TW201643289A - Single-layer or multilayer nonwoven fabric of long polyester fibers, and filter comprising same for food - Google Patents

Single-layer or multilayer nonwoven fabric of long polyester fibers, and filter comprising same for food Download PDF

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TW201643289A
TW201643289A TW105110377A TW105110377A TW201643289A TW 201643289 A TW201643289 A TW 201643289A TW 105110377 A TW105110377 A TW 105110377A TW 105110377 A TW105110377 A TW 105110377A TW 201643289 A TW201643289 A TW 201643289A
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layer
polyester long
fiber
nonwoven fabric
woven fabric
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TW105110377A
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Chinese (zh)
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TWI624571B (en
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Yusuke Yamada
Rumina Obi
Kazufumi Kato
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Asahi Chemical Ind
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    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/005Synthetic yarns or filaments
    • D04H3/009Condensation or reaction polymers
    • D04H3/011Polyesters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • B01D39/16Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/14Other self-supporting filtering material ; Other filtering material
    • B01D39/16Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
    • B01D39/1607Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous
    • B01D39/1623Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin
    • B01D39/163Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin sintered or bonded
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D77/00Packages formed by enclosing articles or materials in preformed containers, e.g. boxes, cartons, sacks or bags
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/08Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating
    • D04H3/14Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with bonds between thermoplastic yarns or filaments produced by welding
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2239/00Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/04Additives and treatments of the filtering material
    • B01D2239/0407Additives and treatments of the filtering material comprising particulate additives, e.g. adsorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2239/00Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/06Filter cloth, e.g. knitted, woven non-woven; self-supported material
    • B01D2239/065More than one layer present in the filtering material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2239/00Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/12Special parameters characterising the filtering material
    • B01D2239/1241Particle diameter
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W90/00Enabling technologies or technologies with a potential or indirect contribution to greenhouse gas [GHG] emissions mitigation
    • Y02W90/10Bio-packaging, e.g. packing containers made from renewable resources or bio-plastics

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Nonwoven Fabrics (AREA)
  • Filtering Materials (AREA)
  • Packages (AREA)
  • Tea And Coffee (AREA)

Abstract

Provided are: single-layer or multilayer nonwoven fabric of long polyester fibers which is excellent in terms of transparency, dimensional stability, powder leakage property, and component extraction property; and a filter for foods which comprises the nonwoven fabric. The single-layer or multilayer nonwoven fabric of long polyester fibers according to the present invention has a content of inorganic particles of 0-100 ppm and a 10%-cumulation pore diameter less than 1,000 [mu]m, the difference between the 10%-cumulation pore diameter and the 2.3%-cumulation pore diameter being 500 or less, and has a basis weight of 10-30 g/m2.

Description

單層或複層聚酯長纖維不織布及使用其之食品用過濾器 Single or multi-layer polyester long-fiber non-woven fabric and food filter using the same

本發明係關於一種透明性、尺寸穩定性、粉體滲漏性、及成分提取性優異之單層或複層聚酯長纖維不織布、以及使用其之面向飲料之提取用之食品用過濾器。 The present invention relates to a single-layer or multi-layer polyester long-fiber non-woven fabric excellent in transparency, dimensional stability, powder leakage property, and component extractability, and a food filter for extracting beverages using the same.

先前,使用包含聚乙烯、聚丙烯、聚酯、聚醯胺等樹脂之不織布作為包裝材料。然而,通常為了充分利用不織布之過濾性等遮蔽功能而要求將纖維製成緻密,從而無法對內部進行確認。又,於進行紅茶、綠茶、烏龍茶等之成分提取之情形時,較多地利用茶葉袋方式作為簡便之方法。茶葉袋用途所使用之包裝材料通常較多地使用紙,但存在透明性變差而無法看見包裝材料內之東西、無法進行熱密封加工等問題點。 Previously, a non-woven fabric containing a resin such as polyethylene, polypropylene, polyester, polyamide or the like was used as a packaging material. However, in order to make full use of the shielding function such as the filterability of the non-woven fabric, it is required to make the fibers dense, and it is impossible to confirm the inside. Further, in the case of extracting components such as black tea, green tea, and oolong tea, the tea bag method is often used as a simple method. The packaging materials used for tea bag applications usually use paper in a large amount, but there is a problem that the transparency is deteriorated and the contents of the packaging material cannot be seen, and heat sealing processing cannot be performed.

