TWI296296B - - Google Patents

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TWI296296B
TWI296296B TW094103356A TW94103356A TWI296296B TW I296296 B TWI296296 B TW I296296B TW 094103356 A TW094103356 A TW 094103356A TW 94103356 A TW94103356 A TW 94103356A TW I296296 B TWI296296 B TW I296296B
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Taiwan
Prior art keywords
fiber
additive
resin
attached
wet heat
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TW094103356A
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Chinese (zh)
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TW200540309A (en
Inventor
Hisatoshi Motoda
Kouki Shigeta
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Daiwa Spinning Co Ltd
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Priority claimed from JP2004181415A external-priority patent/JP4565902B2/en
Priority claimed from JP2004183709A external-priority patent/JP4634072B2/en
Priority claimed from PCT/JP2004/011397 external-priority patent/WO2005012605A2/en
Application filed by Daiwa Spinning Co Ltd filed Critical Daiwa Spinning Co Ltd
Publication of TW200540309A publication Critical patent/TW200540309A/en
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Publication of TWI296296B publication Critical patent/TWI296296B/zh

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  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)

Description

I 1296296 九、發明說明: 【發明所屬之技術領域】 本發明係關於-種將添加物⑽er)附著於纖維表面之 添加物附著纖維、纖維構造物、纖維成形 製造方法。 汉/、寺之 【先前技術】 以往,於纖維表面附著添加物之方法,係提出於不織 布之表面以乾式法來載持粒子之後,加熱到纖維之軟化溫 度以上之溫度使得粒子附著之方法(下述專利文獻u。再 二:出了於含有粒子之水分散溶液中使得片狀或塊狀纖 -准成!物含浸、壓榨後,加熱至纖維之熔點乃至不超過纖 維炫點60。(:之溫度使得粒子附著之 2)。 者之方法(下述專利文獻 ^再者,以往以來於纖維表面附著有添加物之纖維製品, 係使用於各種用途。例如,基於研磨與潔淨化目的之纖維 或布’在潔淨化目的之纖維方面一般已眾所皆知者為用以 研磨牙齒之長絲纖維(DENTee_fi〇ss)。在工業用途上,研磨 布或研磨紙等係使用於透鏡、半導體、金屬、塑膠、陶瓷、 玻璃等各種㈣。再者於家庭帛或業務用廚房等也使用著 又,由於吸入揮發性有機化合物(以下簡稱為VOC)而 造成致病屋(Sick house)症候群發生之增加,是以需要可將 V0C氣體等之有害氣體加以吸附之氣體吸附材。做為前述 氣體吸附材’例如於專利文獻3中係提出了對於v〇c氣 5 1296296 體整體具有吸附效果之氣體吸附片 之氣體吸附片,係於2 、專利文獻3所提出 並於前述w φ 挾持活性碳粒子固定化、 :至少一者之片材使得吸附劑粒子固定 化。在吸附劑粒子之固定 叫拉子固疋 結劑樹脂溶液令混人3 ,可舉出例如(1)於黏 上,於,上重:;合:附劑粒子然後塗佈於-者之片材 佈熱熔劑等,二之方法;(2)事先於一者之片材塗 -片材之方法,、放佈吸附劑粒子’進而於其上重疊另I 1296296 IX. OBJECTS OF THE INVENTION: 1. Field of the Invention The present invention relates to an additive-attached fiber, a fiber structure, and a fiber forming method for attaching an additive (10) er) to a fiber surface. [Previous technique] In the past, a method of attaching an additive to the surface of a fiber is proposed by a method in which a particle is carried by a dry method on a surface of a non-woven fabric, and then heated to a temperature higher than a softening temperature of the fiber to cause adhesion of the particle ( The following patent document u. Secondly, in a water-dispersed solution containing particles, the sheet or the block-like fiber is impregnated and pressed, and then heated to a melting point of the fiber or even no more than 60. The temperature is such that the particles adhere to the 2) method (the following patent document), the fiber product in which the additive has been attached to the surface of the fiber is used in various applications. For example, for polishing and cleaning purposes. Fibers or cloths are generally known as filaments for grinding teeth (DENTee_fi〇ss) for cleaning purposes. In industrial applications, abrasive cloths or abrasive papers are used in lenses and semiconductors. , metal, plastic, ceramics, glass, etc. (4). Also used in households or business kitchens, etc., due to inhalation of volatile organic compounds (hereinafter referred to as VOC) causes an increase in the Sick house syndrome, and is a gas adsorbent which is required to adsorb a harmful gas such as a V0C gas. The gas adsorbent as described above is proposed, for example, in Patent Document 3. The gas adsorption sheet of the gas adsorption sheet having an adsorption effect on the whole body of the v〇c gas 5 1296296 is proposed in Patent Document 3, and the activated carbon particles are immobilized in the above w φ : at least one of the sheets is made The adsorbent particles are immobilized. The immobilization of the adsorbent particles is called a solid solution of the binder, and the resin solution is mixed with 3, for example, (1) on the adhesion, on, on the weight: a method of coating a hot melt on a sheet of cloth, and the like; (2) a method of applying a sheet to a sheet in advance, and placing the adsorbent particles 'and overlapping thereon

礙廢水等淨化用水質淨化材,已提出使 義,准狀活性碳、亦即使用活性碳纖維之各種水質淨化材 (例如專利文獻 4望、/ „ 等)。但疋,使用活性碳纖維之水質淨化 材’會有構成活性碳纖維之活性碳在使財脫落,造成淨 化性能惡化之纟。再I,尚有脫落之活性碳混A淨化後之 液體中之虞。另—方面’於專利文獻5當中係提出了使得In the case of water purification materials for purification of waste water, etc., various water purification materials such as activated carbon fibers, that is, activated carbon fibers (for example, Patent Document 4, „, etc.) have been proposed. However, water purification using activated carbon fibers has been proposed. The material 'has the activated carbon constituting the activated carbon fiber to cause the loss of the purification performance, and the purification performance is deteriorated. I, there is still the enthalpy of the liquid after the separation of the activated carbon mixed A. The other aspect is in the patent document 5 Department proposed

活奴粒子等之有機吸附性粒子透過不溶性黏結劑來附著 於片狀構件之水質淨化過濾器。 又’附著物附著於纖維表面之纖維製品有纖維成形體 之形恶。例如’已提出一種纖維成形體之製造方法,係將 粒子與黏結劑樹脂混合於纖維材料形成纖維鋼(fleece),並 以黏結劑樹脂做熔固來製造高體積墊之後,加壓成形為既 疋形狀者(下述專利文獻6)。再者,已提出一種立體成形 體’係將植物纖維、熱熔固性纖維、以及粉體狀或纖維狀 之機能性材料所構成之機能性纖維片以熱成形所成形者(下 述專利文獻7)。 6 I296296 [專利文獻1]特開平7_268767號公報 [專利文獻2]特公昭51-22557號公報 [專利文獻3]特開2000-246827號公報 [專利文獻4]特開9-234365號公報 [專利文獻5]特開平9-201583號公報 [專利文獻6]特開平9-254264號公報 [專利文獻7]特開20〇4_52116號公報 但是若如前述專利文獻卜2般將纖維加熱至軟化溫产 5熔點以上之溫度,則纖維會收縮又 度,初工也i 1在軟化溫度程 二粒子無法有效以於纖維上,有時必須㈣至溶點以 ::度,如此-來有無法保持纖維形態之問題。再者, 、、義維會收縮變硬,其 θ 保持不織布形態之問題織以有伴隨收縮而無法 之固二=專?: 3所提出之氣體吸附片中之前述⑴ 中,並本/ ,0有°及附劑粒子埋沒於點、结劑樹脂溶液 化方:法得到充分氣體吸附效果之虞。又,前述⑺之固定 附劑粒子附劑粒子之接觸面積少,乃有吸 Μ,於專利文獻4所提出之氣體吸 係使用=:Γ;:Γ述2“材當中之至少1 子之p i材彳―疋於該2 U材之間挾持活性碳粒 粒徑:整二落’必須將活性碳粒子之 子係使用:最大孔徑。是以,活性碳粒 、 0μτη〜1000μη1之粒徑者,由於活性碳粒子之比 積)乃有無法得到充分氣體吸附效果之虞。 1296296 於前述專利文獻5所提出之水質淨化過濾器,會有有 機吸附性粒子埋沒於黏結劑中,有機吸附性粒子之比表面 積減y ’無法得到充分淨化性能之虞。 前述專利文獻6所提丨之成形L鞋子愈黏姓 劑樹脂事先混合來將粒子固定於纖維表面,所以粒子會^ 沒於黏結劑樹脂中,無法充分發揮粒子所具功能,此為問 題所在。再者’於前述專利文獻7中,雖嘗試將熱溶固性 纖維加以熔融來使得粒子狀機能性材料固定,但以該方 法’若未將熱熔固性纖維以相當高溫來熔融,則粒子:去 =,:以高溫炼融又恐有收縮之虞,是以有時難以;到 均勻之成形體。又有時難以製作深抽成形體。 【發明内容】 本發明係用以解決上述習知問題,其目的在於提供— 種添加物附者纖維,可在保持原有纖維之性質的前提 2地附著於纖維表面;並提供-種纖維構造物,可防止於 ==所:Γ添加物之脫落’可抑制添加物之比表面 積的減夕,適用於研磨材、氣體吸附材、水質淨化 亚提供一種纖維成形體,可將 ’ ^ 、加物有效地附著於纖維表 面,可侍到成形均勻、深抽之形 食匕p夂供士、$ # 士 狀’即使於一般之用途亦 “成形成本。本發明並提供前述添加物附著纖維、输 維構造物、纖維成形體之製造方法。 義 本發明之添加物附著纖維, 之黏結劑樹脂、以及於該黏結劑=:維:,辑 特徵在於··該黏結劑樹脂為八附者之添加物;其 Α刀存在下經加熱會凝膠化 1296296 之濕熱凝膠化樹脂,該添加物係藉由該濕熱凝膠化樹脂經 凝膠化之凝膠化物來附著。 本發明之纖維構造物係含有添加物附著纖維,該添加 物附著纖維含有纖維、於該纖維表面之黏結剤樹脂、以及 方、a黏結劑樹脂所附著之添加物;其特徵在於:該黏結劑 樹脂為在水分存在下經加熱會凝膠化之濕熱凝膠化樹脂, 該添加物係藉由該濕熱凝膠化樹脂經凝膠化之凝膠化物來 附著。 本毛月之纖維成形體係纖維構造物所成形而得者,該 纖維構造物係含有纖維、於該纖維表面之黏結劑樹脂、以 及於該黏結劑樹脂所附著之添加物附著纖維;其特徵在 於,玄黏結劑樹脂含有在水分存在下經加熱會凝膠化之谭 樹脂’該纖維構造物令,該纖維係藉由該濕熱凝 鋏胗化之綾膠化物來固定並成形為既定之形 狀0 本發明之添加物附著纖維之製造方法,係用以紫造含 有纖維、於該,纖維表面之黏 : 讲鍫夕沃1 ^黏結劑樹脂所 附者之添加物的添加物附著纖維;其特徵在於 及该黏結劑樹脂係在水 、 你八刀存在下經加熱而凝膠化 膠化纖維,將溶液中分 、 '、、、”、、成 月有5亥/小、加物之添加物分散 予於該濕熱凝膠化纖維,並刀政4液賦 熱凝膠化纖維進行、純/¥ A錢下對該濕 ,、、…處理,使得該濕熱凝膠化纖% $酿 化,以凝膠化物將該添加物附著於纖維表面。纖維抖 本發明之添加物附著纖維之其他製造方法,係用以製 1296296 3有纖維、於該纖維表面之黏結劑樹脂、於該黏結劑樹 月曰所附著之添加物的添加物附著纖維;其特徵在於··該纖 、隹契^魏結劑樹脂係其他纖維與濕熱凝膠化樹脂,對該其 他、截維職予該漏熱凝膠化樹脂之後再賦予添加物,或是將 /合液中分散有該添加物以及該濕熱凝膠化樹脂之添加物分 政’合液賦予於该其他纖維,其次,在濕熱環境氣氛下進行 濕熱處理將該濕熱凝膠化樹脂凝膠化,以凝膠化物將該添 加物附著於其他纖維表面。 本發明之纖維構造物之製造方法,係用以製造含有添 加物附著纖維之纖維構造物,該添加物附著纖維含有纖 、隹於忒纖維表面之黏結劑樹脂、以及於該黏結劑樹脂所 附著之添加物,其特徵在於:該黏結劑樹脂為在水分存在 下、、二加熱會綾膠化之濕熱凝膠化樹脂,該纖維以及該黏結 劑樹脂係擇自 π)含有濕熱凝膠化樹脂纖維成分與其他熱塑性合成 纖維成分之複合纖維; (Π )該複合纖維與其他纖維所混合而成者,· (皿)該複合纖維與濕熱凝膠化樹脂所混合而成者; (IV)濕熱姨膠化樹脂與其他纖維所混合而成者; 中至少一種的組合,以該纖維以及該黏結劑樹脂來製 作纖維構造物,將溶液中分散有該添加物之添加物分散溶 液賦予於該纖維構造物,其次,在濕熱環境氣氛下對該濕 熱凝膠化樹脂進行濕熱處理,使得該濕熱凝膠化樹脂凝膠 化,以凝膠化物將該添加物附著於纖維表面來形成添加物 1296296 附著纖維。 本發明之纖維成形體之製造方法,係用以製造由纖維 構“勿所成形而得之纖維成形體,該纖維構造物含有纖 維、於該纖維表面之黏結劑樹脂、於該黏結劑樹脂所附著 之添加物附著纖維;其特徵在於,該黏結劑樹脂係含有藉 由在水分存在下加熱而凝膠化之濕熱凝膠化樹脂,形成含 有該纖維與黏結劑樹脂之纖維構造物,使得該纖維構造物The organic adsorptive particles such as the living slave particles are attached to the water purification filter of the sheet member through the insoluble binder. Further, the fibrous product in which the adhering matter adheres to the surface of the fiber has a shape of a fibrous formed body. For example, a method for producing a fiber formed body has been proposed in which a particle and a binder resin are mixed with a fiber material to form a fleece, and a high-volume mat is produced by melting with a binder resin, and then pressure-formed into The shape of the crucible (Patent Document 6 below). Further, a three-dimensional formed body has been proposed which is formed by thermoforming a functional fiber sheet composed of a plant fiber, a heat-fusible fiber, and a powdery or fibrous functional material (the following patent document) 7). [Patent Document 1] Japanese Laid-Open Patent Publication No. Hei 9-234365 (Patent Document 3) Japanese Patent Publication No. Hei 9-254264 (Patent Document 7) Japanese Laid-Open Patent Publication No. Hei. No. Hei. No. Hei. No. Hei. 5 above the melting point of the temperature, the fiber will shrink and degree, the initial work also i 1 in the softening temperature range two particles can not be effective on the fiber, sometimes must (four) to the melting point to :: degree, so - there is no way to maintain the fiber The problem of form. Furthermore, the meaning of yue and yue will shrink and harden, and the problem of θ maintaining the non-woven form will be woven with the contraction and cannot be fixed. : In the above-mentioned (1) of the gas adsorption sheet proposed by the above, the / / 0 has ° and the attached particles are buried at the point, and the solution resin is dissolved: the method obtains a sufficient gas adsorption effect. Further, the fixed-attached particle-attached particles of the above (7) have a small contact area, and are sucked, and the gas suction system proposed in Patent Document 4 uses: Γ;: Γ 2 of at least 1 of the materials Material 彳 疋 挟 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 该 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性 活性In the water purification filter proposed in the above Patent Document 5, the organic adsorbent particles are buried in the binder, and the ratio of the organic adsorptive particles is high. The surface area is reduced by y 'there is no sufficient purification performance. The above-mentioned Patent Document 6 proposes that the formed L shoe is more frequently mixed with the resin to fix the particles on the surface of the fiber, so that the particles are not in the binder resin, and the particles are not In order to fully utilize the function of the particles, this is a problem. In the above Patent Document 7, although the hot-melt fiber is attempted to be melted to fix the particulate functional material, If the method does not melt the hot-melt fiber at a relatively high temperature, the particle: go =,: it is difficult to shrink at a high temperature, it is sometimes difficult; to a uniform molded body. Sometimes it is difficult The present invention is directed to solving the above-mentioned conventional problems, and an object thereof is to provide an additive-attached fiber which can be attached to a fiber surface while maintaining the properties of the original fiber; And providing a kind of fiber structure, which can prevent the falling of the Γ additive, can inhibit the reduction of the specific surface area of the additive, and is suitable for the abrasive material, the gas adsorbing material, and the water purification to provide a fiber molded body. ' ^ , Additives can be effectively attached to the surface of the fiber, which can be used to form a uniform, deep-dip shape of the 匕 夂 夂 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 、 即使 即使 即使 即使 即使 即使 即使 即使 即使 即使 即使 即使The present invention also provides a method for producing the above-mentioned additive-attached fiber, an absorbent structure, and a fiber-shaped molded body. The additive-attached fiber of the present invention, the binder resin, and the binder:: dimension: the adhesive resin is an additive of the eight-attachment; in the presence of a file, it is heated by condensation A wet heat gelling resin of 1296296 was adhered, and the additive was adhered by gelation of the wet heat gelling resin. The fiber structure of the present invention contains an additive-attached fiber containing fibers, a binder resin on the surface of the fiber, and an additive to which a binder resin is attached; the binder is characterized in that the binder The resin is a moist heat gelling resin which gels upon heating in the presence of moisture, and the additive is adhered by gelation of the wet heat gelling resin. The fiber structure of the present invention is formed by a fiber structure comprising a fiber, a binder resin on the surface of the fiber, and an additive-attached fiber attached to the binder resin; The mysterious binder resin contains a tan resin which is gelled by heating in the presence of moisture. The fiber structure is fixed by the wet heat gelled sulphide and formed into a predetermined shape. The method for producing the additive-attached fiber of the present invention is for use in a purple fiber-containing fiber, and the adhesive on the surface of the fiber: an additive-attached fiber of the additive attached to the enamel 1 ^ binder resin; The adhesive resin is gelled in the presence of water and water in the presence of your eight knives, and the solution is divided into , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , Dispersing and applying to the damp heat gelling fiber, and processing the wet gelatinized fiber of Kawasaki 4 liquid, treating the wet, ..., so that the wet heat gel chemical fiber is brewed to Gelatin attached to the additive On the surface of the fiber, the other method for producing the fiber attached to the additive of the present invention is for the addition of 1296296 3 fiber, a binder resin on the surface of the fiber, and an additive added to the bond tree. The attached fiber is characterized in that: the fiber, the 隹 ^ 魏 魏 魏 _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ Or the additive and the additive of the wet heat gelling resin are dispersed in the liquid mixture, and the liquid is imparted to the other fibers, and secondly, the wet heat treatment is performed by performing a wet heat treatment in a humid heat atmosphere. Gelation, the addition of the additive to the surface of the other fiber by the gel. The method for producing the fiber structure of the present invention is for producing a fiber structure containing the additive-attached fiber, the additive-attached fiber containing fiber, a binder resin on the surface of the ray fiber and an additive attached to the binder resin, characterized in that the binder resin is in the presence of moisture, and the second heating a gelatinized moist heat gelling resin, the fiber and the binder resin are selected from π) a composite fiber containing a wet heat gelling resin fiber component and other thermoplastic synthetic fiber components; (Π) the composite fiber and other fibers a mixture of the composite fiber and the wet heat gelling resin; (IV) a mixture of a moist heat gelatinized resin and other fibers; a combination of at least one of the fibers And the binder resin is used to form a fiber structure, and the additive dispersion solution in which the additive is dispersed in the solution is applied to the fiber structure, and secondly, the wet heat gelation resin is subjected to a wet heat treatment in a humid heat atmosphere atmosphere. The wet heat gelling resin is gelated, and the additive is adhered to the surface of the fiber by a gel to form an additive 1296296 adhering fiber. The method for producing the fiber molded body of the present invention is for manufacturing a fiber structure. a formed fiber formed body comprising fibers, a binder resin on the surface of the fiber, and an additive attached to the binder resin Fiber; wherein the resin-based binder comprises heating by means of wet heat gelling of the presence of moisture in the gelled resin, is formed with a fiber structure containing the fibers and the binder resin, so that the fiber structure

