN113463270A (en) Polypropylene melt-blown non-woven fabric based on composite antibacterial electret master batch and preparation method
CN115142194A (en) A kind of graphene quantum dot antibacterial and antiviral meltblown cloth, mask and preparation method thereof
CN107141584B (en) A kind of polypropylene composite material and its application in the preparation of hydrophilic flexible non-woven fabric
TW201843362A (en) Method of fabricating fiber masterbatch and fiber
CN109505018B (en) A kind of antibacterial and anti-mite sky tea fiber and preparation method thereof
WO2017092234A1 (en) Mesoporous zirconium-phosphate loaded nano-silver antibacterial polyester fiber and method for preparation thereof
CN118685918A (en) Method for making water-repellent and anti-aging hot air nonwoven fabric
Liu et al. N-chlorination of urea-formaldehyde resin microspheres for antibacterial regenerated cellulose fibers
CN112981589B (en) Chinlon 6 filament and preparation method thereof
CN116536791A (en) Modified graphene polylactic acid antibacterial fiber and its preparation method and application
CN112853521A (en) Production method of anti-static POY (polyester pre-oriented yarn)
CN106435819A (en) Novel high-performance composite porous nanometer antibacterial fiber material adopting functionalized graphene and preparation method of novel high-performance composite porous nanometer antibacterial fiber material
Zheng et al. Thermostable ZnO/Ag@ SiO2 nanohybrid material for extraordinary antibacterial activity polyester fibers
Hou et al. Washing resistant antibacterial PET composite fibers fabricated by melt spinning