於以下之專利文獻1中揭示有透明性經改良後之茶葉袋用不織布,但並無與尺寸穩定性相關之記載,而並非特別注意。進而,使用利用泡點法(JIS-K-3832)所測定之最大孔徑作為對粉體洩漏之評價,但適合測定之孔徑範圍為奈米至微米級別,且係對壓力進行換算後體現孔徑,故而並非為適合實際所使用之茶葉之評價方法。 Patent Document 1 below discloses a non-woven fabric for tea bags having improved transparency, but there is no description relating to dimensional stability, and no particular attention has been paid. Further, the maximum pore diameter measured by the bubble point method (JIS-K-3832) is used as an evaluation of powder leakage, but the pore diameter range suitable for measurement is in the range of nanometers to micrometers, and the pore diameter is expressed by converting the pressure. Therefore, it is not suitable for the evaluation method of the tea used in practice.

又,於以下之專利文獻2中揭示有包含聚L乳酸之纖度為15~35dtex之茶葉袋用生物降解性單絲,因纖度較大而透明性較高,但存在單絲之沸水收縮率為20%以下而尺寸穩定性較低之問題點。 Further, Patent Document 2 below discloses a biodegradable monofilament for tea bags containing a polylactic acid having a fineness of 15 to 35 dtex, which has high transparency and high transparency, but has a boiling water shrinkage ratio of monofilament. Less than 20% and the problem of low dimensional stability.

進而,於以下之專利文獻3中揭示有包含將聚烯烴系聚合物作為 鞘成分且將熔點高於上述鞘成分之聚酯系聚合物作為芯成分之芯鞘型之複合長纖維之熱密封性優異之不織布,但尺寸穩定性較低,又,並無與透明性相關之記載,而並非特別注意。 Further, Patent Document 3 below discloses that a polyolefin-based polymer is included as a non-woven fabric excellent in heat sealability of a core-sheath type composite long fiber having a sheath component and a polyester-based polymer having a melting point higher than the sheath component, but having low dimensional stability and not related to transparency It is recorded without special attention.

[先前技術文獻] [Previous Technical Literature] [專利文獻] [Patent Literature]

[專利文獻1]日本專利第3939326號公報 [Patent Document 1] Japanese Patent No. 3939326

[專利文獻2]日本專利特開2001-131826號公報 [Patent Document 2] Japanese Patent Laid-Open Publication No. 2001-131826

[專利文獻3]日本專利特開平11-43855號公報 [Patent Document 3] Japanese Patent Laid-Open No. Hei 11-43855

本發明鑒於上述先前技術之問題,提供一種透明性、尺寸穩定性、粉體滲漏性、及成分提取性優異之聚酯長纖維不織布、以及使用其之食品用過濾器。 The present invention has been made in view of the above problems of the prior art, and provides a polyester long-fiber nonwoven fabric excellent in transparency, dimensional stability, powder leakage property, and component extractability, and a food filter using the same.

本發明者等人為了解決上述問題而進行了努力研究並反覆進行實驗,結果發現,選定具有特定範圍之鈦元素含量之聚酯系樹脂,並就構成不織布之纖維之結構與纖維直徑、單位面積重量、熱壓接面積率之觀點進行詳細之研究,獲得紡絲性良好且作為食品用過濾器而成分提取性優異且透明性與尺寸穩定性之兩者良好之不織布。進而將使用藉由對不織布直接進行觀察而算出之孔徑定義成粉體滲漏性之評價,藉此完成了本發明。 The inventors of the present invention have diligently studied and repeated experiments in order to solve the above problems, and as a result, have found that a polyester resin having a specific content of a titanium element is selected, and the structure, fiber diameter, and unit area of the fiber constituting the nonwoven fabric are selected. In view of the weight and the hot-pressed area ratio, a non-woven fabric which is excellent in spinnability and which is excellent in component extractability as a food filter and which is excellent in both transparency and dimensional stability is obtained. Further, the evaluation of the pore diameter calculated by directly observing the nonwoven fabric was defined as the powder leakage property, and the present invention was completed.

即,本發明如以下所述。 That is, the present invention is as follows.

[1]一種單層或複層聚酯長纖維不織布,其中無機系粒子之含量為0~100ppm,10%點孔徑未達1000μm,10%點孔徑與2.3%點孔徑之差為500以下,且單位面積重量為10~30g/m2[1] A single-layer or multi-layer polyester long-fiber non-woven fabric, wherein the content of inorganic particles is 0 to 100 ppm, the pore diameter of 10% is less than 1000 μm, and the difference between the pore diameter of 10% and the pore diameter of 2.3% is 500 or less, and The weight per unit area is 10~30g/m 2 .

[2]如上述[1]之單層或複層聚酯長纖維不織布,其熱壓接面積率 為5~40%,且平均視密度為0.1~0.5g/cm3[2] The single-layer or multi-layer polyester long-fiber non-woven fabric according to the above [1], which has a thermocompression bonding area ratio of 5 to 40% and an average apparent density of 0.1 to 0.5 g/cm 3 .