在金屬模具内、濕熱環境氣氛下將該濕熱凝膠化樹脂濕熱 凝膠化做濕熱成形加工。 【實施方式】 d於本發日月中,<故為在水分存在下加熱可凝膠化之黏結 J树知,係使用濕熱凝膠化樹脂。濕熱凝膠化樹脂之形能 可舉出粉末狀、尖突(tip)狀、纖維狀等。特別是,渴^ 膠化樹脂以纖維狀為佳。做為纖維狀之濕熱凝膠化樹脂(以 下稱為「濕熱凝膠化纖維」)可使用濕熱凝膠化樹脂單獨之 纖維、或是含有濕熱凝膠化樹脂纖維成分與其他熱塑性合 成纖維成分之複合纖維(以下稱為「濕熱凝膠化複合纖 維」)。藉此,其他纖維或是至少其他熱塑性合成纖維成分 可保持纖維形態,且濕熱凝膠化樹脂可被凝膠化而發揮可 將添加物加以附著之黏結劑的作用功能。再者,添加物可 藉由濕熱凝膠化樹脂纖維成分或是於纖維表面所附著之濕 熱凝膠化樹脂經濕熱凝膠化之凝膠化物來被附著。較佳為 添加物係外露而附著。又,濕熱凝膠化樹脂彼此以及/或是 其他纖維可藉由濕熱凝膠化樹脂纖維成分或是於纖維表面 11 1296296 所附著之濕熱凝膠化樹脂經濕熱凝膠化所得之凝膠化物來 固定。 又,本發明之纖維成形體可藉由在金屬模具内使得纖 維構造物凝膠化之狀態下進行濕熱成形,來成形為既定形 狀之成形體。濕熱凝膠化樹脂之形態可舉出粉末狀、尖突 狀、纖維狀等。特別是,若考慮成形加工性,以纖維狀、 亦即濕熱凝膠化纖維為佳。 前述濕熱凝膠化樹脂之較佳凝膠化溫度為5〇ι 1佳之凝膠化溫度為80t以上。若使用能在未滿5(rc凝 膠化之樹脂,有時於凝膠加工之際會嚴重黏附於輥子或金 屬模具等造成纖維構造物與纖維成形體之生產變得困難, 或是在盛夏或高溫環境無法使用。又,所謂的「凝膠加工」 係使得濕熱凝膠化樹脂凝膠化之加工。 前述濕熱凝膠化樹脂以乙稀—乙稀醇共聚樹脂為佳。 其理由在於’可藉由濕熱而凝膠化’避免其他纖維以及/或 是其他熱塑性合成纖維成分變質之故。所說的乙烯—乙稀 酵共聚樹脂,係使得乙稀—乙酸乙稀醋鹼化所得之樹脂, 其鹼化度以95%以上為佳。更佳之驗化度為98%以上。又, 較佳之乙稀含有率為2G莫爾%以上。較佳之乙烯 50莫爾%以下。更佳之7 γ 早為 更仏之乙細含有率為25莫爾%以上 之乙浠含有率為45莫爾%以下。若驗化度未滿㈣有· =膠加工之際會黏附⑽子或金屬模㈣造成 物 莫_情況也同樣,有;:二,乙稀含有率為 有4於减膠加工之際會黏附於輥子 12 1296296 或金屬模具等造成纖维播 纖維構造物與纖維成形體之生產變得困 難。另一方面,若己说八士 坪3有量超過50莫爾%,則濕熱凝膠 化溫度會變高,不得不 个对加工溫度上升至熔點附近,其結 果 才“對於纖維構造物與纖維成形體之尺寸安定性造 成不良影響。 月J述識維與别述黏結劑樹脂之較佳組合可舉出 ()s有濕、熱政膠化樹脂纖維成分與其他熱塑性合成 纖維成分之複合纖維;The wet heat gelled resin is wet-gelled into a wet heat forming process in a molten metal atmosphere under a hot and humid atmosphere. [Embodiment] d In the present day and the month, <therefore, it is a gel which can be gelled in the presence of moisture. It is known that a wet heat gelling resin is used. The shape of the moist heat gelling resin may be a powder, a tip, a fiber or the like. In particular, the gelatinized resin is preferably fibrous. As the fibrous moist heat gelling resin (hereinafter referred to as "wet heat gelling fiber"), it is possible to use a wet heat gelling resin alone fiber or a wet heat gelling resin fiber component and other thermoplastic synthetic fiber components. Composite fiber (hereinafter referred to as "wet heat gelled composite fiber"). Thereby, the other fibers or at least other thermoplastic synthetic fiber components can maintain the fiber form, and the moist heat gelling resin can be gelated to function as a binder which can adhere the additives. Further, the additive may be adhered by a wet heat gelation resin fiber component or a wet heat gelled gel of a moist heat gelled resin attached to the surface of the fiber. Preferably, the additive is exposed and adhered. Further, the wet heat gelling resins and/or other fibers may be obtained by wet heat gelation of the resin fiber component or the wet heat gelation resin attached to the fiber surface 11 1296296 by wet heat gelation. fixed. Further, the fibrous formed article of the present invention can be molded into a molded article of a predetermined shape by wet thermoforming in a state where the fibrous structure is gelled in a metal mold. The form of the moist heat gelling resin may, for example, be powdery, pointed, or fibrous. In particular, in consideration of moldability, it is preferred to use a fibrous, that is, a wet heat gelled fiber. The gelation temperature of the wet heat gelling resin is preferably 5 〇 1 and the gelation temperature is 80 t or more. If it is used in a resin that is less than 5 (rc gelled, sometimes it may become difficult to adhere to a roller or a metal mold during gel processing, resulting in difficulty in the production of fiber structures and fiber molded bodies, or in midsummer or The high temperature environment cannot be used. Further, the so-called "gel processing" is a process of gelling a wet heat gelling resin. The wet heat gelling resin is preferably a vinyl-ethylene glycol copolymer resin. The reason is that Gelling by damp heat 'avoids deterioration of other fibers and/or other thermoplastic synthetic fiber components. The ethylene-ethylene glycol copolymer resin is a resin obtained by alkalizing ethylene-acetic acid ethyl acetate. The degree of alkalization is preferably 95% or more, and more preferably 98% or more. Further, the preferred ethylene content is 2 G mol% or more. Preferably, the ethylene is 50 mol% or less. More preferably, 7 γ is early. For the more detailed content of B, the content of acetamidine is 25 mol% or less, and the content of acetamidine is 45 mol% or less. If the degree of test is not full (4), there is adhesion (10) or metal mold (4). _The same is true, there are;: Second, Ethylene If there is a rate of 4, it will stick to the roller 12 1296296 or the metal mold at the time of the rubber reduction processing, which makes it difficult to produce the fiber-fiber structure and the fiber-shaped body. On the other hand, if it is said that the Ba Shiping 3 has When it exceeds 50% by mole, the wet heat gelation temperature becomes high, and the processing temperature rises to the vicinity of the melting point, and as a result, "the effect on the dimensional stability of the fiber structure and the fiber formed body is adversely affected. The preferred combination of the dimension and the other adhesive resin may be a composite fiber of the wet and thermal gelatinized resin fiber component and other thermoplastic synthetic fiber components;

(π)忒複合纖維與其他纖維所混合而成者; (瓜)4複合纖維與濕熱凝膠化樹脂所混合而成者; (^)濕熱凝膠化樹脂與其他纖維所混合而成者; 中至J 一種(以下稱為「形態(I )〜形態(贝)」)。前述 ^悲(I)係以「黏結劑樹脂」做為濕熱凝膠化樹脂,以「纖 、准J彳故為其他熱塑性合成纖維成分之濕熱凝膠化複合纖 維。則述形態(Π )係以「黏結劑樹脂」做為濕熱凝膠化複 合纖維,以「總祕 、截、准」做為其他纖維所混合而成者。前述形 恶(m)係以「纖維」做為濕熱凝膠化複合纖維,並以「黏 結劑樹脂」做為濕熱凝膠化樹脂所混合而成者。前述形態(IV) ’、以黏結劑樹脂」做為採取前述濕熱凝膠化複合纖維以 外之形態的濕熱凝膠化樹脂(例如濕熱凝膠化樹脂單獨之纖 、隹)以「纖維」做為其他纖維所混合而成者。 於刚述形態(I )〜(m)所使用之濕熱凝膠化複合纖維, 以濕熱凝膠化樹脂纖維成分露出或是部份區分之複合纖維 為佳。其複合形狀係指同心圓型、偏心芯套型、並列蜇、 13 1296296 分剎型、海島型等。 η 姑μ 特另〗疋同心圓型以添加物容易附著於(π) 忒 composite fiber mixed with other fibers; (melon) 4 composite fiber and wet heat gelatinized resin mixed; (^) wet heat gelatinized resin mixed with other fibers; Medium to J (hereinafter referred to as "form (I) ~ form (bei)"). The above-mentioned (I) is a moist heat-gelled composite fiber in which "bonding agent resin" is used as a damp heat-gelating resin, and "fiber and quasi-J" are used as other thermoplastic synthetic fiber components. The "bonding agent resin" is used as a damp heat gelled composite fiber, and the "general secret, cut, and quasi" is mixed with other fibers. The above-mentioned form (m) is a mixture of "fiber" as a wet heat gelled composite fiber and a "bonding agent resin" as a moist heat gelling resin. The above-mentioned form (IV) ', the binder resin is used as the wet heat gelling resin (for example, the wet heat gelling resin alone fiber or enamel) other than the wet heat gelled composite fiber, and the "fiber" is used as the "fiber" Other fibers are mixed. The wet heat gelled composite fiber used in the form (I) to (m) is preferably a composite fiber in which the wet heat gelled resin fiber component is exposed or partially distinguished. The composite shape refers to a concentric circle type, an eccentric core sleeve type, a parallel raft, a 13 1296296 split brake type, an island type, and the like. η 姑μ Special 疋 疋 concentric type with additives easy to attach to

纖維表面為佳。又,1I 入具截面形狀可為圓形、中空、異型、 橢圓形、星形、扁平 考旦、^ , 扁干^荨任一,從纖維製造之難易程度來 、i t為佳。分割形複合纖維以事先喷射高壓水流等 / ^刀#j為佳°藉此’經分割之濕熱凝膠化樹脂纖維 成刀可精由濕執處理炎)耗a …、处木凝膠化,形成凝膠化物來附著於其 他纖維表面,將添加物 加物附者。亦即,發揮黏結劑之功能。The fiber surface is preferred. In addition, the 1I shape of the cross-section can be circular, hollow, profiled, elliptical, star-shaped, flat, or flat, and can be made from the ease of fiber manufacture, and i t is preferred. The split-type composite fiber is preferably sprayed with a high-pressure water stream or the like, so that the 'divided wet heat gelled resin fiber can be processed by the wet handle. A gel is formed to adhere to the surface of the other fibers, and the additive is attached. That is, the function of the binder is exerted.

八;A Hi膠化複合纖維所#濕熱凝膠化樹脂纖維成 匕例以10質置%〜90質量%之範圍内為佳。更佳之濕 熱凝膠化樹脂纖維成分的含有量為30質量%〜70質量%:、 若濕熱凝膠化樹脂纖維成分之含有量未滿ι〇質量%,添加 :有難以附著之傾向。若濕熱凝膠化樹脂纖維成分之含有 里超過90貝1 % ’則複合纖維之纖維成形性有降低 向。 *八; A Hi gelled composite fiber ########################################################## More preferably, the content of the hot-gelled resin fiber component is from 30% by mass to 70% by mass. When the content of the wet heat gelling resin fiber component is less than 〇% by mass, the addition tends to be difficult to adhere. When the content of the wet heat gelled resin fiber component exceeds 90 lbs and 1%, the fiber formability of the conjugate fiber is lowered. *

、則述濕熱凝膠化複合纖維中之其他熱塑性合成纖維成 分,可為聚烯烴、聚酿、聚醯胺等,較佳為聚稀煙。使用 乙烯乙烯醇系共聚樹脂當作濕熱凝膠化樹脂纖維成分的 情況,容易形成以熔融紡絲所構成之複合纖維(組合纖維)。 又,做為其他熱塑性合成纖維成分,以使用具有熔點 高於用以將濕熱凝膠化樹脂纖維成分;疑膠化之溫度的熱塑 性合成纖維成分為#。若其他熱塑&合成纖維成分為具有 熔點低於用以形成凝膠化物之溫度之熱塑性合成纖維成 分,則其他熱塑性合成纖維成分本身有熔融變硬之傾向, 例如做成纖維成形體時有時會伴隨收縮而成為不均勻。 14 1296296 丽述濕熱凝膠化複合纖維在纖維構造物中所佔之比例 只要是可將添加物附著之量即可並無特別限定,藉由凝膠 化物將纖維固定以及/或是將添加物有效固定所需之複合纖 維的比例以ίο質量%以上為佳。更佳之複合纖維之比例為 30質量%以上。特佳之複合纖維之比例為5〇質量%以上。 例如,當纖維構造物係含有複合纖維之纖維網存在於兩表 面,内部存在其他纖維的情;兄,係指含有複合纖維之纖維 網的含有量。Further, the other thermoplastic synthetic fiber component in the wet heat gelled composite fiber may be a polyolefin, a polystyrene, a polyamide or the like, preferably a polydue smoke. When an ethylene vinyl alcohol-based copolymer resin is used as the component of the wet heat-gelled resin fiber, it is easy to form a composite fiber (combined fiber) composed of melt-spinning. Further, as the other thermoplastic synthetic fiber component, a thermoplastic synthetic fiber component having a melting point higher than that for hydrothermally gelling the resin fiber component; If the other thermoplastic & synthetic fiber component has a thermoplastic synthetic fiber component having a melting point lower than the temperature at which the gelation is formed, the other thermoplastic synthetic fiber component itself has a tendency to melt and harden, for example, when it is formed into a fiber formed body. It will become uneven with shrinkage. 14 1296296 The ratio of the Lichaothermal gelled composite fiber in the fiber structure is not particularly limited as long as it can adhere the additive, and the fiber is fixed by the gel and/or the additive is added. The ratio of the composite fibers required for effective fixation is preferably ίο% by mass or more. The ratio of the more preferable composite fiber is 30% by mass or more. The ratio of the excellent composite fiber is 5% by mass or more. For example, when the fiber structure contains a composite fiber, the fiber web exists on both surfaces, and other fibers are present inside; brother, the content of the fiber web containing the composite fiber.

亦可於濕熱凝膠化複合纖維進— 在前述形態(m)中 步含有濕熱凝膠化樹脂而於複合纖維表面形成凝膠化物。 藉此’可進一步提升添加物之附著效果。 於前述形態U)或是形態(IV)所使用之其他纖維,可選 :使用人造絲等之化學纖維、棉、麻、羊毛等之天然纖维 等、聚烯烴樹脂'f酯樹脂、聚醯胺樹脂、丙烯酸樹脂、 聚胺基甲酸醋樹脂等合成樹脂之單獨或複數成分 維等任意之物。 〜則通㈣uv)中,濕熱凝膠化樹脂相對於纖維構造 :以含有i質量%〜90質量%之範圍内為佳。更佳之含有量 -3質量%〜70質量%。若濕熱凝膠化樹脂之含有 質量。/。,I藉由凝膠化物來固定其他纖維會有困難,或θ !;加物變得難以附著之傾向。若濕熱凝膠化樹脂之含; =過90質量% ’有時纖維形狀會消失而成為薄膜狀 疋漆加物埋沒於凝膠化物中。 述添加物只要是粒子即可能使用任意物質。例如 15 1296296 “物:無機粒子為佳。只要為無機粒子,則做為研磨劑 使用勺!·月况,研磨作用顯著。前述無機粒子可舉出氧化銘、 :虱化矽、三聚磷酸鈉(trip〇ly)、鑽石、剛玉、剛砂、石 火石、合成鑽石、氮化硼、碳化矽、碳化硼、氧 1匕釭氧化飾、氧化鐵、石夕酸膠體、碳、石墨、沸石、二 氧者呵嶺土、黏土等。該等粒子可適宜混合使用。 。當添加物為氣體吸附性粒子的情況,氣體吸附性粒子 ’、要為具有將空氣中之氣體物質加以吸附之功能者即可並 無特別限定,又以、、去r山Jav π ' 又以活性妷粒子、沸石、矽膠、活性白土、 層狀%酸鹽等之多孔質粒子、於該等多孔質粒子擔載化學 吸附劑之多孔質粒子等為佳。於多孔質粒子當中又以 碳粒子為特佳。 & 當前述添加物為有機物吸附性粒子的情%,有機 附性粒子只要是具有可將液體中之有機物予以吸附之功处 者即可並無特別限定,以活性碳粒子、沸石、石夕膠、活性 白土、層狀破酸鹽等之多孔質粒子、於該等多孔質粒子擔 載化學吸附劑之多孔質粒子等為佳。於多孔質粒子當中‘ 以活性碳粒子為特佳。 再者除了前述研磨劑、氣體吸附性粒子以及有機 附性粒子以外,亦可使用做為乾燥劑之石夕膠、做為光觸媒 ^一虱化鈦、病毒吸附/分解劑 '抗菌劑、除臭劑、導電劑、 抗包d、s周濕劑、防蟲劑、防徽劑、難燃劑等之功能性、天 加物之1種或2種以上。 外 月述添加物之平均粒徑以〇 (H〜1〇〇jum之範圍為隹。 16 1296296 更佳之平均粒徑為〇.5_以 上。更佳之承t住之十均粒徑為Ιμηι以 1之十均粒徑為80μηι以 〇.〇1μηι,則右_ + 1 ^ 右千均粒徑未滿 —工Α 可"】、、加物會埋沒於凝膠化物中。 若平均粒徑超讲lnn Τ 另一方面, 超過ΙΟΟμπι的情況,添 小,有時盔法y 、 奶义比表面積會變 果。 崎分之添加物之功能、例如氣體吸附效 前述纖維構造物係含有纖維以及 所說的纖川曰者此處 物、今網望〇 歲#纖維塊、不織布、編織 高之纖維所形成者。特別是由於不織布之加工性 造物中含右该躺 rt 做為本發明之纖維構 著纖維於飞’木便用的匱况’以添加物附 ^准^表面以纖維網狀存在,㈣存在著親水性纖維 述親水性纖維以擇自人造絲纖維、棉纖維以及紙 :中至種纖維為佳。其理由在於,賦予水、界面活性 片,洗淨劑等之液體進行研磨之際,水分保持性高之故。 本^月之一貫施形態’例如在添加物方面使用氣體吸 付生粒子之氣體吸附材,不限定於不織布,亦能為鳴 口口勿附者纖維所形成之複數束纖維束做為氣體吸附部之氣 婊°模!。另外,亦可將該添加物附著纖維之集合物捲 繞成圓筒狀者、成形為打摺狀者當做氣體吸附過濾器來使 用。又,使用有機物附著性粒子做為添加物之水質淨化材 並不限定於不織布,亦可為以該添加物附著纖維複數束形 成之纖維束做為有機物吸附部之水質淨化模組。又,亦可 將忒添加物附著纖維之集合物捲繞成圓筒狀者、成形為打 17 1296296 摺狀者當做水質淨化過濾器來使用。 又將、截維構造物以金屬模具做成形加工之際,纖維 構Xe物以不、哉布為佳。若為不織布,貝I】製造成本便宜,加 也合易田加工成形時含有水分,容易適度伸長而順沿 金屬模具的形狀,容易得到深抽成形體。 纖維構造物之較佳的單位面積重量為 20g/m〜600g/m2。纖維構造物之較佳厚度負荷) 為0.1mm〜3mm之範圍。It is also possible to form a gelled product on the surface of the composite fiber by wet-gelling the composite fiber into a wet heat gelling resin in the above form (m). Thereby, the adhesion effect of the additive can be further improved. Other fibers used in the above-mentioned form U) or form (IV) may be selected from chemical fibers such as rayon, natural fibers such as cotton, hemp, wool, etc., polyolefin resin 'f ester resin, polyfluorene. Any of a single or a plurality of synthetic resins such as an amine resin, an acrylic resin, or a polyurethane resin. In the case of the above-mentioned (four) uv), the wet heat gelling resin is preferably in a range of from i% by mass to 90% by mass based on the fiber structure. More preferably, the content is -3% by mass to 70% by mass. If the wet heat gelled resin contains the mass. /. I may have difficulty fixing other fibers by gelation, or θ!; the additive tends to be difficult to adhere. If the content of the moist heat gelling resin is ≥ 90% by mass, the fiber shape may disappear and become a film-like enamel additive which is buried in the gel. Any additive may be used as long as it is a particle. For example, 15 1296296 "Material: Inorganic particles are preferred. As long as it is an inorganic particle, a scoop is used as an abrasive. · The state of the moon is remarkable. The inorganic particles are oxidized, bismuth telluride, sodium tripolyphosphate. (trip〇ly), diamond, corundum, corundum, slate, synthetic diamond, boron nitride, tantalum carbide, boron carbide, oxygen oxide, iron oxide, agglomerate, carbon, graphite, zeolite, Dioxins, clay, clay, etc. These particles may be suitably used in combination. When the additive is a gas-adsorbing particle, the gas-adsorbing particle 'has to be a function of adsorbing a gaseous substance in the air. There is no particular limitation, and the porous particles, such as active cerium particles, zeolite, tannin, activated clay, layered % acid salt, etc., are supported on the porous particles. The porous particles of the adsorbent and the like are preferred. The carbon particles are particularly preferred among the porous particles. & When the additive is an organic adsorbent particle, the organic additive particles may have a liquid in the liquid. Have The organic matter to be adsorbed by the organic matter is not particularly limited, and porous particles such as activated carbon particles, zeolite, talc, activated clay, and layered acid salt are supported on the porous particles to carry chemical adsorption. The porous particles of the agent are preferably used. Among the porous particles, 'the activated carbon particles are particularly preferable. In addition to the above-mentioned abrasives, gas-adsorbing particles, and organic particles, a stone as a desiccant can also be used. As a photocatalyst, as a photocatalyst, a titanium oxide, a virus adsorption/decomposition agent, an antibacterial agent, a deodorant, a conductive agent, an anti-bag d, a sweating agent, an insect repellent, an anti-indicator, a flame retardant, etc. One or more of the functional and daily additions. The average particle size of the external additions is 〇 (H~1〇〇jum is 隹. 16 1296296 The better average particle size is 〇.5_ The better ten-size particle size is Ιμηι, the average particle size of 1 is 80μηι 〇.〇1μηι, then the right _ + 1 ^ right thousand average particle size is not full - work can be "], The additive will be buried in the gel. If the average particle size exceeds lnn Τ on the other hand, it exceeds ΙΟΟμπι In the case of small additions, sometimes the helmet method y, the milky specific surface area will change. The function of the additive of the Kawasaki, such as the gas adsorption effect, the fiber structure contains fibers and the fiber , 今网望〇岁# fiber block, non-woven fabric, weaving high fiber formed. Especially because the non-woven fabric processing product contains the right lie rt as the fiber of the invention, the fiber is used in the fly The condition is that the surface of the additive is in the form of a fibrous web, and (4) the hydrophilic fiber is present. The hydrophilic fiber is preferably selected from the group consisting of rayon fiber, cotton fiber, and paper: medium to fiber. The reason is that When a liquid such as water, an interface active sheet, or a detergent is applied, the water retaining property is high. The constant application form of the present month, for example, a gas adsorbing material that uses a gas to absorb raw particles in an additive, is not limited to a non-woven fabric, and can also be used as a gas adsorption for a plurality of bundles of fibers formed by the fibers of the mouth of the mouth. Department of the gas 婊 ° die! . Further, the additive-attached fiber aggregate may be wound into a cylindrical shape and formed into a folded shape as a gas adsorption filter. Further, the water purification material using the organic-adherent particles as an additive is not limited to the non-woven fabric, and may be a water purification module in which the fiber bundle formed by the plurality of bundles of the additive-attached fibers is used as the organic adsorption portion. In addition, if the aggregate of the ruthenium-attachment-attached fibers is wound into a cylindrical shape, it may be used as a water purification filter when it is formed into a 17 1296296 fold. Further, when the cut structure is formed by a metal mold, the fiber structure Xe is preferably not cloth or cloth. In the case of non-woven fabric, the product is inexpensive to manufacture, and it is easy to obtain a deep-drawn molded body by containing moisture in the processing of Yitian. The preferred basis weight of the fibrous structure is from 20 g/m to 600 g/m2. The preferred thickness load of the fibrous structure is in the range of 0.1 mm to 3 mm.