[3]如上述[1]或[2]之單層或複層聚酯長纖維不織布,其平均纖維直徑為13~40μm。 [3] The single-layer or multi-layer polyester long-fiber nonwoven fabric of the above [1] or [2], which has an average fiber diameter of 13 to 40 μm.

[4]如上述[1]~[3]中任一項之單層或複層聚酯長纖維不織布,其中至少1層包含於拉曼光譜中所觀測到之1740cm-1附近之由C=O基所產生之波峰寬度之半峰全幅值之平均值為18~24cm-1之纖維。 [4] The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of the above [1] to [3], wherein at least one layer is contained in the vicinity of 1740 cm -1 observed in the Raman spectrum by C = The average value of the full width at half maximum of the peak width generated by the O group is 18 to 24 cm -1 .

[5]如上述[1]~[4]中任一項之單層或複層聚酯長纖維不織布,其中至少1層包含結晶度為30~50%之纖維。 [5] The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of [1] to [4] above, wherein at least one layer contains fibers having a crystallinity of 30 to 50%.

[6]如上述[1]~[5]中任一項之單層或複層聚酯長纖維不織布,其中至少1層包含雙折射率0.04~0.12之纖維。 [6] The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of the above [1] to [5], wherein at least one layer contains fibers having a birefringence of 0.04 to 0.12.

[7]如上述[1]~[6]中任一項之單層或複層聚酯長纖維不織布,其透明性為60%以上。 [7] The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of the above [1] to [6], which has a transparency of 60% or more.

[8]如上述[1]~[7]中任一項之單層或複層聚酯長纖維不織布,其沸水收縮率為2.0%以下。 [8] The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of the above [1] to [7], which has a boiling water shrinkage ratio of 2.0% or less.

[9]如上述[1]~[8]中任一項之單層或複層聚酯長纖維不織布,其質地係數為0.5~2.0。 [9] The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of the above [1] to [8], which has a texture coefficient of 0.5 to 2.0.

[10]如上述[1]~[9]中任一項之單層或複層聚酯長纖維不織布,其中至少1層之拉伸強度為5N/30mm以上。 [10] The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of [1] to [9] above, wherein at least one of the layers has a tensile strength of 5 N/30 mm or more.

[11]如上述[1]~[10]中任一項之單層或複層聚酯長纖維不織布,其中至少1層含有熔點240℃以下之低熔點纖維。 [11] The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of [1] to [10] above, wherein at least one layer contains a low melting point fiber having a melting point of 240 ° C or less.

[12]如上述[1]~[11]中任一項之聚酯長纖維不織布,其包含藉由熱壓接使下述a層與b層一體化之積層不織布。 [12] The polyester long-fiber nonwoven fabric according to any one of [1] to [11] above which comprises a laminated non-woven fabric in which the following a layer and b layer are integrated by thermocompression bonding.

a層:包含與高熔點樹脂之熔點差為30℃~150℃之低熔點樹脂之聚酯長纖維不織布 a layer: polyester long fiber non-woven fabric containing a low melting point resin having a melting point difference of 30 ° C to 150 ° C with a high melting point resin

b層:包含上述高熔點樹脂之聚酯長纖維不織布 Layer b: polyester long-fiber non-woven fabric containing the above high melting point resin

[13]如上述[1]~[12]中任一項之單層或複層聚酯長纖維不織布, 其具有上述聚酯長纖維不織布之纖維之配向性於剖面方向上不同之結構。 [13] The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of the above [1] to [12], The fiber having the above-mentioned polyester long fiber nonwoven fabric has a structure in which the orientation is different in the cross-sectional direction.

[14]如上述[1]~[13]中任一項之單層或複層聚酯長纖維不織布,其中至少1層含有包含0~25%之間苯二甲酸之樹脂。 [14] The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of [1] to [13] above, wherein at least one layer contains a resin containing 0 to 25% of phthalic acid.

[15]如上述[1]~[14]中任一項之單層或複層聚酯長纖維不織布,其中上述無機系粒子為氧化鈦。 [15] The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of [1] to [14] wherein the inorganic particles are titanium oxide.

[16]如上述[15]之單層或複層聚酯長纖維不織布,其包含鈦元素含量0~0.1ppm之樹脂。 [16] The single-layer or multi-layer polyester long-fiber nonwoven fabric according to [15] above, which comprises a resin having a titanium element content of 0 to 0.1 ppm.