如述纖維構造物為了蚀4田 一 乃Γ使仵添加物之功能性有效發揮, 前述添加物之附著量對於纖維構造㈣im2以2g以上為 佳,以⑽以上為更佳,20g以上為特佳。 :、人針對本發明之添加物附著纖維以及纖維構造物 之製造方法做說明。本發明中 ^十 中之濕熱處理係以濕熱環境氣 巩來施行。此處所說的「 i 蜋纟兄軋矹」,意指包含水分 而被加熱之環境氣氛。所謂 的“、熱處理,係對於賦予了黏 …口劑樹脂之纖維、含有渴献、妹 人一 有濕熱,旋膠化纖維成分之纖維、或是 各有该等纖維之纖維構造物賦予 八私Λ s有添加物之添加物 刀放/谷液之後進行加熱之處 八私a 或疋一邊賦予前述添加物 刀放洛液一邊加熱之處理。加 成 > > 丄 乃次可舉出暴露於加埶環 土兄虱氖中之方法、使貫通加 '' ,.^ ^ 孔T之方法、以及使其盥 加熱體接觸之方法等。 /…、 賦予前述添加物分散溶液後進行加熱的情況 熱處理中之纖維或是纖維構造物所 、‘、 盤幺「u、十 、 之尺刀的比例(以下 稱為水分率」)以20質量%〜8〇〇 下 貝里/〇為佳。更佳之水 18 1296296 分平馬質重一 ^ %〜600質量%。水分率若未滿2〇質 '二、〇貝i 無法充分產生。另一方面,若水分率超過8:=膠化 濕熱處理在纖維構造物表面與内部之 里❹,則 曰J播法均句谁、 熱凝膠化之程度有不均勻之傾向。 丁 ’濕 艰刀之賦予方、、土 Λ匕 以贺霧、浸潰於水槽中等眾知方法來進 去月匕 斤守別疋,你j曰 添加物分散溶液含浸於纖維構造物之 — 侍 7広’谷易使得大旦The fiber structure is effective for the function of the ruthenium additive, and the adhesion amount of the additive is preferably 2 g or more for the fiber structure (4), more preferably (10) or more, and more preferably 20 g or more. . The method for producing the additive-attached fiber of the present invention and the fiber structure will be described. In the present invention, the wet heat treatment is carried out in a moist heat environment. The term "i 螂纟 矹 矹" as used herein means an ambient atmosphere that is heated by moisture. The so-called "heat treatment" is given to the fiber which imparts the resin to the adhesive, the fiber containing the thirst, the wet heat of the sister, the fiber of the gelatinized fiber component, or the fiber structure of each of the fibers. Λ s Addition of the additive, the knife is placed, and the gluten is heated, and then the heat is applied to the additive knife. The addition is added to the solution. Addition >> a method of adding a ring to a brother in the earth, a method of adding a '', a ^^ hole T, a method of contacting the heating body, etc. /..., applying the above-mentioned additive dispersion solution and heating In the case of the heat treatment, the fiber or the fiber structure, 'the ratio of the knives of the u, ten, and the knives (hereinafter referred to as the water content) is preferably 20% by mass to 8 lbs. Better water 18 1296296 The level of horses is 1%~600% by mass. If the moisture rate is less than 2 enamel's, the mussel i cannot be fully produced. On the other hand, if the moisture content exceeds 8: = gelation The wet heat treatment is on the surface of the fiber structure and the inside of the fiber structure, and the degree of thermal gelation tends to be uneven. Ding 'wet hard knife to give the party, the earthworms to the fog, soaked in the sink, the publicly known method to go into the moon, 守 守 守 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋 疋広 '谷易使大旦

添加物進入纖維構造物内部’故為所喜好者。被賦予1 分之纖維或纖維構造物可利用擠壓輥等做壓榨 I水 整為既定之水分率。 /來調 當-邊賦予添加物分散溶液一邊加熱的情況, 膠化樹脂之凝膠化由於是和水分賦予同時進行,所以只 調整添加物分散溶液中之添加物濃度以及添加物分聽 之溫度來調整添加物之附著量即可。具體而言, 纖 維或纖維構造物含浸於含有添加物之熱水中(9(rc以上) 可將添加物附著於纖維表面。 於濕熱處理前之纖維構造物亦可施行親水處理。若施 以親水處理,則當纖維構造物含有疎水性纖維的情況,可 對纖維構造物大致均勻地賦予水分。其結果,複合纖維被 大致均勻地濕熱凝膠化,添加物容易附著,故為所喜好者。 在親水處理方面,可舉出界面活性劑處理、弧光放電或輝 光放電法、電漿處理法、電子束照射法、γ線照射法、光 子法、火焰法、氟處理法、接枝處理法、以及碏化處理 等0 4 19 1296296 前述濕熱處理中之濕熱處理溫度以濕熱凝膠化樹脂或 是濕熱凝膠化樹脂纖維成分(以下有時也將兩者統稱為「點 結劑树月曰」)之凝膠化溫度以上、炫點_2〇(>c以下為佳。更 佳之濕熱處:溫度為50t以上。特佳之濕熱處理溫度為扣 c以上。另-方面,更佳之濕熱處理溫度為黏結劑樹脂之 炼點鐵以下。特佳之濕熱處理溫度為黏結劑樹脂之炫點 _贼以下。若濕熱處理溫度未滿黏結劑樹脂之凝谬化溫 度’有時無法有效地附著添加物。若濕熱處理溫度超過^ 結劑樹脂之溶點鐵,由於接近黏結劑樹脂之炼點,所以 做成纖維構造物時有時會引起收縮。 於刖述濕熱處理中,與加熱體接觸的情況,面壓以 0.01〜0.2MPa為佳。更佳之面壓下限& Q•隨Pa。更佳之 面麼上限A G.〇8MPa。又,t加熱體為熱輥來進行麼縮成 形處理的情況,熱輥之線M卩1〇〜彻N/cm為佳。更佳之 熱輥線壓為5GN/em。更佳之熱輥線壓的上限為2刪 依據此方法’由於可瞬間將濕熱凝膠化樹脂纖維成分渴埶 凝膠化並同時壓展凝膠化物,所以可廣範圍地使得添加 附者。又’依據此方法,當濕熱凝膠化時,添加物可壓入 凝膠化物當中,可將添加物更強固地附著於纖維表面。 對纖維構造物賦予體積膨脹性以及/或是柔軟性的情 :兄^於含有前述纖維與前述濕熱凝膠化樹脂之纖維網進 仃瘵氣處理,可形成濕熱凝膠化樹脂經凝膠化所得之凝膠 化物來使得添加物附荖。傲盔兮* 订^做為蒸氣處理方法,可舉出例如 從纖維網等之上方以及/或是下方吹送蒸氣之方法、以熱壓 20 1296296 鋼等曝露於墓惫中 維構造物施加凝勝加工時二:=:方二,無須對於纖 纖維構造物可m、*£力以上之壓力。其結果’ 維表面而在此狀態;附:維形態-邊使得添加物露議 本發明中戶力維成形體:製造方法做說明。於 添加物分散溶液後纖維構造物賦予The additive enters the interior of the fibrous structure, so it is preferred. The fiber or fiber structure to which 1 minute is imparted can be pressed by a squeezing roller or the like to be a predetermined moisture rate. / When the mixture is heated while the additive is dispersed, the gelation of the gelled resin is performed simultaneously with the moisture supply, so that only the concentration of the additive in the additive dispersion solution and the temperature at which the additive is heard are adjusted. To adjust the amount of adhesion of the additive. Specifically, the fiber or fiber structure is impregnated with hot water containing an additive (9 (rc or more) to attach the additive to the surface of the fiber. The fiber structure before the wet heat treatment may also be subjected to a hydrophilic treatment. In the case of the hydrophilic treatment, when the fibrous structure contains the hydrophobic fiber, the fibrous structure can be uniformly and uniformly supplied with water. As a result, the composite fiber is substantially uniformly wet-gelled, and the additive is likely to adhere, so that it is preferred. In the hydrophilic treatment, a surfactant treatment, an arc discharge or a glow discharge method, a plasma treatment method, an electron beam irradiation method, a γ-ray irradiation method, a photon method, a flame method, a fluorine treatment method, a graft treatment method, etc. may be mentioned. And the deuteration treatment, etc. 0 4 19 1296296 The wet heat treatment temperature in the above wet heat treatment is a wet heat gelation resin or a wet heat gelation resin fiber component (hereinafter sometimes referred to as "pointing agent tree moon 曰" ") above the gelation temperature, Hyun point _2 〇 (> c or less is better. More preferred wet heat: temperature is 50t or more. The best moisture heat treatment temperature is above the c c. Another side The better heat treatment temperature is below the melting point of the binder resin. The special heat treatment temperature is the bright point of the binder resin _ thief. If the wet heat treatment temperature is not full of the gelatinization temperature of the binder resin, sometimes it is impossible. The additive is effectively adhered to. If the wet heat treatment temperature exceeds the melting point of the resin of the binder, it is close to the refining point of the binder resin, so that the fiber structure may cause shrinkage when it is formed into a fiber structure. When the heating body is in contact, the surface pressure is preferably 0.01 to 0.2 MPa. More preferably, the lower surface pressure & Q • with Pa. The upper surface is higher than the upper limit A G. 〇 8 MPa. Also, is the t heating body a heat roller? In the case of shrink forming treatment, the line of hot roll M卩1〇~ thoroughly N/cm is better. The better hot roll line pressure is 5GN/em. The upper limit of the hot roll line pressure is 2 according to this method' Instantly gels the wet heat gelled resin fiber component to thirst and simultaneously compresses the gelled product, so that the additive can be widely applied. According to this method, when wet heat gelation, the additive can be pressed in. Among the gels, the additive can be stronger The solid surface adheres to the surface of the fiber. The volume expansion and/or softness of the fiber structure is imparted: the wet fiber is formed by the helium gas treatment of the fiber containing the fiber and the wet heat gelling resin. The gelled resin is gelated to obtain an additive. The method of steam treatment is, for example, a method of blowing steam from above and/or below a fiber web. When hot pressing 20 1296296 steel is exposed to the tomb, the dimensional structure is applied to the condensing process. 2:=: square 2, there is no need for the fiber fiber structure to be more than m, *£ force. The result is 'dimensional surface In this state; attached: dimension form - edge makes the additive appear in the present invention, the Uyghur shaped body: the manufacturing method is explained. After the additive dispersion solution, the fiber structure is given

分散溶液-邊純、成:之处理、或疋—邊^添加物 雨 …、成形為既定形狀。加熱方法可舉出曝 ^口「、環境氣氛中之方法、與加熱體接觸之方法等。對 八、隹構&物賦予添加物分散溶液之際之水分率係與上述水 /刀率相同,在此省略其說明。 ;月;】述濕熱成形加工中,冑含有添加斗勿分散溶液之纖 ,構造㈣人-對之金屬w㈣行加熱加壓處理乃為較 仏做法。右在不含水分之狀態下加熱,不織布本身會適度 =長而今易順沿金屬模具之形狀,容易得到深抽成形體。 、邊賦予—加物为散溶液一邊加熱的情況,可藉由例如 將纖維構造物插入一對之金屬模具内並含浸於熱水中(9(rc 以上)來得到成形體。 濕熱成形加工係在濕熱環境氣氛下施行。濕熱成形加 工溫度以凝膠化樹脂之凝膠化溫度以上〜熔點-2(rc為佳。 更佳之濕熱成形加工溫度為5(^c以上。特佳之濕熱成形加 工溫度為80°C以上。另一方面,更佳之濕熱成形加工溫度 為濕熱凝膠化樹脂之熔點·3〇°ς:以下。特佳之濕熱成形加工 /嚴度為濕熱凝膠化樹脂之熔點-40°C以下。若濕熱成形加工 21 1296296 溫度未滿濕熱凝膠化樹脂之凝膠化溫度,則難以形成凝膠 化物。若濕熱成形加工溫度超過濕熱凝膠化樹脂之炫點_2〇 °c,由於接近濕熱凝膠化樹脂之溶點,有日夺成形體會變得 不均勻。 於本發明中,以濕熱環境氣氛來使得該濕熱凝膠化樹 脂濕熱凝膠化之際,較佳為在金屬模具内進行接觸壓成形 加工來製造纖維成形體。此處所說的接觸壓成形加工,係 施加纖維構造物與金屬模具可接觸之程度的壓力之加工。 I所謂的接觸壓,係纖維構造物與金屬模具密合時施加金屬 模具本身重量,為包含到此程度之壓力的概念。該濕熱凝 膠化樹脂由於在濕熱環境氣氛凝膠化即會變得柔軟,所以 僅僅是成形的情況,成形壓力即使未變得相當高亦可。依 據接解壓成形加工,由於纖維成形體係一邊維持纖維之狀 態一邊以凝膠化物來固定纖維,所以可得到蓬鬆、柔軟之 成形體。前述金屬模具只要係例如不鏽鋼板般之輕薄的金 屬模具即足夠,亦可為緻密的網眼狀金屬模具。 ® 於本發明中,當纖維成形體需要硬度、或是需將濕熱 凝膠化樹脂壓展成為膜狀之凝膠化物的情況,能以通常之 製k纖維成形體的塵力來進行加熱加壓加工。 其次,針對本發明參照圖式做說明。圖1A〜C係本發 明之一實施形態之添加物附著纖維之截面圖。圖1A係以 聚丙烯做為芯成分2、以乙烯一乙烯醇共聚樹脂做為鞘成 分1之複合纖維5,鞘成分1係具有黏結劑樹脂之功能, 鞘成分1中係附著有添加物3。圖1B係以聚丙烯做為芯成 22 1296296 :,1、:乙婦—乙稀醇共聚樹脂做為崎1之複合纖維 為黏結^4分λ之/側係附著有乙稀—乙稀醇共聚樹脂做The dispersion solution - pure, into: treatment, or 疋 - edge ^ additive rain ..., formed into a predetermined shape. The heating method includes an exposure method, a method in an ambient atmosphere, a method of contacting the heating body, and the like. The moisture content at the time of imparting the additive dispersion solution to the 隹 隹 && The description is omitted here. [Month;] In the wet heat forming process, the crucible contains the fiber of the addition of the do not disperse solution, and the structure (4) the person-to-metal t (four) row is heated and pressurized. Heating in the state of moisture, the non-woven fabric itself will be moderately = long and easy to follow the shape of the metal mold, and it is easy to obtain a deep-drawn molded body. When the additive is heated as a dispersion solution, for example, the fiber structure can be obtained by Insert into a pair of metal molds and immerse them in hot water (9 (rc or more) to obtain a molded body. The wet heat forming process is performed under a humid hot atmosphere. The hot and cold forming processing temperature is above the gelation temperature of the gelled resin. ~ melting point - 2 (rc is better. The better wet heat forming processing temperature is 5 (^c or more. The preferred wet heat forming processing temperature is above 80 ° C. On the other hand, the better wet heat forming processing temperature is wet thermal gel Melting point of resin ·3〇°ς: below. Particularly good wet heat forming processing/severity is the melting point of wet heat gelling resin below -40 ° C. If wet hot forming processing 21 1296296 temperature is not full of wet heat gelling resin gel When the temperature is lowered, it is difficult to form a gelled product. If the wet heat forming processing temperature exceeds the dazzling point of the wet heat gelled resin, the melting point of the wet heat gelled resin may become uneven due to the melting point of the wet heat gelled resin. In the present invention, when the wet heat gelation resin is wet-gelled in a hot and humid atmosphere, it is preferred to perform a contact press forming process in a metal mold to produce a fiber molded body. The processing is a process of applying a pressure at which the fiber structure can be in contact with the metal mold. I is a so-called contact pressure, and the weight of the metal mold itself is applied when the fiber structure is in close contact with the metal mold, and the concept of pressure to the extent is included. Since the wet heat gelling resin is softened by gelation in a hot humid atmosphere, it is only a case of molding, and the molding pressure may not be made relatively high. In the fiber forming system, the fibers are fixed by gelation while maintaining the state of the fiber, so that a bulky and flexible molded body can be obtained. The metal mold is preferably a thin metal mold such as a stainless steel plate. It can also be a dense mesh-shaped metal mold. In the present invention, when the fiber molded body requires hardness or a wet-gelled resin is required to be rolled into a film-like gel, it can be used in the usual manner. The dusting force of the k-fiber molded body is subjected to heat and pressure processing. Next, the present invention will be described with reference to the drawings. Figs. 1A to 1C are cross-sectional views showing the additive-attached fibers according to an embodiment of the present invention. The polypropylene is used as the core component 2, and the ethylene-vinyl alcohol copolymer resin is used as the conjugate fiber 5 of the sheath component 1. The sheath component 1 has a function as a binder resin, and the sheath component 1 has an additive 3 attached thereto. Fig. 1B is made of polypropylene as a core 22 1296296 :, 1, : Ethyl-ethylene glycol copolymer resin as a composite fiber of Saki 1 for bonding ^ 4 points λ / side attached with ethylene - ethylene glycol Copolymer resin

杯於此黏結劑4中混合著添加物3。w 1C 、8與乙烯—乙烯醇共聚樹脂7以多分$配£ ^ 維9,乙焔7 m 夕刀割配置之複合纖 乙烯—乙烯酵共聚樹脂7係具有黏結劑樹脂之功 其週邊部附著有添加物3。 “ 圖二係、本叙明之一貫施形態之3層構造的不織布截面 •人“ 著添加物附著纖維層",",於内側配置著 k、、糸纖維層12之例。 不織:;二本二:之製造方法之一例的製程圖。將纖維或 或是人古、 内之含有添加物之添加物分散溶液 液33\巾加物與乙烯—乙烯醇共聚樹脂之添加物分散溶 -之中,以擠壓報34做擠壓,於蒸氣機35與吸氣機% 為;Si濕熱處理,然後在該狀態下加以捲繞,或是若是 帆布係以附設有—對加_ 37,37之圖案化用 籲#面賊不 S MM38,38來壓縮成形,對不織布 =賦予既定圖案模樣後,以捲繞機39做捲繞。亦可取 。二機35與吸氣機36,改用上下熱板以例如溫度"Ο :5分鐘之加壓處理。在其他實施形態方面尚有不設 作署^機35而僅以一對之加熱輥做壓縮成形之方法、不 ^布^機35而僅以附設有—對加熱輥37,37之圖案化用 布輸迗帶輥38,38做壓縮成形之方法。 ,4A〜F係顯示以本發明之一實施例所得之不織布及 成纖維附著有添加物之狀態,A係顯示不織布之掃描 23 1296296 電子顯微鏡平面照片(倍率100)、B為同截面照片(倍率 1〇〇)、c為同不織布表面之纖維表面放大照片(倍率㈧)、 D為同其他部分不織布的掃描電子顯微鏡平面照片(倍率 100)、E係同截面照片(倍率100)、F為同不織布表面之纖 維表面放大照片(倍率1〇〇〇)。 圖5A〜C係顯示以本發明之其他實施例所得之不織布 及其構成纖維附著有添加物之狀態,A係顯示不織布之掃 >描電子顯微鏡平面照片(倍率1〇〇)、B為同截面照片(倍率 > 10〇)、c為同不織布表面之纖維表面放大照片(倍率⑺⑻)。 圖7係本發明之纖維成形體之一實施形態之含有水分 與添加物之不織布之製造方法之一例製程圖。將不織布原 板31含改於槽32内之含有添加物之添加物分散溶液或是 3有添加物與乙烯一乙烯醇共聚樹脂之添加物分散溶液33 中,以擠壓輥34做擠壓。藉此,對於不織布賦予水分以 及添加物約500質量%。其次,密合於厚度〇 3mm之不鏽 鋼板製金屬模具呈為接處壓狀態,放入加工溫度。。之 熱風乾燥機進行10分鐘熱處理來做接觸壓加工。成形體 係製作成為圖8所示之用以覆蓋人的口鼻之罩體40、以及 圖9所示之空氣清靜機過濾器之打摺加工品5〇。 圖10係本發明之其他實施形態之添加物附著纖維或不 織布之製造方法之一例製程圖。將纖維或不織布原板31 έ /又於槽32内之含有添加物(例如氣體吸附性粒子)之水系 液或疋含有添加物(例如氣體吸附性粒子)與乙烯一乙烯醇 κ相* 曰之添加物分散溶液3 3中,以擠壓輕3 4做擠壓, 24 •1296296 以從下方吹出蒸氣之蒸氣機35做蒸氣處理,以乾燥機41 2 =燥並以捲繞機39做捲繞。圖11Α、Β*示係本發明之 2實施例所得之不織布及其構成纖維附著有添加物之狀 Α係顯示不織布之掃描電子顯微鏡平面照片(倍率 00)、Β為同不織布表面之纖維表面放大照片(倍率Μ⑼)。 以下依據實施例做更具體的 [實施例1] 做為研磨不織布係準備以下之物。 (不織布) 形成下述三層構成之水流交絡不織布。 弟1層與第3層係做為鞠成分之乙烯一乙 脂㈣卵,乙稀38莫爾%,溶點176。〇與做為芯成The cup 3 is mixed with the additive 3 in the binder 4. w 1C , 8 and ethylene-vinyl alcohol copolymer resin 7 with a multi-point $ with a v ^ dimension 9, 焔 7 m 夕 knife cut configuration of the composite fiber ethylene - ethylene glycol copolymer resin 7 series with the adhesive resin work its peripheral part attached There is additive 3. Fig. 2 is a non-woven cross section of a three-layer structure in accordance with the consistent embodiment of the present invention. • The person attaches an additive-attached fiber layer ", ", an example in which k and 糸 fiber layer 12 are disposed inside. Non-woven:; two two: a process map of one of the manufacturing methods. Dispersing and dissolving the fiber or the additive solution of the additive containing the additive in the human or the interior, and the additive of the ethylene-vinyl alcohol copolymer resin, and extruding it by extrusion 34 The steam machine 35 and the air extractor %; the Si heat treatment, and then wound in this state, or if the canvas is attached - the addition of _ 37, 37 patterning with the use of the face thief not S MM38, 38 is compression-molded, and a predetermined pattern is applied to the non-woven fabric = and then wound by a winder 39. Also available. The two machines 35 and the aspirator 36 are replaced with upper and lower hot plates for, for example, temperature "Ο: 5 minutes of pressurization. In other embodiments, there is a method in which the heating machine is not provided, and only a pair of heating rolls are used for compression molding, and the machine 35 is not provided, and only the patterning of the heating rolls 37 and 37 is attached. The cloth feed belt rolls 38, 38 are subjected to compression forming. 4A to F show the state in which the non-woven fabric and the fiber-made fabric obtained by the embodiment of the present invention are attached with the additive, and the A-system shows the scanning of the non-woven fabric. 23 1296296 Electron microscope plane photograph (magnification 100), B is the same cross-sectional photograph (magnification 1〇〇), c is a magnified photograph of the surface of the fiber with the surface of the non-woven fabric (magnification (eight)), D is a scanning electron microscope plane photograph (magnification of 100) with the other part of the non-woven fabric, E-system with the same cross-section photograph (magnification of 100), F is the same Enlarged photo of the fiber surface of the non-woven surface (magnification 1〇〇〇). Figs. 5A to 5C show a state in which the non-woven fabric obtained by another embodiment of the present invention and the constituent fibers thereof are adhered with an additive, and the system A shows a non-woven fabric sweep> a photomicrograph of a scanning electron microscope (magnification: 1), B is the same Cross-sectional photograph (magnification > 10 〇), c is an enlarged photograph of the surface of the fiber on the same non-woven surface (magnification (7) (8)). Fig. 7 is a process chart showing an example of a method for producing a non-woven fabric containing water and an additive according to an embodiment of the fiber molded body of the present invention. The non-woven original sheet 31 is changed to the additive-dispersed solution containing the additive in the tank 32 or the additive dispersion liquid 33 having the additive and the ethylene-vinyl alcohol copolymer resin, and is extruded by the pressing roll 34. Thereby, moisture and the additive are imparted to the nonwoven fabric in an amount of about 500% by mass. Next, a metal mold made of a stainless steel sheet having a thickness of 〇 3 mm is placed in a state of being pressed and placed at a processing temperature. . The hot air dryer performs heat treatment for 10 minutes for contact pressing. The molded body was produced into a cover body 40 for covering a person's mouth and nose as shown in Fig. 8, and a folded product 5 of the air cleaner filter shown in Fig. 9. Fig. 10 is a process chart showing an example of a method for producing an additive-attached fiber or a nonwoven fabric according to another embodiment of the present invention. Adding the fiber or the non-woven original plate 31 έ or the aqueous solution containing the additive (for example, gas-adsorbing particles) in the tank 32 or the hydrazine-containing additive (for example, gas-adsorbing particles) and the ethylene-vinyl alcohol κ phase* In the dispersion medium 3 3, extrusion is carried out by pressing light 34, and 24 • 1296296 is steamed by a steam machine 35 which blows steam from below, and the dryer 41 2 = dry and wound by a winder 39. Fig. 11A and Β* show a non-woven fabric obtained by the second embodiment of the present invention and a fluorene-based photograph of a non-woven fabric in which the constituent fibers are attached with an additive (magnification 00), and the surface of the fiber which is the same as the surface of the non-woven fabric is enlarged. Photo (magnification (9)). The following is more specific in accordance with the examples. [Example 1] The following were prepared as a non-woven fabric. (Non-woven fabric) A water flow entanglement non-woven fabric having the following three layers is formed. The first layer and the third layer of the brothers are ethylene-ethyl ester (tetra) eggs, bismuth 38 mol%, and melting point 176. 〇 and as a core

丙知[? S SO. C A ^ 5〇之比例的芯鞘型複合纖維(纖度:2.8dtex, 戴、准長度· 51mm)所構成之梳棉纖維網,單位面 層皆為30g/m2。 所J 2層係人造絲纖維(纖度:1.7dtex ’纖維長度:4〇匪) ^之梳棉纖維、網,單位面積重量為30g/m2。 90二述Γ層構成之水流交絡不織布之單位面積重量為 進不織布係以第1層/第2層/第3層之順序疊合, 進灯6MPa之高壓水流 N /爪慝理,使侍厚度方向之纖維交絡。 (添加物分散溶液) 、 :仵做為添加物之曰本輕金屬公司製造,,氧化鋁 粒徑0·7μιη)以1供田 、弓 貝S %的比例在水中懸浮成為添加物分散 25 j296296 溶液(研磨劑溶液)。 (研磨劑之賦予與凝膠加工) 織布浸潰於該研㈣溶液中,以軋輥機(_咖The carded fiber web composed of the core-sheath type composite fiber (denier: 2.8 dtex, wearing, quasi-length, 51 mm) of the ratio [? S SO. C A ^ 5 ,) has a unit surface layer of 30 g/m 2 . The J 2 layer was a rayon fiber (denier: 1.7 dtex ‘fiber length: 4 〇匪) ^ carded fiber, net, and the basis weight was 30 g/m 2 . 90 二 Γ 构成 水 水 水 水 水 不 水 水 水 水 水 水 水 水 水 水 水 水 水 水 水 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 The direction of the fiber is entangled. (Additional dispersion solution): 仵 仵 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻 轻(abrasive solution). (Grinding agent and gel processing) The woven fabric is immersed in the research (4) solution to roll machine (_Cai

(研磨特性評價試驗) 將下述之墨水塗覆於不鏽鋼板與陶器皿上,乾燥後使 用各研磨材來去除油污。油污之去除係以人的手對各樣本 施加相同的力量進行摩擦。墨水與評價物體以及評分如下 所示。 的::康里成為表1所示數值的方式進行調整。又,所謂 10“係水分量與添加物量之和相對於不織布質量乘以 嫌之值。其次於加熱至12代的上下熱板張設帆布輸送 t_anvas net) ’於其間夾入不織布,以0崩Mpa的壓 力進行2秒鐘的凝膠加卫。其次以⑽。c之熱風來乾燥。 (1) 墨水 A:寺西化學工業製油性墨水(N〇5〇〇) B ·夏基海特公司製造油性墨水(artiine) C :謝普拉公司製造油性墨水(海瑪奇) D :三菱鉛筆公司製造油性墨水(三菱馬卡匹絲) E :櫻花克雷帕斯公司製造油性墨水(麥尼姆) (2) 評價物體與研磨材之狀態 a :不鏽鋼板 b :陶器m dry :在乾燥狀態使用 26 1296296 wet :沾水後甩脫水之狀態下使用 (3)評分 6分:摩擦次數5次可使得油污完全消失 5分:摩擦次數1〇次可使得油污完全消失 4刀·摩擦次數2 0次可使得油污完全消失 3分:摩擦次數30次可使得油污完全消失 2刀·摩擦次數3 0次仍部分有些許的油污殘留 1分:摩擦次數3〇次仍殘留一半程度之油污 _ 〇分·摩擦次數3 0次油污仍幾乎不會掉落 又,評價樣本係各試驗5個。研磨性試驗之結果係總 結於表1。 又,所彳亍不織布及其構成纖維附著有添加物之狀態係 表不於圖4A〜F。 [比較例1] 形成下述三層構成之水流交絡不織布。 第1層與第3層係乙烯—乙酸乙婦酯共聚樹轉va, 炼點1〇rc)與聚丙婦呈50:50之比例的芯顆型複合纖維(纖 度纖維長度:51mm)所構成之梳棉纖維網,單 位面積重量各層皆為3〇g/m2。 第2層係人造絲纖維(纖度:1·7(^χ,纖維長度·偏叫 所構成之梳棉纖維網,單位面積重量為3〇g&2。 前述三層構成之水流交絡不織布之單位面積重量為 _。此不織布係以第…第2層/第3層 進行6MPa之高犀皮治声师 ..^ ^ 、序且〇 之円&水肌處理,使得厚度方向之纖維交絡。 27 1296296 研磨J之賦予等其他的條件係與實施例1相同。研磨 性试驗之結果係總結於表1。 [比較例2] 幵y成下述二層構成之水流交絡不織布。 —第1層與第3層係乙烯一丙烯酸甲酯共聚樹脂(EMA, 炫,’占86 C )與水丙婦呈5〇 : 5〇之比例的芯鞘型複合纖維(纖 度·· 2.2dtex,纖維長度:45mm)所構成之梳棉纖維網,單 位面積重量各層皆為30g/m2。 1 第2層係人造絲纖維(纖度·· 1.7dteX,纖維長度·· 4〇mm) 所構成之梳棉纖維網,單位面積重量為3〇g/m2。 耵述三層構成之水流交絡不織布之單位面積重量為 9〇g/m2。此不織布係以第!層/第2層/第3層之順序疊合, 進行6MPa之高壓水流處理’使得厚度方向之纖維交絡。 研磨劑之賦予等其他的條件係與實施例丨相同。研磨 性試驗之結果係總結於表1。 [習知品1 ] ^ 使用附有市售研磨粒子之不織布刷(3M公司製造)來進 行與實施例1相同之研磨性試驗。結果係總結於表^。 [習知品2] 使用附有市售研磨粒子之海綿刷(愛司提公司製造)來 進行與實施例1相同之研磨性試驗。結果係總結於表^。 28 1296296(Polishing property evaluation test) The following ink was applied to a stainless steel plate and a ceramic dish, and after drying, each of the abrasive materials was used to remove oil stains. The removal of oil stains is performed by applying the same force to each sample by the human hand. Ink and evaluation objects and ratings are shown below. :: Conley adjusted to the value shown in Table 1. In addition, the sum of the 10" water content and the additive amount is multiplied by the value of the non-woven fabric. Secondly, it is heated to 12 generations of upper and lower hot plate to set the canvas transport t_anvas net). The pressure of Mpa is gelled for 2 seconds. Secondly, it is dried by hot air of (10).c (1) Ink A: Sisei Chemical Industry Oil-based Ink (N〇5〇〇) B · Made by Sharkey Head Company Oily ink (artiine) C: Sherpray manufactures oily ink (Haiqiqi) D: Mitsubishi pencil company manufactures oily ink (Mitsubishi macacine) E: Sakura Krepas manufactures oily ink (Menim) (2) Evaluation of the state of the object and the abrasive material a: Stainless steel plate b: Pottery m dry : Use in a dry state 26 1296296 wet: Use in a state of dehydration after dipping water (3) Score 6 points: 5 times of rubbing times can make Oil stain completely disappears 5 points: the number of rubbing times 1 可 can make the oil completely disappear 4 knives · the number of rubbing 2 times can make the oil completely disappear 3 points: the number of rubbing times 30 times can make the oil completely disappear 2 knives · friction times 30 times still Partially a little oil residue 1 point : The number of rubbing times remains at half the level of oil _ 〇 points · number of rubs 3 times the oil stains will almost never fall, and the evaluation sample is 5 tests. The results of the abrasive test are summarized in Table 1. The state in which the non-woven fabric and the constituent fibers adhered to the additive are shown in Figs. 4A to 4F. [Comparative Example 1] A water flow entanglement nonwoven fabric having the following three-layer structure was formed. The first layer and the third layer were ethylene- A carded fiber web composed of a core-type composite fiber (fineness fiber length: 51 mm) having a ratio of 50:50 in the ratio of the copolymer of the ethyl acetate of the ethyl acetate to the va, and a ratio of 50:50 to the polypropylene, each layer of the weight per unit area It is 3〇g/m2. The second layer is rayon fiber (denier: 1. 7 (^χ, fiber length, partial twist, composed of carded fiber web, unit weight: 3〇g& 2. The above three layers The weight per unit area of the water flow undulation non-woven fabric is _. This non-woven fabric is made of the second layer/third layer of 6 MPa high rhino skin treatment.. ^ ^ , sequence and 〇 円 & water muscle treatment, The fibers in the thickness direction are entangled. 27 1296296 Other conditions and implementation of the grinding J The same is true. The results of the polishing test are summarized in Table 1. [Comparative Example 2] 幵y is a water-flow entangled non-woven fabric composed of the following two layers. - First layer and third layer of ethylene-methyl acrylate copolymer resin ( EMA, Hyun, '86 C) and the water-acrylic woman is 5 〇: 5 〇 ratio of core-sheath type composite fiber (denier · 2.2 dtex, fiber length: 45 mm) composed of carded fiber web, weight per unit area Each layer was 30 g/m2. 1 The second layer of rayon fiber (denier · 1.7 dteX, fiber length · 4 mm) composed of a carded fiber web having a basis weight of 3 〇g/m2. The weight per unit area of the three-layered water flow undulation non-woven fabric is 9〇g/m2. This non-woven fabric is the first! The layers/layer 2/layer 3 are superimposed in sequence, and a high pressure water flow treatment of 6 MPa is performed to make the fibers in the thickness direction entangle. Other conditions such as imparting an abrasive are the same as those in the examples. The results of the abrasive test are summarized in Table 1. [Knowledge 1] ^ The same polishing test as in Example 1 was carried out using a non-woven cloth brush (manufactured by 3M Company) containing commercially available abrasive particles. The results are summarized in Table ^. [Knowledge 2] The same polishing test as in Example 1 was carried out using a sponge brush (manufactured by Esther) containing commercially available abrasive particles. The results are summarized in Table ^. 28 1296296

#^趄爾左1< 總平均分數 (N irl v〇 rn (N tri 寸 ir! W PQ wet 1 1 v〇 VO VO VO Ό MD vo v〇 v〇 a wet Ό VO 1 Os CO ro I> ro rn 寸· cn 寸· 卜 in VO a I' 寸 〇· O d 00 d 1 VO d o O O O O m rn 卜 r4 Q Xi wet 1 VO 1 v〇 VO wS v〇 00 v〇 v〇 l> uS cd wet VO VO Ό 1 VO 00 (N ro ON CN rn 寸· ro Ό l> Λ I' v〇 r〇 CN rn 々 rn 1 寸 rn o 〇 〇 O O l> rn MD U wet 1 v〇 1 VO Ό in in 卜 ro cd wet 寸· 寸· 1 oo 寸· o 寸 rn t—H m m m — in cd I' <N CO 00 CN 1 m o O 〇 O O 寸 m PQ wet 1 VO 1 v〇 00 in >n 寸 CN wS ro m· CO uS 卜 v〇 a wet v〇 Ό vo 1 VO m 00 CO 寸 rn O — v〇 a vo VO V<D 1 VO O 寸 CO (N CS rn v〇 < Xi wet 1 1 VO uS 00 oo ON 寸· 寸· — VO VO cd wet v〇 Ό VO 1 VO r〇 oo (N a\ CN <n vo VO ci I' v〇 v〇 1 r〇 ro ro rn — rn 寸· ro uS Ό 氧化鋁附著率 (質量%) t—H t—1 寸 r-H CO oo r*H 平均分數 (M i—H 卜 平均分數 CO 平均分數 平均分數 平均分數 實施例 比較例 實施例1 比較例1 比較例2 習知品1 習知品2 * 1296296 如表1所示般,本實施例之含有添加物附著纖維之不 織布展現與市售研磨材大致相同等級之研磨性。再者 實施例之含有添加物附著纖維之不織布,添加物不會2 洛,耐久性可得到良好的結果。添加物不脫落對於透鏡與 半導體之研磨等特別有用。 [實施例2] (不織布) 使用由實施例丨之芯鞘型複合纖維所構成之單位面積 重量l〇〇g/m2之水流交絡不織布(水壓6M]pa之高壓水流产 理)。 /;,L ^ (加工順序與條件) 將該不織布含浸於含有界面活性劑(烷基之碳數為9之 聚氧化乙烯烷基苯酚醚)〇」質量%之水溶液中、擠壓來做 鈾處理。其次,浸潰於乙烯一乙烯醇共聚樹脂(EVOH)粉末 (日本合成化學公司製造,商品名「索阿諾魯」,粉末類型 B-7 ’乙烯29莫爾%,熔點188。〇與活性碳(庫拉雷化學公 司製造,商品名「庫拉雷可魯」PL — D)之水分散溶液中, 、軋1½機做搐壓。之後,使用熱板油壓加壓機(將上下熱板 加熱)’於帆布輸送帶網之間夾入不織布施行凝膠加工。加 熱溫度為120X:、加壓壓力為〇〇32MPa,加熱時間為2分 4里。之後洗掉殘餘量之添加物,以1〇(rc之熱風做乾燥。 則述活性碳係強固且均勻地附著著。所得之含有添加 物附著纖維之不織布的結果係總結於表2。 30 1296296 [實施例3] 除了使用人造絲纖維! .7dtex、5 lmm所構成之6〇g/m2 之水流交絡不織布(水壓6MPa之高壓水流處理)以外,其 餘與實施例2同樣來進行處理。 —前述活性碳係強固且均勻地附著著。所得之添加物附 者不織布的結果係總結於表2。 [貫施例4 ] 二了使用聚醋纖維l 7dtex、51mm所構成之卿^之 水^交絡不織布(水壓6MPa之高壓水流處理)以外,其餘 人貝知例2同樣來進行處理。 “前述活性碳係強固且均勻地附著著。所得之添加物附 者不織布的結果係總結於表2。 [貫施例5 ] 除了使用聚丙烯纖維H,、51mm所構成之6〇g/m2 水流交絡不織布(水壓6Mpa之高壓水流處理)以外,其 餘與實施例2同樣來進行處理。 前述活性碳係強固且均句地附著著。所得之添加物附 者不織布的結果係總結於表2。 31 1296296 表2 實施例 編號 EV0H粉末+活性碳之分散溶液 挾帶率 (質量%) 全附著率 (質量%) EV0H附著率 (質量W 活性碳附著率 (質量%) EV0H粉末量 (質量%) 活性碳量 (質量%) 實施例2 1 5 425 63 11 52 3 5 500 77 29 48 3 10 498 85 20 65 實施例3 1 5 452 52 9 43 3 5 565 94 35 59 3 10 550 96 22 74 實施例4 1 5 556 67 11 56 3 5 820 165 62 103 3 10 575 105 24 81 實施例5 1 5 582 67 11 56 3 5 688 106 40 66 3 10 622 Π7 27 90#^趄尔左1< Total average score (N irl v〇rn (N tri inch ir! W PQ wet 1 1 v〇VO VO VO Ό MD vo v〇v〇a wet Ό VO 1 Os CO ro I&ro; ro Rn inch · cn inch · 卜 in VO a I' inch 〇 · O d 00 d 1 VO do OOOO rn 卜 r4 Q Xi wet 1 VO 1 v〇VO wS v〇00 v〇v〇l> uS cd wet VO VO Ό 1 VO 00 (N ro ON CN rn inch · ro Ό l> Λ I' v〇r〇CN rn 々rn 1 inch rn o 〇〇OO l> rn MD U wet 1 v〇1 VO Ό in in Ro cd wet inch · inch · 1 oo inch · o inch rn t—H mmm — in cd I' <N CO 00 CN 1 mo O 〇OO inch m PQ wet 1 VO 1 v〇00 in >n inch CN wS ro m· CO uS 卜 v〇a wet v〇Ό vo 1 VO m 00 CO inch rn O — v〇a vo VO V<D 1 VO O inch CO (N CS rn v〇< Xi wet 1 1 VO uS 00 oo ON inch · inch · — VO VO cd wet v〇Ό VO 1 VO r〇oo (N a\ CN <n vo VO ci I' v〇v〇1 r〇ro ro rn — rn inch·ro uS 氧化铝 alumina adhesion rate (% by mass) t—H t—1 inch rH CO oo r*H average score (M i—H average score CO average Numerical average score average score Example Comparative Example Example 1 Comparative Example 1 Comparative Example 2 Conventional product 1 Conventional product 2 * 1296296 As shown in Table 1, the non-woven fabric containing the additive-attached fiber of the present embodiment exhibited substantially the same as the commercially available abrasive material. The polishing property of the grade. In addition, the non-woven fabric containing the additive-attached fibers in the examples does not have a good effect on the durability, and the durability is excellent. The addition of the additive is particularly useful for polishing the lens and the semiconductor. 2] (non-woven fabric) The water flow entangled non-woven fabric (water pressure 6M]pa high-pressure water flow produced by the core-sheath type composite fiber of the embodiment 〇〇 is used. /;, L ^ (Processing sequence and conditions) The non-woven fabric is impregnated with an aqueous solution containing a surfactant (alkyl group having a carbon number of 9 polyoxyethylene alkylphenol ether) 质量 mass%, and extruded into uranium deal with. Next, it was impregnated with ethylene-vinyl alcohol copolymer resin (EVOH) powder (manufactured by Nippon Synthetic Chemical Co., Ltd. under the trade name "Soanoru", powder type B-7 'ethylene 29 mol%, melting point 188. 〇 and activated carbon (In the water dispersion solution manufactured by Kuraray Chemical Co., Ltd. under the trade name "Kura Rekoru" PL-D), the rolling machine is used for rolling. After that, the hot plate hydraulic press is used (the upper and lower hot plates will be used). Heating) 'The non-woven fabric is sandwiched between the canvas conveyor belt nets. The heating temperature is 120X: the pressing pressure is 〇〇32MPa, and the heating time is 2 minutes and 4 miles. After that, the residual amount of the additive is washed away. 1 〇 (the hot air of rc is dried. The activated carbon is strongly and uniformly adhered. The results of the resulting non-woven fabric containing the additive-attached fibers are summarized in Table 2. 30 1296296 [Example 3] In addition to the use of rayon fibers Other than the water flow entanglement nonwoven fabric of 6 〇g/m2 composed of 7 dtex and 5 lmm (high-pressure water flow treatment with a water pressure of 6 MPa), the treatment was carried out in the same manner as in Example 2. The activated carbon was strongly and uniformly adhered thereto. The resulting additive is attached The results of the non-woven fabrics are summarized in Table 2. [Example 4] The other is the use of polyester fiber l 7dtex, 51mm composed of water ^ entangled non-woven fabric (water pressure 6MPa high pressure water flow treatment), the rest of the people The treatment of Example 2 was carried out in the same manner. "The activated carbon was strongly and uniformly adhered. The results of the obtained additive-attached nonwoven fabric are summarized in Table 2. [Example 5] In addition to the use of polypropylene fiber H, 51 mm The treatment was carried out in the same manner as in Example 2 except that the 6 〇g/m2 water flow entangled nonwoven fabric (high pressure water flow treatment at a water pressure of 6 MPa) was used. The activated carbon was strong and uniformly attached. The obtained additive was attached. The results of the non-woven fabric are summarized in Table 2. 31 1296296 Table 2 Example No. EV0H powder + activated carbon dispersion solution entrainment rate (% by mass) Full adhesion rate (% by mass) EV0H adhesion rate (mass W Activated carbon adhesion rate (quality %) EV0H powder amount (% by mass) Activated carbon amount (% by mass) Example 2 1 5 425 63 11 52 3 5 500 77 29 48 3 10 498 85 20 65 Example 3 1 5 452 52 9 43 3 5 565 94 35 59 3 10 550 96 22 74 Example 4 1 5 556 67 11 56 3 5 820 165 62 103 3 10 575 105 24 81 Example 5 1 5 582 67 11 56 3 5 688 106 40 66 3 10 622 Π7 27 90

[實施例6] 第1層與第3層係實施例1之乙烯一乙烯醇共聚樹脂 (EV〇H)與實施例1之聚丙烯呈· 50 : 50之比例的分割型複 合纖維(纖度·· 3.3dtex ’纖維長度:51mm)所構成之梳棉纖 維網,單位面積重量各層為3〇g/m2。第i層與第3層之間 的第2層係實施例丨之人造絲纖維與聚醋纖維(纖度: ⑶⑽,纖維長度:51mm)以1:1混合之梳棉纖維網,單 量為—以下,以與實施例"目同之方法做 成水流父絡不織布,進杆 …η, π 工。與實施例1同樣,添 力物係強固且均勻地附著 附荖右、大★札 ^传之不織布及其構成纖維 附考有添加物之狀態係示於圖5A〜c。 32 1296296 [實施例7] (不織布原板之製作) 準備鞘成分為乙烯一乙烯醇共聚樹脂(EVOH,乙晞含 有里38莫爾%’溶點176C)、芯成分為聚丙稀(pp,溶點 bit)之EVOH : PP為50 : 50之比例(體積比)之芯鞘型複 合纖維(纖度:3.3dtex,纖維長度:51mm)。再者,準備鞘 成分為聚乙烯(PE,熔點i32t )、芯成分為聚丙烯(PP,溶 二占161 C )之纖度· 2 · 2 dteX ’纖維長度· 5 1 mni之乾熱接著 籲 性複合纖維(大和紡織製造,NBF(H))。 將前述芯鞘型複合纖維75質量%與前述乾熱接著性纖 維25質量%混合,以半隨機梳棉機進行開纖,製作單位面 積重量45g/m2之梳棉網(card web)。其次,將該梳棉網載 放於90網眼之平織支持體上,自在該梳棉網之寬方向配 置一列孔口(直徑· 0.12mm,間距:0 · 6mm)之噴嘴朝向該 梳棉網以水壓3MPa進行喷射之後,進一步以水壓4MPa 進行噴射。接著,將該梳棉網反過來,自該噴嘴以水壓4MPa 籲噴射水流,製作水流交絡不織布原板。 (添加物之準備) 在添加物方面係使用活性碳粒子:「太閣SA1〇〇〇」(二 村化學製造,平均粒徑1〇μιη)。 (含有添加物附著纖維之不織布的製作) ' 將前述不織布原板浸潰於由水中分散有8質量%之活 性碳粒子所構成之添加物分散溶液(2(rc ) _,使用軋輕機 以線壓約60N/cm之擠壓壓力來調整挾帶率。其次,使用 33 1296296 可從不織布原板下部吹出蒸氣之蒸氣機,對於含浸有添加 物分散溶液之該不織布原板以槽内溫度102。(:、加工時間 15秒施以条氣處理,以熱風乾燥器(1〇〇。〇)乾燥,得到本 發明之不織布。所得之不織布的單位面積重量為68g/m2, 約23 g/m2之添加物呈現附著狀態。所得之不織布及其構 成纖維附著有添加物之狀態係示於圖11A-B。所得之不織 布維持著纖維狀態,添加物係以露出於纖維表面之狀態附著。 [實施例8〜U] ’ 做為氣體吸附材係準備以下之物。 (不織布原板之製作) 準備鞘成分為乙烯一乙烯醇共聚樹脂(EVOfj,乙烯含 有量38莫爾%,熔點176。〇、芯成分為聚丙烯(pp,熔點 161 C )之EVOH · PP為5〇 : 50之比例(體積比)之芯鞘型複 合纖維(纖度:2.8dtex,纖維長度:51mm)。 將前述芯鞘型複合纖維以半隨機梳棉機進行開纖,製 作具有表3所示單位面積重量之梳棉網。其次,將該梳棉 網載放於90網眼之平織支持體上,自在該梳棉網之寬方 向配置一列孔口(直控:〇· 12mm,間距:0.6mm)之喷嘴朝 向該梳棉網以水壓3MPa來喷射水流之後,進一步以水壓 4MPa進行喷射。接著,將該梳棉網反過來,自該喷嘴以 水壓4MPa喷射水流,製作實施例8〜丨!所使用之水流交絡 不織布原板。 (添加物之準借) 在添加物方面係準備氣體吸附性粒子。做為氣體吸附 34 1296296 性粒子係使用活性碳 丁 犀拉雷可魯PL-D」(康把爺 化學公司製造,椰子Μ石山1 μ 」W車拉田 耶千风妷,平均粒徑40〜5〇μηι)。 (含有添加物附著纖維之不織布的製作) 將前述不織布原板浸潰於由水中分散有[Example 6] The first layer and the third layer were the ethylene-vinyl alcohol copolymer resin (EV〇H) of Example 1 and the polypropylene of Example 1 in a ratio of 50:50 (fineness· · The carded web composed of 3.3dtex 'fiber length: 51mm' has a weight per unit area of 3〇g/m2. The second layer between the i-th layer and the third layer is a 1:1 mixture of rayon fibers and polyester fibers (denier: (3) (10), fiber length: 51 mm), a single amount is - Hereinafter, in the same manner as in the embodiment, the water flow parent is not woven, and the rod is ... η, π. In the same manner as in the first embodiment, the reinforcing material is strongly and uniformly adhered to the right and the large non-woven fabrics and the constituent fibers thereof. The state in which the additives are attached is shown in Figs. 5A to 5C. 32 1296296 [Example 7] (Preparation of non-woven original board) Preparation of sheath component is ethylene-vinyl alcohol copolymer resin (EVOH, acetonitrile contains 38% Mool% 'dissolving point 176C), and core component is polypropylene (pp, melting point) Bit) EVOH: PP is a 50:50 ratio (volume ratio) core-sheath type composite fiber (denier: 3.3 dtex, fiber length: 51 mm). Furthermore, the preparation of the sheath component is polyethylene (PE, melting point i32t), the core component is polypropylene (PP, dissolved in 161 C), the fineness · 2 · 2 dteX 'fiber length · 5 1 mni dry heat and then appeal Composite fiber (made by Daiwa Textile, NBF(H)). 75 mass% of the core-sheath type composite fiber and 25 mass% of the dry heat-bonding fiber were mixed, and opened by a semi-random carding machine to prepare a card web having a basis weight of 45 g/m2. Next, the card web is placed on a 90-mesh plain woven support, and a row of nozzles (diameter · 0.12 mm, spacing: 0 · 6 mm) is arranged in the width direction of the card web toward the carding net. After the injection was carried out at a water pressure of 3 MPa, the injection was further carried out at a water pressure of 4 MPa. Next, the card web was reversed, and a water jet was sprayed from the nozzle at a water pressure of 4 MPa to produce a water flow entangled nonwoven original plate. (Preparation of Additives) Activated carbon particles were used for the additive: "Taige SA1" (manufactured by Yoshimura Chemical Co., Ltd., average particle size: 1 〇μιη). (Preparation of non-woven fabric containing additive-attached fibers) The impregnated raw sheet was immersed in an additive dispersion solution (2(rc)_) composed of 8 mass% of activated carbon particles dispersed in water, using a rolling machine to wire Pressing the extrusion pressure of about 60 N/cm to adjust the entrainment rate. Secondly, using 33 1296296, a steam machine capable of blowing steam from the lower portion of the non-woven original plate, the inner temperature of the non-woven original plate impregnated with the additive dispersion solution is 102. The processing time was 15 seconds, and the mixture was dried by a hot air dryer (1 Torr.) to obtain the non-woven fabric of the present invention. The obtained non-woven fabric had a basis weight of 68 g/m 2 and an additive of about 23 g/m 2 . The state of adhesion is shown. The obtained non-woven fabric and the state in which the constituent fibers adhere to the additive are shown in Fig. 11A-B. The obtained non-woven fabric maintains the fiber state, and the additive adheres to the surface of the fiber. [Example 8~ U] ' Prepare the following for the gas adsorption material system. (Preparation of non-woven original board) Prepare the sheath component as ethylene-vinyl alcohol copolymer resin (EVOfj, ethylene content 38 mol%, melting point 1 76. 芯 〇, core composition of polypropylene (pp, melting point 161 C) EVOH · PP is 5 〇: 50 ratio (volume ratio) core sheath type composite fiber (denier: 2.8 dtex, fiber length: 51 mm). The core-sheath type composite fiber was opened by a semi-random carding machine to produce a carding net having a basis weight per unit area shown in Table 3. Secondly, the carding net was placed on a 90-mesh plain woven support body. A nozzle of a row of orifices (straight control: 〇·12 mm, pitch: 0.6 mm) disposed in the width direction of the card web is sprayed toward the card web at a water pressure of 3 MPa, and then further sprayed at a water pressure of 4 MPa. The card web was reversed, and a water flow was sprayed from the nozzle at a water pressure of 4 MPa to prepare a water flow entangled non-woven original sheet used in Example 8 to 丨! (Approved by the additive) The gas adsorbing particles were prepared in terms of the additive. As a gas adsorption 34 1296296 particle system using activated carbon Ding Rhiraruru PL-D" (made by Kang Ting Chemical Co., Ltd., coconut ochre mountain 1 μ) W car Latian Ye Qianfeng, average particle size 40 ~5〇μηι). (with additive attached fiber The production of the non-woven fabric) is immersed in the original non-woven fabric in the water

述活性碳粒子所椹&夕% i t 里月丨J β 冓成之添加物分散溶液(20。〇中,以軋輥 機之擠壓塵力炎纲勉*4+ _ ^ ^挾▼率,將活性碳粒子之附著量調整The activated carbon particles are 椹 amp amp it it it β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β β Adjust the amount of activated carbon particles

:、3所不之數值。又,所謂的挾帶率係水分量與活性碳 =之和相對於不織布原板質量乘卩⑽之值。其次,將含 浸有添加物分散溶液之該不織布原板以線徑:0·3_、網 眼數:,30條/inch, 25條/⑽之2片平織塑膠雜 也、40cm)做挾持,載放於加熱到15〇它之熱板上,進 而將上側之該塑膠網以鋁片〇g/cm2)被覆做15分鐘之濕熱 2理。將所得之不織布水洗’以熱風乾燥器(100。〇乾燥, 得到本發明之不織布。 [貫施例1 2 ] 將與貝施例8所使用之水流交絡不織布原板相同之不 織布原板浸潰於由水中分财5質量%之前述活性碳粒子 所構成之添加物分散溶液(95r)* 3〇秒之後上拉。接著, 將该不織布原才反勾掛支撐直到該不織布原板之溫度成為5〇 C之後,將該不織布水洗,以熱風乾燥器(100。〔))乾燥, 得到本發明之不織布(氣體吸附材)。 、表3針對實施例8〜12之不織布(氣體吸附材)顯示了不 线布原板之單位面積重量、活性碳粒子之附著量、活性石炭 粒子之附著率以及不織布(氣體吸附材)之單位面積重量。 35 i296296 表3 實施例 編號 不織布原板之單位 面積重量(g/m2) 活性碳粒子之附 著量(g/m2) 活性a 率(質 8 113 159 141 9 114 98 86 10 110 114 104 11 41 43 105 12 113 27 24 著 不織布(氣體吸附材)之單 位面積重量(g/m2) 272:, 3 not worth the value. Further, the so-called entrainment ratio is a value obtained by multiplying the sum of the water content and the activated carbon by the mass of the non-woven original sheet by (10). Next, the original non-woven fabric impregnated with the additive dispersion solution is held in a wire diameter: 0·3_, mesh number: 30 pieces/inch, 25 pieces/(10) of two pieces of plain woven plastic miscellaneous, 40 cm), and placed. The plastic web was heated to 15 〇 on the hot plate, and the upper plastic web was coated with aluminum sheet 〇g/cm 2 ) for 15 minutes. The obtained non-woven fabric was washed with water in a hot air dryer (100. Drying to obtain a non-woven fabric of the present invention. [Comprehensive Example 1 2] The original non-woven fabric sheet which was the same as the original water-repellent nonwoven fabric used in Example 8 was impregnated with 5 % by mass of the above-mentioned activated carbon particles in the water, the additive dispersion solution (95r)* is pulled up after 3 sec. Then, the non-woven fabric is back-supported until the temperature of the non-woven original sheet becomes 5 〇C. Thereafter, the nonwoven fabric was washed with water and dried by a hot air dryer (100 ° ()) to obtain a nonwoven fabric (gas adsorbent) of the present invention. Table 3 shows the basis weight of the original non-woven fabric, the adhesion amount of the activated carbon particles, the adhesion ratio of the activated carbonaceous particles, and the unit area of the nonwoven fabric (gas adsorbent) for the nonwoven fabric (gas adsorbent) of Examples 8 to 12. weight. 35 i296296 Table 3 Example No. Unit weight of non-woven original board (g/m2) Attachment amount of activated carbon particles (g/m2) Activity a rate (quality 8 113 159 141 9 114 98 86 10 110 114 104 11 41 43 105 12 113 27 24 Weight per unit area (g/m2) of non-woven fabric (gas adsorbent) 272

定了除臭劑之2片的紡黏(spunb〇nd)不織布間使得活性碳 粒子以熱熔劑做固定所得者。 [比較例3 ] 準備含有自交聯型丙烯酸醋乳膠(曰本碳化物工業製 造,商品名「尼卡索魯FX_555A」)15質量%與前述活性碳 敉子10質量%之添加物分散溶液。其次,將與前述實施例 S所使用之水流交絡不織布原板相同之不織布原板浸潰於 该溶液中,以軋輥機做擠壓,使用熱風乾燥機在溫度14〇 X:、處理時間15分鐘進行乾燥、硬化,得到活性碳粒子 之附著量為38g/m2之化學黏附(chemicalb〇nd)不織布。 [比較例4] 比較例4係準備V〇c氣體吸附片(旭成化纖維製造, 商品名「謝米阿V」,單位面積重量134g/m2,活性碳粒 孑之附著量為約40g/m2),此v〇c氣體吸附片係於表面固 [VOC氣體吸附試驗方法] 將貫施例8〜12以及比較例3,4 之片材分別切斷為縱 36 1296296 lOcmx橫10cm之大小,放入容量5公升之公害分析用袋(商 品名「提德拉袋」),以成為表4〜6所示初期濃度的方式注 入空氣與調合之各VOC氣體。然後,以注入時刻為開始 時間,每隔一段時間以氣體檢測管來測定袋内之各VOC 氣體濃度。結果係示於表4〜6。又,於表4〜6中所謂的「ND」 係各VOC氣體濃度未滿所使用之氣體檢測管之測定濃度 (2ppm)的情況。 表4 初期濃度 30分鐘後 1小時後 3小時後 6小時後 甲醛殘存濃 實施例8 100 4 3 2 2 度(卿) 實施例12 100 9 8 — — 20 3 3 一 — 比較例3 100 10 8 7 7The spunb〇nd non-woven fabric of two pieces of deodorant was prepared so that the activated carbon particles were fixed by a hot melt agent. [Comparative Example 3] An additive dispersion solution containing 15% by mass of a self-crosslinking type acryl lactic acid latex (manufactured by Sakamoto Carbide Co., Ltd., trade name "Nicasol FX_555A") and 10% by mass of the above activated carbon tweezers was prepared. Next, the non-woven original sheet which is the same as the original water-free woven original sheet used in the above Example S was immersed in the solution, extruded by a roll mill, and dried using a hot air dryer at a temperature of 14 〇 X: and a treatment time of 15 minutes. And hardened to obtain a chemically bonded (chemicalb〇nd) nonwoven fabric in which the amount of activated carbon particles adhered was 38 g/m2. [Comparative Example 4] In Comparative Example 4, a V〇c gas adsorption sheet (manufactured by Asahi Kasei Fiber Co., Ltd., trade name "Shemier V" was produced, and the basis weight was 134 g/m2, and the adhesion amount of activated carbon particles was about 40 g/ M2), the v〇c gas adsorption sheet is attached to the surface [VOC gas adsorption test method] The sheets of the examples 8 to 12 and the comparative examples 3 and 4 are respectively cut into a length of 36 1296296 lOcmx and a width of 10 cm. A jewellery analysis bag (trade name "Tedlar bag") having a capacity of 5 liters was placed, and air and the combined VOC gas were injected so as to have an initial concentration shown in Tables 4 to 6. Then, the concentration of each VOC gas in the bag was measured by a gas detecting tube at intervals of the injection time as the start time. The results are shown in Tables 4 to 6. Further, the "ND" in Tables 4 to 6 is a case where the concentration of each VOC gas is less than the measured concentration (2 ppm) of the gas detecting tube used. Table 4 Initial concentration 30 minutes after 1 hour, 3 hours after 6 hours, formaldehyde residual concentration Example 8 100 4 3 2 2 degrees (Qing) Example 12 100 9 8 - 20 3 3 1 - Comparative Example 3 100 10 8 7 7

表5table 5

初期濃度 5分鐘後 30分鐘後 卜J、時後 曱苯殘存濃度 (ppm) 實施例9 20 10 2 ND 實施例12 23 4 ND ND 比較例4 20 11 4 ND 二曱苯殘存濃 度(ppm) 實施例9 24 11 ND ND 實施例12 24 5 ND ND 比較例4 24 15 5 ND 對二氣苯殘存 濃度(ppm) 實施例9 28 6 ND ND 實施例12 20 5 ND ND 比較例4 28 18 ND ND 37 Ϊ296296 表6 初期濃度 5分鐘後 30分鐘後 1小時·後 乙基苯殘存濃 實施例10 20 6 1 ND 度(I3pm) 實施例11 20 6 1 ND 實施例12 20 3 ND ND 比較例4 20 8 1.5 ND 苯乙烯殘存濃 實施例10 22 4 2 ---- 2 度(ppm) 實施例11 22 6 3 2 實施例12 24 4 2 2 比較例4 22 10 3 ----— 3 [結果] 如表4〜6所示般,使用實施例8〜n之不織布的情況, 相較於比較例3,4,各V0C氣體之濃度減少速度快,氣體 之吸附性能獲得提升。又,如表4所示般,實施例12相 較於比較合"雖活性碳粒子之附著量少,但展現與比較例 3同等之甲醛吸附性能。再者,如表5,6所示般,實施例 相較於比較例4雖活性碳粒子之附著量少,但氣體吸附性 能獲得提升。此被認為係實施例8〜12之不織布中之活性 碳粒子(氣體吸附性粒子)由纖維表面之濕熱凝膠化之凝膠 化物來附著1以氣體吸附性粒子係在露出於表面之狀能 下被附者’故相較於比較例3,4’氣體吸附性粒子之 面積的減少受到抑制。7 、 ^ 卩制又,貫施例8〜12之不織布保持著 !、維形狀’於破膠加工時並無不織布收縮之情事。又,者 施例8〜12之不織右*么々只 並…、氣體吸附性粒子脫落之情事。 38 1296296 [實施例13] 做為水質淨化材係準備以下之物。 (不織布原板之製作) 準備鞘成分為乙稀一乙稀醇共聚樹脂(EVOH ’乙烯含 有量38莫爾%,熔點176°C )、芯成分為聚丙烯(pP,熔點 161°C)之EV〇H : pp為50 : 50之比例(體積比)之芯鞘型複 合纖維(纖度:2_8dtex,纖維長度:51mm)。 將前述芯鞘型複合纖維以半隨機梳棉機進行開纖,製 ® 作單位面積重量101 g/m2之梳棉網。其次,將該梳棉網載 放於90網眼之平織支持體上,自在該梳棉網之寬方向配 置 列孔口(直徑:0· 12mm,間距:〇.6mm)之噴嘴朝向該 梳棉網以水壓3MPa來噴射水流之後,進一步以水壓4MPa 進行噴射。接著,將該梳棉網反過來,自該喷嘴以水壓4MPa 喷射水流,製作實施例1所使用之水流交絡不織布原板。 (添加物之準備) 在添加物方面係準備有機物吸附性粒子。做為有機物 籲吸附性粒子係使用活性碳粒子:「庫拉雷可魯」(庫 拉雷化學公司製造,椰子殼碳,平均粒徑4〇〜5叫叫。 (含有添加物附著纖維之不織布的製作) 將前述不織布原板浸潰於由水中分散有1〇質量%之前 述活性碳粒子所構成之添加物分散溶液(201 )中,以軋輥 機之擠壓壓力來調整挾帶率,將活性碳粒子之附著量調整 為表7所示之數值。其次,將含浸有添加物分散溶::: 不織布原板以線徑:〇.3mm、網眼數:縱3〇條/^^橫乃 39 1296296 條/inch之2片平織塑膠網(縱40cmx橫4〇cm)做挾持,載 放於加熱到150°C之熱板上,進而將上側之該塑膠網以紹 片(lg/cm2)被覆做15分鐘之濕熱處理。將所得之不織布水 洗,以熱風乾燥β (100 c )乾燥,得到本發明之不織布(水 質淨化材)。 [實施例14] 除了使用單位面積重量40g/m2之梳棉網,將附著該活 性碳粒子之際之水分散液中之活性碳粒子之濃度調整為5 _ 夤篁% ’以軋親機來調整挾帶率使得活性碳粒子之附著量 成為表1所示之數值以外,其餘與實施例13相同之方法 來得到本發明之不織布(水質淨化材)。 - 表7中針對貫施例13以及實施例14之不織布(水質淨 化材),顯示了不織布原板之單位面積重量、活性碳粒子之 附著量、活性碳粒子之附著率以及不織布(水質淨化材)之 單位面積重量。實施例13、14之不織布係保持著纖維形 狀,於凝膠加工時並無不織布之收縮。 實施例 不織布原板之單位 活性碳粒子之附 活性碳粒子之附著 不織布(水質淨化材)之單 編號 面積重量(g/m2) 著量(g/m2) 率(質量%) 位面積重量(g/m2) 13 101 90 89 191 14 40 20 50 60 [比較例5 ] 比較例5係準備活性碳纖維不織布(庫拉雷化學製造, # 1296296 商品名「庫拉庫提布」,單位面積重量約180g/m2)。 [水質淨化性能試驗方法]After 30 minutes after the initial concentration of 5 minutes, the residual concentration of benzene (ppm) after the J and the subsequent examples. Example 9 20 10 2 ND Example 12 23 4 ND ND Comparative Example 4 20 11 4 ND Residual concentration of diphenylbenzene (ppm) Example 9 24 11 ND ND Example 12 24 5 ND ND Comparative Example 4 24 15 5 ND Dioxane Residual Concentration (ppm) Example 9 28 6 ND ND Example 12 20 5 ND ND Comparative Example 4 28 18 ND ND 37 Ϊ296296 Table 6 Initial concentration 5 minutes after 30 minutes 1 hour · Post-ethylbenzene residue concentration Example 10 20 6 1 ND degree (I3pm) Example 11 20 6 1 ND Example 12 20 3 ND ND Comparative Example 4 20 8 1.5 ND Styrene Residual Example 10 22 4 2 ---- 2 degrees (ppm) Example 11 22 6 3 2 Example 12 24 4 2 2 Comparative Example 4 22 10 3 ----— 3 [Results As shown in Tables 4 to 6, in the case of using the non-woven fabrics of Examples 8 to n, the concentration of each V0C gas was decreased faster than that of Comparative Examples 3 and 4, and the adsorption performance of the gas was improved. Further, as shown in Table 4, in Example 12, although the amount of adhesion of the activated carbon particles was small, the formaldehyde adsorption performance equivalent to that of Comparative Example 3 was exhibited. Further, as shown in Tables 5 and 6, the amount of adhesion of the activated carbon particles was small as compared with Comparative Example 4, but the gas adsorption performance was improved. It is considered that the activated carbon particles (gas-adsorbing particles) in the non-woven fabrics of Examples 8 to 12 are adhered by the wet-thermal gelation of the surface of the fiber, and the gas-adsorbing particles are exposed to the surface. The decrease in the area of the lower adsorbent was lower than that of the comparative example 3, 4' gas-adsorbing particles. 7 , ^ 卩 又 , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , In addition, the case of the example 8 to 12 does not woven the right * 々 only ... and the gas-adsorbing particles fall off. 38 1296296 [Example 13] The following were prepared as a water purification material system. (Preparation of non-woven original board) Preparation of the sheath component is ethylene-ethylene glycol copolymer resin (EVOH 'Ethylene content 38 mol%, melting point 176 ° C), and the core component is polypropylene (pP, melting point 161 ° C) EV 〇H : Core-sheath type composite fiber with a ratio of 50:50 (volume ratio) (denier: 2_8 dtex, fiber length: 51 mm). The core-sheath type composite fiber was opened by a semi-random carding machine to make a carding net having a weight per unit area of 101 g/m2. Next, the card web is placed on a 90-mesh plain woven support, and a nozzle having a column aperture (diameter: 0·12 mm, pitch: 〇.6 mm) is disposed facing the card from the width direction of the card web. The net was sprayed with a water pressure of 3 MPa, and further sprayed at a water pressure of 4 MPa. Next, the card web was reversed, and a water flow was sprayed from the nozzle at a water pressure of 4 MPa to prepare a water flow entangled nonwoven original sheet used in Example 1. (Preparation of Additives) Organic adsorbent particles were prepared in terms of additives. As an organic matter-adsorbing particle system, activated carbon particles are used: "Kura Rekoru" (manufactured by Kuraray Chemical Co., Ltd., coconut shell carbon, average particle size 4〇~5 is called. (Non-woven fabric containing additive-attached fibers) (Production) The impregnated raw sheet is impregnated into an additive dispersion solution (201) composed of 1% by mass of the activated carbon particles dispersed in water, and the crucible ratio is adjusted by the extrusion pressure of the roll machine to activate The amount of carbon particles adhered was adjusted to the value shown in Table 7. Secondly, the impregnated with the additive was dissolved and dissolved::: Non-woven original board with wire diameter: 〇.3 mm, mesh number: vertical 3 〇 / / ^ 横 is 39 2 pieces of 1296296 pieces/inch of flat woven plastic net (longitudinal 40cmx horizontal 4〇cm) are placed on a hot plate heated to 150°C, and then the upper side of the plastic net is covered with a sheet (lg/cm2). The wet heat treatment was performed for 15 minutes, and the obtained non-woven fabric was washed with water and dried by hot air drying (100 c) to obtain a nonwoven fabric (water purification material) of the present invention. [Example 14] In addition to using a card having a basis weight of 40 g/m 2 Net, when the activated carbon particles are attached The concentration of the activated carbon particles in the dispersion was adjusted to 5 _ 夤篁%. The same method as in Example 13 was carried out except that the amount of the activated carbon particles was adjusted so that the adhesion amount of the activated carbon particles was changed to the value shown in Table 1. The non-woven fabric (water purification material) of the present invention was obtained. - The non-woven fabric (water purification material) of Example 13 and Example 14 in Table 7 shows the basis weight of the original nonwoven fabric, the adhesion amount of the activated carbon particles, and the activity. The adhesion rate of the carbon particles and the basis weight of the non-woven fabric (water purification material). The nonwoven fabrics of Examples 13 and 14 retained the fiber shape, and there was no shrinkage of the nonwoven fabric during the gel processing. Example Non-woven original sheet of activated carbon particles Single-numbered area weight (g/m2) of attached non-woven fabric (water purification material) with attached activated carbon particles (g/m2) Rate (% by mass) Bit area weight (g/m2) 13 101 90 89 191 14 40 20 50 60 [Comparative Example 5] Comparative Example 5 was prepared by preparing an activated carbon fiber nonwoven fabric (manufactured by Kuraray Chemical, #1296296, trade name "Kurakutibu", and having a basis weight of about 180 g/m2). [Water quality purification test method]

針對實施例13,14以及比較例3,5,以圖6所示之水循 壞式簡易試驗機來進行水質淨化性能試驗。如圖6所示般, 水循環式簡易試驗機2〇係由台座2 1、於台座2 1所安裝之 固定夹具22a,22b、藉由固定夾具22a來固定於台座21之 有底圓筒狀容器23、以及使得容器23内之水循環之泵24。 泵24係具備於容器23之底部開口 23a所安裝之管2乜、 以及藉由固定夾具22b固定於台座21之管24b,從容器23 之開口 23a將容器23内之水加以吸引,所吸引之水藉由管 24b朝容器23之上部排出。又,於本試驗中,針對實施例 13以及比較例5係對於容器23内注入化學需氧量為 40ppm之工廠廢水,針對實施例14以及比較例3係注入 為2〇PPm之工廠廢水。又,藉由在泵24所連接之電力調 整裝置(未圖示)將水的循環流量控制在6升/分鐘,於試驗 中將容器23内之工廠廢水的液量維持在丨升。 [试驗用樣本之製作方法] 〜W V Y別切 3cmx3cm之小片25(參照圖6)。其次分別針對實施例‘、、、 以及比較例3’5’以活性礙量成為…的方式秤取小’ 將所秤取之小片25 4入市售之茶包26(參照圖6) 驗用樣本零照目6)。又,於水質淨化性能試驗之^ 如圖6所示般,將試驗用樣本27浸潰於容器U : ’ 工廠廢水令,以金屬線28固定於固定夹具22b〇 則述 41 1296296 [C 0 D濃度測定方法] COD濃度係每到測定時間將容器23内之工廠廢水以 滴管採集至燒瓶中,利用共理化學研究所製造之簡易水質 分析製品「包裝試驗機」(WAK-COD,測定範圍0〜100mg/ 升)來與標準色做比色進行測定。結果顯示於表8。 表8 C0D 濃度(ppm )~~--—-- 初期濃度 10分鐘後 15分鐘後 30分鐘後 60分鐘後 120分鐘後 實施例13 —--- 40 30 " 30 28 16 — 貫施例14 20 '— 20 13 "Ϊ3 一 10 比較例3 20 — 20 20 20 20 比較例5 40 35~ 30 30 T8 ~ —For Examples 13 and 14 and Comparative Examples 3 and 5, the water purification performance test was carried out using the water-floating type simple tester shown in Fig. 6. As shown in Fig. 6, the water circulation type simple tester 2 is a bottomed cylindrical container which is fixed to the pedestal 21 by a pedestal 2 1 and fixing jigs 22a and 22b attached to the pedestal 2 1 by a fixing jig 22a. 23. A pump 24 that circulates water within the vessel 23. The pump 24 is provided with a tube 2A to which the bottom opening 23a of the container 23 is attached, and a tube 24b fixed to the pedestal 21 by the fixing jig 22b, and sucks the water in the container 23 from the opening 23a of the container 23, thereby attracting The water is discharged to the upper portion of the container 23 by the tube 24b. Further, in the present experiment, in Example 13 and Comparative Example 5, factory waste water having a chemical oxygen demand of 40 ppm was injected into the vessel 23, and factory waste water of 2 〇 PPm was injected into Example 14 and Comparative Example 3. Further, by controlling the circulation flow rate of water to 6 liter/min by the electric power adjusting device (not shown) connected to the pump 24, the amount of the factory waste water in the container 23 was maintained at a high level during the test. [Method for Producing Test Sample] ~ W V Y Cut a small piece 25 of 3 cm x 3 cm (see Fig. 6). Next, for the examples ', , and the comparative example 3'5', the small amount of the scaled piece 25 was put into the commercially available tea bag 26 (see Fig. 6). Zero photo 6). Further, in the water purification performance test, as shown in Fig. 6, the test sample 27 was immersed in the container U: 'factory waste water, and the metal wire 28 was fixed to the fixing jig 22b. 41 1296296 [C 0 D Concentration measurement method] The COD concentration system collects the factory wastewater in the container 23 into the flask in a dropper every time during the measurement, and uses the simple water quality analysis product "packaging test machine" (WAK-COD, measuring range) manufactured by the Institute of Synthetic Chemistry. 0 to 100 mg / liter) to measure color with the standard color. The results are shown in Table 8. Table 8 C0D Concentration (ppm)~~----- After initial concentration of 10 minutes, after 15 minutes, after 30 minutes, after 60 minutes, after 120 minutes, Example 13 —--- 40 30 " 30 28 16 — Example 14 20 '— 20 13 "Ϊ3-10 Comparative Example 3 20 — 20 20 20 20 Comparative Example 5 40 35~ 30 30 T8 ~ —

[結果] 如表8所示,使用實施例13,14之不織布的情況,相 較於比較例3,5,COD濃度之減少速度快,展現良好之水 質淨化性能。特別是,於測定開始丨2〇分鐘後,實施例i 4 之COD濃度會成為比較例3之c〇D濃度的一半,水質淨 化性能獲得提升。此被認為乃由於實施例14之不織布中 之活性碳粒子(有機物吸附性粒子)藉由纖維表面所固定之 濕熱凝膠化凝膠化物來附著,於是有機物吸附性粒子係在 露出表面的狀態下附著,相較於比較例,有機物吸附性粒 子之比表面積的減少受到抑制之故。 [活性碳脫落率] 將實施例14以及比較例5之不織布以活性碳量成為 1.2 1 g的方式做裁切。所裁切之樣本的尺寸,實施例14為 42 * 1296296 3 0 cmx 2 Ocm,比較例5為6.6cm x l〇cm。其次,於3升之燒 瓶中加入2升的水’將實施例13以及比較例5之前述樣 本分別放入燒瓶内之水中,以磁攪拌子攪拌4小時。之後, 取出樣本,將燒瓶内之殘存液以質量事先測定過之玻璃濾 紙(東洋濾紙公司製造,商品名「阿德幫提克」,型錄「GLASs FIBER GS25」,直徑47mm)來抽氣過濾,將過濾後之玻璃 濾紙加以乾燥,然後測定乾燥後之玻璃濾紙之質量。然後, 從所得之玻璃濾紙之質量來算出活性碳之脫落量以及脫落 率。又,活性奴之脫落量係乾燥後之玻璃濾紙之質量減掉 過濾刚之玻璃濾紙之質量所得之值。又,活性碳之脫落率, 係活性碳之脫落量除以試驗前之活性碳量(121g)再乘以 1 〇〇之值。結果顯示於表9。 表9 活性碳量(g) 脫落量(g) 脫落率(g) 實施例14 1.21 0.0016 0.13 比較例5 1.21 0.0201 ----— 1.66 [結果] 如表9所顯示般,實施例14之不織布相較於比較例5 之不織布在活性碳之脫落量以及脫落率獲得抑制。此被認 為是由於實施们4之不織布中之活性碳(活性碳粒子)被在 纖維表面所固定之濕熱凝膠化之凝膠化物所 、 1可考’所以相 車乂於比較例5,活性碳能更強固地保持之故。 43 1296296 [實施例15] (不織布原板之製作) 準備鞘成分為乙烯一乙烯醇共聚樹脂(EVOH,乙烯含 有量38莫爾%,熔點176。〇、芯成分為聚丙烯(pp,熔點 161°C )之EVOH : pp為50 ·· 50之比例(體積比)之芯鞘型複 5纖維(纖度·· 2.8dtex,纖維長度:51mm)。 將前述芯鞘型複合纖維以半隨機梳棉機進行開纖,製 作單位面積重量4〇g/m2之梳棉網。其次,將該梳棉網載放 於90網眼之平織支持體上,自在該梳棉網之寬方向配置 列孔口(直徑:〇· 12mm,間距:0.6mm)之噴嘴朝向該梳 棉網以水壓3MPa來喷射水流之後,進一步以水壓4MPa 進行贺射。接著,將該梳棉網反過來,自該喷嘴以水壓4mpa 噴射水流,製作水流交絡不織布原板。 (添加物之準備) 在添加物方面係使用活性碳粒子:「庫拉雷可魯pL-D」(庫拉雷化學公司製造,椰子殼碳,平均粒徑4〇〜5〇μπι)。 (添加物附著濕熱成形加工) 將前述不織布原板浸潰於由水中分散有1〇質量%之前 述活性碳粒子所構成之添加物分散溶液(2(rc)中,以軋輥 機之擠壓壓力來調整挾帶率。 將含有水分與添加物之不織布夾在厚度〇 3mm之不鏽 鋼板製之1對金屬模具之間做密合,放入加工溫度i4(rc 之熱風乾燥機,以10分鐘之接觸壓做熱處理。成形體係 使用碗型之金屬模具來製作成圖8所示之用以覆蓋人的口 1296296 鼻之罩體40’另使用打摺型之金屬模具來製作成圖9所干 之空氣清靜機用過滤器之打摺加工品。計算所得之罩體以 及打摺加工品之活性碳粒子之附著率,結果均$ _ %。 里 &圖8所示之罩體,具有適度的柔軟性,保持著纖維形 悲’士纖維均勻分散之深抽的碗型成形體。藉由凝膠化物 所固定之活性碳粒子,並不會從成形體脫落。又,即使戴 上罩體,也不會有呼吸困難的感覺。圖9之打摺加工品,[Results] As shown in Table 8, in the case of using the non-woven fabrics of Examples 13, 14, compared with Comparative Examples 3 and 5, the COD concentration was decreased rapidly, and good water purification performance was exhibited. In particular, after 2 minutes from the start of the measurement, the COD concentration of Example i 4 became half of the concentration of c〇D of Comparative Example 3, and the water purification performance was improved. This is considered to be because the activated carbon particles (organic adsorbent particles) in the non-woven fabric of Example 14 are adhered by the moist heat gelation gelled by the surface of the fiber, and the organic adsorbent particles are exposed to the surface. The adhesion was suppressed, and the decrease in the specific surface area of the organic adsorbent particles was suppressed as compared with the comparative example. [Activated carbon shedding rate] The non-woven fabrics of Example 14 and Comparative Example 5 were cut so that the amount of activated carbon became 1.2 1 g. The size of the cut sample, Example 14 was 42 * 1296296 3 0 cm x 2 Ocm, and Comparative Example 5 was 6.6 cm x l〇cm. Next, 2 liters of water was placed in a 3-liter flask. The above-mentioned samples of Example 13 and Comparative Example 5 were placed in water in a flask, and stirred with a magnetic stirrer for 4 hours. After that, the sample was taken out, and the residual liquid in the flask was filtered by a glass filter paper (manufactured by Toyo Filter Co., Ltd., trade name "Ade Bang Tike", catalogue "GLASs FIBER GS25", diameter 47 mm). The filtered glass filter paper is dried, and then the quality of the dried glass filter paper is measured. Then, the amount of the activated carbon and the shedding rate were calculated from the mass of the obtained glass filter paper. Further, the amount of active slaves is the mass of the dried glass filter paper minus the value obtained by filtering the quality of the glass filter paper. Further, the shedding rate of activated carbon is the amount of activated carbon which is divided by the amount of activated carbon before the test (121 g) and multiplied by 1 〇〇. The results are shown in Table 9. Table 9 Amount of activated carbon (g) Amount of shedding (g) Shedding rate (g) Example 14 1.21 0.0016 0.13 Comparative Example 5 1.21 0.0201 ----- 1.66 [Results] As shown in Table 9, the nonwoven fabric of Example 14 Compared with the non-woven fabric of Comparative Example 5, the amount of seizure of activated carbon and the shedding rate were suppressed. This is considered to be due to the fact that the activated carbon (activated carbon particles) in the nonwoven fabric of the manufacturer 4 is fixed by the wet heat gelation of the surface of the fiber, and the test can be carried out in Comparative Example 5, and the activity is Carbon can remain stronger for the sake of it. 43 1296296 [Example 15] (Preparation of non-woven original board) The sheath component was prepared as an ethylene-vinyl alcohol copolymer resin (EVOH, ethylene content: 38 mol%, melting point 176. 〇, core component was polypropylene (pp, melting point 161°) C) EVOH: core-sheath type complex 5 fiber (denier ··2.8 dtex, fiber length: 51 mm) with a ratio of pp of 50 ·· 50 (the fiber length: 51 mm). The core-sheath type composite fiber is a semi-random carding machine The fiber was opened to produce a card net having a basis weight of 4 〇g/m 2 . Secondly, the card web was placed on a 90-mesh plain woven support, and the column apertures were arranged in the width direction of the card ( The nozzle having a diameter of 〇·12 mm and a pitch of 0.6 mm is sprayed toward the card web at a water pressure of 3 MPa, and further subjected to a water jet of 4 MPa. Then, the card web is reversed, from the nozzle Water pressure 4mpa spray water flow to make water flow entangled non-woven original board. (Preparation of additives) Activated carbon particles are used for additives: "Kura Rekoru pL-D" (Curaray Chemical Co., Ltd., coconut shell carbon, The average particle size is 4〇~5〇μπι). Hot forming process) The raw material of the nonwoven fabric is impregnated into an additive dispersion solution (2 (rc) composed of 1% by mass of the activated carbon particles dispersed in water, and the pinch rate is adjusted by the pressing pressure of the roll machine A non-woven fabric containing moisture and additives was placed between a pair of metal molds made of a stainless steel plate having a thickness of 3 mm, and placed in a hot air dryer at a processing temperature of i4 (rc), and heat-treated at a contact pressure of 10 minutes. The forming system uses a bowl-shaped metal mold to form a mouth for covering a person as shown in Fig. 8 1296296. The nose cover 40' is also made of a metal mold of a discount type to be used as an air cleaner for drying in Fig. 9. The discounted product of the filter, the calculated adhesion rate of the obtained cover body and the activated carbon particles of the folded processed product, the result is both _%. The cover shown in Fig. 8 has moderate flexibility and remains. The deep-drawn bowl-shaped formed body in which the fiber-shaped sorrow fibers are uniformly dispersed. The activated carbon particles fixed by the gelled material do not fall off from the molded body. Moreover, even if the cover is worn, there is no breathing. Difficult feeling. Figure 9 Discounted products,

保持著纖維狀態,纖維呈均勻分散,為打摺之山谷(折曲面) 明顯之深抽的成形體。藉由凝膠化物所固定之活性碳粒 子並不會從成形體脫落。圖9之打摺加工品,由於確實 地摺豐著,所,以對於打摺型卡匣式過濾器之加工性也良 好0 本發明能提供一種可保持原本纖維之性質、且能有效 發揮添加物所具有之功能的添加物附著纖維、纖維構造物 以及纖維成形體、以及其等之製造方法。 本發明中,由於添加物在纖維表面係以凝膠化物來附 著’所以添加物不易脫落,可於露出在纖維表面之狀態下 附著。例如’將本發明之纖維構造物使用於氣體吸附材的 【月况’氣體吸附性粒子利用纖維表面之凝膠化物來附著, 所以氣體吸附性粒子可在露出於表面之狀態下附著。藉 此’可防止於纖維表面所附著之氣體吸附性粒子之脫落, 且可抑制氣體吸附性粒子之比表面積的減少,故相較於以 往之氣體吸附材,可提升氣體吸附性能。又,將本發明之 45 I296296 纖維構造物使用於水質淨化材的情況,由於有機物吸附性 粒子以纖維表面之凝膠化物來附著,所以有機物吸附性粒 子可在露出於表面之狀態下附著。藉此,可防止於纖維表 面所附著之有機物吸附性粒子之脫落,且可抑制有機物吸 附性粒子之比表面積的減少,故相較於以往之水質淨化 材’可提升淨化性能。 ±本發明之纖維成形體,黏結劑樹脂係含有濕熱凝膠化 樹脂,纖維構造物之纖維係以濕熱凝膠化樹脂經濕熱凝膠 化^疑膝化物所固定,成形為既定之形狀,藉此,於衣料 用途的情況,即使直接或間接接觸到人的肌膚也呈現柔軟 2感覺、又,成形均勾,可得到深抽之形狀。再者,添加 物可有效地附著於纖維表面。 维二本發明之纖維成形體之製造方法,係形成含有纖 V.一輸樹脂之纖維集合體,進行濕熱成形加工, 二用T均勾地成形,即使是深抽之形狀也容易成形。於 叙用逆可降低成形成本。 產^_上可刺用作 «研著纖維以及纖維構造物可適用於用 之(麵T.e.f1。♦做為q用研磨材 ;透鏡、半導體、金屬、塑膠、 的研磨好、%〜产 見坡項等各種領域 以吸或業務用廚房等所使用之研磨材、用 交換材、… 材、抗菌材、除臭材、離子 物、〃 7处理用材、吸油材、金屬吸附材、電池八p 物用不織材、導電性材、制電 寸材電池^ 电Γ (抗靜電)材、調濕、除濕(防 46 1296296 止結露)材、吸音一隔音材、防蟲一防黴材、抗病毒材等。 例如,氣體吸附材、抗病毒材可使用於建材之養生片、壁 紙、罩體、空調用等之過濾器。 本發明之纖維成形體於衣料用途的情況,可用於例如 肩墊、乳房墊、外套之衣領襯布、袖襯布、口袋襯布、前 身大片、後身大片、鑲邊、褲子的腰襯布等。又非衣料用 途的情況,可成形為:罩體、空氣清靜機或真空室所使用 之過濾器濾材的打摺加工品、空調用空氣導管之隔熱材、 參 配管、管子、平板、經壓延機加工之表面具有凹凸花紋之 片材等。 【圖式簡單說明】 圖1A〜1C係本發明之一實施形態之添加物附著纖維之 截面圖。 圖 圖2係本發明之一實施形態之3層構造 之不織布截面 圖3係本發明之製造方法之一例製程圖。 圖4A係以本發明之實施例1所得之不織布的掃描電 子顯微鏡平面照片(倍率1 00)。 圖4B係同截面照片(倍率100)。 圖4C係同不織布表面之纖維表面放大照片(倍 1000) ° 圖扣係同其他部分不織布的掃描電子顯 片(倍率100)。 _ 圖4E係同戴面照片(倍率1〇〇)。 47 1296296 圖4F係、同不織布表面之纖維表面放大照片(倍率 1000) 圖 5 A係以本2各日月> u t \ r 貫施例6所得之不織布的掃描電 子顯微鏡平面照片(倍率J 〇〇)。 圖5B係同載面照片(倍率100)。 圖5C係、同不織布表面之纖維表面放大照片(倍率 1000) 〇 圖6係水循環式簡易試驗機之示意立體圖。Maintaining the fiber state, the fibers are uniformly dispersed, which is a deep drawn body of the discounted valley (folded surface). The activated carbon particles fixed by the gel do not fall off from the molded body. The discounted product of Fig. 9 is also excellent in workability for a discount type cassette filter. The present invention can provide a property capable of maintaining the original fiber and can be effectively added. Additives having a function as a substance adhere to a fiber, a fiber structure, a fiber molded body, and a method of producing the same. In the present invention, since the additive is attached to the surface of the fiber by gelation, the additive is less likely to fall off and can be attached to the surface of the fiber. For example, the fiber structure of the present invention is used for the gas adsorbing material. The gas adsorbing particles are adhered by the gel on the surface of the fiber. Therefore, the gas adsorbing particles can be attached to the surface while being exposed. By this, the gas adsorbing particles adhering to the surface of the fiber can be prevented from falling off, and the specific surface area of the gas adsorbing particles can be suppressed from being reduced, so that the gas adsorbing performance can be improved compared with the conventional gas adsorbing material. Further, when the 45 I296296 fiber structure of the present invention is used for a water purification material, since the organic substance-adsorbing particles adhere to the gel on the surface of the fiber, the organic-adsorbing particles can adhere to the surface while being exposed. Thereby, it is possible to prevent the organic substance-adsorbing particles adhering to the surface of the fiber from falling off, and it is possible to suppress the decrease in the specific surface area of the organic-adsorbing particles, so that the purification performance can be improved compared with the conventional water-purifying material. In the fiber molded body of the present invention, the binder resin contains a moist heat gelling resin, and the fiber of the fiber structure is fixed by a wet heat gelation resin by wet heat gelation, and formed into a predetermined shape. Therefore, in the case of the use of the clothing, even if it is directly or indirectly contacted with human skin, it exhibits a soft feeling, and the shape is hooked, and the shape of deep drawing can be obtained. Furthermore, the additive can be effectively attached to the surface of the fiber. In the method for producing a fiber molded body according to the present invention, a fiber assembly containing a fiber V. a resin is formed, and a wet heat forming process is carried out, and the T is formed by a double T, and the shape is easily formed even in a deep drawn shape. The use of reverse can reduce the cost of forming. Produced on the ^_ can be used as « grinding fiber and fiber structure can be applied to use (face Tef1. ♦ as q with abrasive; lens, semiconductor, metal, plastic, grinding, %~ see Abrasive materials, exchange materials, materials, antibacterial materials, deodorizing materials, ionic materials, 〃7 processing materials, oil absorbing materials, metal adsorption materials, batteries, etc. used in suction and business kitchens, etc. Non-woven materials, conductive materials, electric battery materials, electric Γ (anti-static) materials, humidity control, dehumidification (anti-46 1296296 anti-condensation), sound-absorbing and sound-absorbing materials, insect-proof, anti-mold materials, anti- For example, a gas adsorbing material or an antiviral material can be used for a filter for a health-care sheet of a building material, a wallpaper, a cover, an air conditioner, etc. The fiber molded body of the present invention can be used for, for example, a shoulder pad in the case of a clothing use. , breast pad, jacket collar lining, sleeve lining, pocket lining, front body large, back body large, hem, waist lining of pants, etc.. Filter filter used in vacuum chamber The material of the material, the heat insulating material of the air duct for air conditioning, the pipe, the tube, the flat plate, the sheet having the uneven pattern on the surface processed by the calender, etc. [Fig. 1A to 1C] Fig. 2 is a cross-sectional view of a three-layer structure according to an embodiment of the present invention. Fig. 3 is a process diagram of a manufacturing method of the present invention. Fig. 4A is a view of the present invention. A scanning electron microscope photograph (magnification of 100) of the non-woven fabric obtained in Example 1. Fig. 4B is a photograph of the same cross section (magnification of 100). Fig. 4C is an enlarged photograph of the surface of the fiber with the surface of the non-woven fabric (1000 times). Partially non-woven scanning electronic display (magnification of 100). _ Figure 4E is a photo of the same face (magnification 1〇〇). 47 1296296 Figure 4F, enlarged surface of the fiber surface of the same non-woven surface (magnification 1000) Figure 5 A Fig. 5B is a photograph of the same scanning surface (magnification: 100). Fig. 5B is the same as the surface of the non-woven fabric. Dimensional surface of an enlarged photograph (magnification 1000) of FIG. 6 billion water circulation system of FIG simplified schematic perspective view of the test machine.

圖7係本發明之一實施形態之對於不織布賦予水分之 一例製程圖。 圖8係本發明之一實施形態之纖維成形體(罩體)之立 體圖。 圖9係本發明之一實施形態之纖維成形體(空氣清靜機 過濾器之打摺加工品)之立體圖。 圖10係本發明之製造方法其他實施例之製程圖。 圖11A係以本發明之實施例7所得之不織布的掃描電 子顯微鏡平面照片(倍率2〇〇)。 圖11B係同不織布表面之纖維表面放大照 2〇〇〇) 〇 “、、乃率 【主要元件符號說明】 1 鞘成分(黏結劑樹脂) ^ 芯成分 3 添加物 4 黏結劑樹脂 48 ^ 1296296Fig. 7 is a view showing an example of a process for imparting moisture to a nonwoven fabric according to an embodiment of the present invention. Fig. 8 is a perspective view showing a fiber molded body (cover) according to an embodiment of the present invention. Fig. 9 is a perspective view showing a fiber molded body (a bent product of an air cleaner filter) according to an embodiment of the present invention. Figure 10 is a process diagram of another embodiment of the manufacturing method of the present invention. Fig. 11A is a plan photograph (magnification 2 〇〇) of a scanning electron microscope of the nonwoven fabric obtained in Example 7 of the present invention. Fig. 11B is an enlarged view of the surface of the fiber with the surface of the non-woven fabric. 2〇〇〇) 、 ",, and rate" [Main component symbol description] 1 sheath component (adhesive resin) ^ core component 3 additive 4 binder resin 48 ^ 1296296

5,6,9 7 8 11 12 20 21 22a,22b 23 23a 24 24a,24b 25 26 27 28 31 32 33 34 35 36 37 38 複合纖維 乙烯一乙烯醇共聚樹脂(黏結劑樹脂) 聚丙烯 添加物附著纖維層 人造絲纖維層 水循環式簡易試驗機 台座 固定夾具 容器 開口 豕 管 小片 茶包 試驗用樣本 金屬線 纖維或不織布 槽 添加物分散溶液 擠壓輥 蒸氣機 吸氣機 加熱輥 圖案化用帆布輸送帶輥 49 12962965,6,9 7 8 11 12 20 21 22a,22b 23 23a 24 24a,24b 25 26 27 28 31 32 33 34 35 36 37 38 Composite fiber ethylene-vinyl alcohol copolymer resin (adhesive resin) Polypropylene additive adhesion Fiber layer rayon fiber layer water circulation type simple test machine pedestal fixing jig container opening tube small piece tea bag test sample metal wire fiber or non-woven groove additive dispersion solution squeeze roller steam machine aspirator heating roller patterning canvas conveyor belt Roller 49 1296296

39 捲繞機 40 罩體 41 乾燥機 50 空氣清靜機過濾器之打摺加工品 5039 Winder 40 Cover 41 Dryer 50 Discounted products for air cleaner filter 50

Claims (1)

1296296 十、申請專利範圍: 於該纖維表面之 之添加物;其特 h一種添加物附著纖維,含有纖維、 黏結劑树脂、以另 M及於该黏結劑樹脂所附著 徵在於: 該黏結 凝膠化樹脂 刮枒知為在水分存在下經加熱會凝膠化之濕熱 之凝膠化 °亥添加物係藉由該濕熱凝膠化樹脂經凝膠化 物來附著。 ' _ 2·如申請專利範圍第1項之添加物附著纖維,其中, 該濕熱凝膠化樹脂係乙烯—乙烯醇共聚樹脂。 3·如申請專利範圍帛1項之添加物附著纖維,其中, 該添加物之平均粒徑為〇 〇1〜1〇〇μηι之範圍。 4· -種纖維構造物,係含有添加物附著纖維,該添加 物附著纖維含有纖維、於該纖維表面之黏結劑樹脂、以及 於該黏結劑樹脂所附著之添加物;其特徵在於: 孩黏結劑樹脂為在水分存在下經加熱會凝膠化之濕熱 φ 凝膠化樹脂, … 該添加物係藉由該濕熱凝膠化樹脂經凝膠化之凝膠化 物來附著。 5·如申請專利範圍第4項之纖維構造物,其中,該濕 • 熱凝膠化樹脂係乙烯一乙烯醇共聚樹脂。 ^ 6·如申請專利範圍第4項之纖維構造物,其中,該纖 維以及該黏結劑樹脂係擇自 (I )含有濕熱旋膠化樹脂成分與其他熱塑性合成纖維 51 1296296 成分之複合纖維; (π )該複合纖維與其他纖維所混合而成者; (瓜)該複合纖維與濕熱凝膠化樹脂所混合而成者丨以 及 (IV)濕熱减膠化樹脂與其他纖維所混合而成者·, 中至少一種的組合。1296296 X. Patent application scope: an additive on the surface of the fiber; an additive fiber attached to the fiber, containing a fiber, a binder resin, and another M and a binder resin attached thereto: the cemented gel The resin scraping is known to be a gelation of moist heat which is gelled by heating in the presence of moisture, and the gelled product is adhered by the wet heat gelling resin. The additive-attached fiber according to the first aspect of the invention, wherein the wet heat gelling resin is an ethylene-vinyl alcohol copolymer resin. 3. The additive-attached fiber according to claim 1, wherein the additive has an average particle diameter in the range of 〇 〇 1 to 1 〇〇 μηι. 4· - a fibrous structure comprising an additive-attached fiber, the additive-attached fiber comprising a fiber, a binder resin on the surface of the fiber, and an additive attached to the binder resin; characterized in that: The agent resin is a moist heat φ gelling resin which gels upon heating in the presence of moisture, and the additive is adhered by gelation of the wet heat gelling resin. 5. The fibrous structure according to item 4 of the patent application, wherein the wet thermal gelling resin is an ethylene-vinyl alcohol copolymer resin. [6] The fiber structure of claim 4, wherein the fiber and the binder resin are selected from the group consisting of: (I) a composite fiber comprising a component of a wet heat-gelatinized resin component and another thermoplastic synthetic fiber 51 1296296; π) the composite fiber is mixed with other fibers; (the melon) is a mixture of the composite fiber and the moist heat gelling resin, and (IV) the wet heat gelatinization resin is mixed with other fibers. , a combination of at least one of them. 7·如申請專利範圍帛4 ,貝之纖維構造物,其中,該添 加物之平均粒徑為〇.〇1〜ΙΟΟμηι之範圍。 ^ 8·如申請專㈣㈣4項之纖維構造物,其巾,該添 加物為無機粒子。 9·如申請專利範圍第8 $之纖維構 機粒子係擇自氧化铭、)氧化石夕、:聚…:中。玄無 一來峨酸納(tripoly)、 鑽石、剛玉、剛砂、石權石、打火石、 Σ山儿、 σ成鑽石、氮化硼、 反化矽、碳化硼、氧化鉻、氧化鈽、 .^^ 乳化鐵、矽酸膠體、 厌、石墨、沸石、二氧化鈦、高嶺土、 少-種之粒子。 黏土以及料中至 ,其中,該添 ’其中,該添 10·如申請專利範圍第9項之纖維構造物 加物係研磨劑,該纖維構造物係研磨不織布 U·如申請專利範圍第4項之纖維構造物 加物含有多孔質粒子。 11項之纖維構造物,其中,該 12項之纖維構造物,其中,該 12·如申請專利範圍第 多孔質粒子係&性碳粒子 u_如申請專利範圍第 纖維構造物係氣體吸附材 52 1296296 14.如申睛專利範圍第12項之纖維構造物,其 纖維構造物係水質淨化材。 15·如申請專利範圍帛4項之纖維構造物,其 加物附著纖維伟;^ + ϋ主I J、、 、、隹係存在於兩表面,内部係存在著親水性纖 維0 16·如申請專利範圍第15項之纖維構造物,其中,該 親生、戴、准係擇自人造絲纖維、棉纖維以及紙激中至少一 種之纖維。 17·如申請專利範圍帛4項之纖維構造物,其中,該纖 維構造物係在厚度方向被壓縮成形而附著著。 18·一種纖維成形體,係纖維構造物所成形而得者,該 纖維構k物係含有纖維、於該纖維表面之黏結劑樹脂、以 及於該黏結劑樹脂所附著之添加物附著纖維;其特徵在 於: 垓黏結劑樹脂含有在水分存在下經加熱會凝膠化之渴 熱凝膠化樹脂, 該纖維構造物中,該纖維係藉由該濕熱凝膠化樹脂經 4勝化之凝膠化物來固定並成形為既定之形狀。 19·如申請專利範圍第18項之纖維成形體,其中,該 纖維成形體係以接觸壓成形加工所成形者。 20·種添加物附著纖維之製造方法,係用以製造含有 、截、准於汶纖維表面之黏結劑樹脂、以及於該黏結劑樹脂 所附著之添加物的添加物附著纖維;纟肖徵在於: 名、截、准以及该黏結劑樹脂係在水分存在下經加熱而凝 53 1296296 膠化之濕熱凝膠化纖維, 將溶液中分散有該添加物之添加物分散溶液賦予於該 濕熱凝膠化纖維, 其次,在濕熱環境氣氛下對該濕熱凝膠化纖維進行濕 熱處理,使得該濕熱凝膠化纖維凝膠化,以凝膠化物將該 添加物附著於纖維表面。 士申明專利範圍弟20項之添加物附著纖維之製造 方法,其中,該濕熱凝膠化纖維係濕熱凝膠化樹脂單獨或 • 是含有濕熱凝膠化樹脂成分與其他熱塑性合成纖維成分之 複合纖維。 22·如申印專利範圍第2〇項之添加物附著纖維之製造 方法,其中,該濕熱環境氣氛係該濕熱凝膠化樹脂之凝膠 化溫度〜熔點_2(Tc之溫度範圍。 23.—種添加物附著纖維之製造方法,係用以製造含有 ’截、准於4纖維表面之黏結劑樹脂、於該黏結劑樹脂所附 著之添加物的添加物附著纖維;其特徵在於: 鲁 該纖維與該黏結劑樹脂係其他纖維與濕熱凝膠化樹 脂, 對該其他纖維賦予該濕熱凝膠化樹脂之後再賦予添加 物’或是將溶液中分散有該添加物以及該濕熱凝膠化樹脂 • 之添加物分散溶液賦予於該其他纖維, • 其次’在濕熱環境氣氛下進行濕熱處理將該濕熱凝膠 化樹脂凝膠化,以凝膠化物將該添加物附著於其他纖維表 面0 54 1296296 24·—種纖維構造物之製 物附著纖維之纖維構造物, 於该纖維表面之黏結劑樹脂 之添加物;其特徵在於: 造方法,係用以製造含有添加 該添加物附著纖維含有纖維、 、以及於該黏結劑樹脂所附著 該黏結劑樹脂為在水分存在 凝膠化樹脂, 下經加熱會凝膠化之濕 敎 該纖維以及該黏結劑樹脂係擇自 (I)含有濕熱凝膠化樹脂纖維成分與其他熱塑性合成 纖維成分之複合纖維; (π)該複合纖維與其他纖維所混合而成者; (π)該複合纖維與濕熱凝膠化樹脂所混合而成者; (IV)濕熱凝膠化樹脂與其他纖維所混合而成者; 中至少一種的組合, 以該纖維以及該黏結劑樹脂來製作纖維構造物, 將/谷液中分散有該添加物之添加物分散溶液賦予於該 纖維構造物, 其次’在濕熱環境氣氛下對該濕熱凝膠化樹脂進行濕 熱處理’使得該濕熱凝膠化樹脂凝膠化,以凝膠化物將該 添加物附著於纖維表面來形成添加物附著纖維。 25·如申請專利範圍第24項之纖維構造物之製造方 法,其中,該濕熱環境氣氛係該濕熱凝膠化樹脂之凝膠化 溫度〜熔點-20°C之溫度範圍。 26.如申請專利範圍第24項之纖維構造物之製造方 法,其中,該濕熱處理係在厚度方向壓縮成形之處理。 55 1296296 27. 如申請專利範圍第24項之纖維構造物之製造方 法,其甲,該濕熱處理係以蒸氣所進行之處理。 28. 如申請專利範圍第24項之纖維構造物之製造方 法,其中,該添加物分散溶液係水溶液或是含有濕熱凝膠 化樹脂之水溶液。 2 9 · —種纖維成形體之製;生古、、土 &田 人/版又表w方法,係用以製造由纖維構 造物所成形而得之纖維成形體,該纖維構造物含有纖維、 於該纖維表面之黏結劑樹脂、於該黏結劑樹脂所附著之添 ® 加物附著纖維;其特徵在於, 該黏結劑樹脂係含有藉由在水分存在下加熱而凝膠化 之濕熱凝膠化樹脂, • 形成含有該纖維與黏結劑樹脂之纖維構造物, “ 使得該纖維構造物在金屬模具内、濕熱環境氣氛下將 該濕熱凝膠化樹脂濕熱凝膠化做濕熱成形加工。 30.如申請專利範圍第29項之纖維成形體之製造方 法’其中’該濕熱成形加工係將含有水分與添加物之纖維 籲構造物插入一對之金屬模具内,進行加熱加壓處理之加 工。 31·如申請專利範圍第29項之纖維成形體之製造方 法’其中’該濕熱成形加工係以纖維構造物與金屬模具之 接觸壓力來進行加工之接觸壓成形加工。 Η^一、圖式: 如次頁。 567. For example, in the patent application scope 帛4, the fiber structure of the shell, wherein the average particle diameter of the additive is in the range of 〇.〇1~ΙΟΟμηι. ^ 8· If you apply for a fiber structure of 4 (4) and (4), the towel is an inorganic particle. 9. If the patent application range is 8th, the particle size of the fiber structure is selected from the oxidation of the crystal, and the oxidized stone eve,: poly...: medium. Nothing comes to tripoly, diamond, corundum, emerald, stone stone, flintstone, Σ山儿, σ into diamond, boron nitride, anti-cyanide, boron carbide, chromium oxide, antimony oxide, .^^ Emulsified iron, citric acid colloid, anaerobic, graphite, zeolite, titanium dioxide, kaolin, less-species particles. In the case of the clay and the material, wherein the addition is the fiber structure additive abrasive according to claim 9 of the patent application, the fiber structure is a non-woven fabric U. The fibrous structure additive contains porous particles. Item 11 of the fibrous structure, wherein the fibrous structure of the 12th item, wherein the 12th patent, the porous particle sub-system & carbon particle u_, as claimed in the patent scope, the fibrous structure is a gas adsorbing material 52 1296296 14. The fibrous structure of claim 12, wherein the fibrous structure is a water purification material. 15·If the fiber structure of the patent application scope 帛4 item, the additive is attached to the fiber; ^ + ϋ main IJ, , , , 隹 are present on both surfaces, and there are hydrophilic fibers in the interior. The fiber structure of item 15, wherein the living, wearing, and quasi-series are selected from at least one of rayon fibers, cotton fibers, and paper fibers. 17. The fiber structure according to claim 4, wherein the fiber structure is compression-molded and adhered in the thickness direction. 18. A fiber molded body obtained by molding a fiber structure containing fibers, a binder resin on a surface of the fiber, and an additive-attached fiber adhered to the binder resin; The ruthenium binder resin contains a thirst thermal gelation resin which is gelled by heating in the presence of moisture, and the fiber structure is a gel which is subjected to 4 wins by the wet heat gelation resin. The compound is fixed and shaped into a predetermined shape. The fiber formed body of claim 18, wherein the fiber forming system is formed by contact press forming. 20. A method for producing an additive-attached fiber, which is used for producing an additive-attached fiber containing a binder resin which is included in the surface of the fiber, and an additive attached to the binder resin; : The name, the cut, the quasi-and the adhesive resin is a moist heat-gelled gel which is gelled by heating in the presence of moisture, and the additive dispersion solution in which the additive is dispersed in the solution is imparted to the wet heat gel. The wet fiber is subjected to a wet heat treatment in a humid heat atmosphere to gel the wet heat gelled fiber, and the additive is attached to the fiber surface with a gel. The invention relates to a method for producing an additive-attached fiber of 20 parts of the patent scope, wherein the wet heat gelling fiber is a wet heat gelling resin alone or a composite fiber containing a wet heat gelling resin component and other thermoplastic synthetic fiber components. . The method for producing an additive-attached fiber according to the second aspect of the invention, wherein the moist heat atmosphere is a gelation temperature to a melting point of the wet heat gelation resin (Tc temperature range. a method for producing an additive-attached fiber, which is used for producing an additive-attached fiber containing a binder resin which is cut off from the surface of the fiber and adhered to the additive of the binder resin, and is characterized in that: The fiber and the other resin of the binder resin and the damp heat gelling resin, the moist heat gelling resin is applied to the other fiber, and then the additive is added or the additive and the wet heat gelling resin are dispersed in the solution. • The additive dispersion solution is imparted to the other fibers, • Secondly, the wet heat treatment gel is gelled by wet heat treatment in a humidified atmosphere, and the additive is attached to the surface of the other fibers by gelation. 0 54 1296296 a fibrous structure of a fiber-attached structure-attached fiber, an additive of a binder resin on the surface of the fiber; characterized by: And the use of the fiber containing the additive-attached fiber, and the binder resin adhered to the binder resin to wet the gel after heating in a gelled resin The binder resin is selected from the group consisting of (I) a composite fiber containing a wet heat gelled resin fiber component and other thermoplastic synthetic fiber components; (π) a composite fiber of the composite fiber and other fibers; (π) the composite fiber and a mixture of a moist heat gelling resin; (IV) a mixture of a moist heat gelling resin and another fiber; a combination of at least one of the fibers, and a fiber structure made of the fiber and the binder resin, An additive dispersion solution in which the additive is dispersed in the valley liquid is applied to the fiber structure, and then the wet heat gelation resin is subjected to a wet heat treatment in a humid heat atmosphere atmosphere to gel the wet heat gelation resin. The gelled material adheres the surface of the fiber to the surface of the fiber to form an additive-attached fiber. 25) A method for producing a fiber structure according to claim 24 The wet heat environment atmosphere is a gelation temperature of the wet heat gelation resin to a temperature range of -20 ° C. 26. The method for producing a fiber structure according to claim 24, wherein the moist heat The treatment is a process of compression molding in the thickness direction. 55 1296296 27. The method for producing a fibrous structure according to claim 24, wherein the wet heat treatment is carried out by steam. A method for producing a fiber structure according to the item 24, wherein the additive dispersion solution is an aqueous solution or an aqueous solution containing a moist heat gelling resin. 2 9 · a fiber-formed body; a raw material, a soil, an earth man And a method for producing a fiber formed body formed of a fiber structure containing fibers, a binder resin on the surface of the fiber, and a layer attached to the binder resin. Additive-attached fiber; characterized in that the binder resin contains a moist heat gelling resin which is gelated by heating in the presence of moisture, • forming a fiber containing Coalescent resin fiber structure, "so that the fiber structure within the mold, the hot and humid atmosphere to heat wet heat gelling resin gel overtaken by heat molding. 30. The method for producing a fibrous formed body according to claim 29, wherein the wet heat forming process inserts a fibrous structure containing moisture and an additive into a pair of metal molds, and performs heat and pressure treatment. . 31. A method of producing a fibrous formed body according to claim 29, wherein the wet thermoforming process is a contact press forming process in which the fiber structure is subjected to a contact pressure with a metal mold. Η^一,图: As the next page. 56
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US9062398B2 (en) 2011-01-04 2015-06-23 Young Green Energy Co. Non-woven fabric, method for fabricating non-woven fabric, and gas generation apparatus
US9109807B2 (en) 2011-12-21 2015-08-18 Industrial Technology Research Institute Device for desorption and dehumidification and system using the same

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TWI744108B (en) * 2020-11-24 2021-10-21 勤倫有限公司 Silk made by cutting film material and refined to improve physical properties and its production method

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Publication number Priority date Publication date Assignee Title
US9062398B2 (en) 2011-01-04 2015-06-23 Young Green Energy Co. Non-woven fabric, method for fabricating non-woven fabric, and gas generation apparatus
US9109807B2 (en) 2011-12-21 2015-08-18 Industrial Technology Research Institute Device for desorption and dehumidification and system using the same

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