[17]如上述[1]~[16]中任一項之單層或複層聚酯長纖維不織布,其中製成不織布後之樹脂之IV值為0.6以上。 [17] The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of [1] to [16] above, wherein the resin having a non-woven fabric has an IV value of 0.6 or more.

[18]一種食品用過濾器,其包含如上述[1]~[17]中任一項之單層或複層聚酯長纖維不織布。 [18] A filter for a food comprising the single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of [1] to [17] above.

構成本發明之單層或複層聚酯長纖維不織布之纖維之紡絲性良好,使用包含該纖維之不織布而製造之食品用過濾器之成分提取性優異,透明性、尺寸穩定性、進而耐粉體滲漏性亦良好。 The fiber constituting the single-layer or multi-layer polyester long-fiber nonwoven fabric of the present invention is excellent in spinnability, and the food filter produced by using the nonwoven fabric containing the fiber is excellent in component extractability, transparency, dimensional stability, and further resistance. Powder leakage is also good.

圖1係表示如板狀之分散板等控制氣流之裝置之一例之概略圖。 Fig. 1 is a schematic view showing an example of a device for controlling a gas flow such as a plate-shaped dispersion plate.

圖2係表示沸水收縮率與透明性之關係之圖表。 Fig. 2 is a graph showing the relationship between boiling water shrinkage ratio and transparency.

圖3係表示拉伸比與配向結晶性之關係之圖表。 Fig. 3 is a graph showing the relationship between the draw ratio and the alignment crystallinity.

圖4係表示紡絲溫度與配向結晶性之關係之圖表。 Fig. 4 is a graph showing the relationship between the spinning temperature and the alignment crystallinity.

圖5係表示樹脂IV值與配向結晶性之關係之圖表。 Fig. 5 is a graph showing the relationship between the resin IV value and the alignment crystallinity.

以下,對本發明之實施形態詳細地進行說明。 Hereinafter, embodiments of the present invention will be described in detail.

作為構成構成本實施形態之聚酯長纖維不織布之聚酯長纖維之聚酯系樹脂,可列舉作為熱塑性聚酯之聚對苯二甲酸乙二酯、聚對苯 二甲酸丁二酯或聚對苯二甲酸丙二酯作為代表例,亦可為作為形成酯之酸成分之間苯二甲酸或鄰苯二甲酸等經聚合或共聚而成之聚酯。熱塑性聚酯進而亦可為具有生物降解性之樹脂,例如聚二醇酸或聚乳酸般之聚(α-羥酸)、或將該等作為主要之重複單元要素之共聚物。該等樹脂可單獨使用,或亦可將2種以上進行組合。 Examples of the polyester-based resin constituting the polyester long fibers constituting the polyester long-fiber nonwoven fabric of the present embodiment include polyethylene terephthalate and polyparaphenylene as thermoplastic polyesters. As a representative example, butylene dicarboxylate or polytrimethylene terephthalate may be a polyester obtained by polymerizing or copolymerizing phthalic acid or phthalic acid as an acid component forming an ester. The thermoplastic polyester may further be a biodegradable resin such as a polyglycolic acid or a polylactic acid-like poly(α-hydroxy acid), or a copolymer of these as a main repeating unit element. These resins may be used singly or in combination of two or more.

本實施形態之聚酯長纖維不織布係透明性越高(隱蔽性較低)越佳,因此熱塑性合成纖維不織布中通常用作消光劑之無機系粒子之含有率越低越佳。 The polyester long-fiber nonwoven fabric of the present embodiment has a higher transparency (lower concealability), and therefore, the content of the inorganic-based particles which are generally used as a matting agent in the thermoplastic synthetic fiber nonwoven fabric is preferably as low as possible.

作為用作消光劑之無機粒子,可並無特別限定地使用合成品及天然產物之任一者。作為無機粒子,例如可列舉:氧化鋁、氧化矽、氧化鈦、氧化鋯、氧化鎂、氧化鈰、氧化釔、氧化鋅及氧化鐵等氧化物系陶瓷;氮化矽、氮化鈦及氮化硼等氮化物系陶瓷;碳化矽、碳酸鈣、硫酸鋁、氫氧化鋁、氫氧化鎂、鈦酸鉀、滑石、高嶺黏土、高嶺石、狄克石、透輝橄無球粒隕石、多水高嶺土、葉蠟石、拉輝煌斑岩、蒙脫石、鋁膨潤石、綠脫石、鉻嶺石、皂石、鋅膨潤石、鋰蒙脫石、蛭石、鐵鋁蛇紋石、絹雲母、鎂綠泥石、錳鋁蛇紋石、鋅鋁蛇紋石、鎳鋁蛇紋石、膨潤土、沸石、黑雲母、金雲母、鐵雲母、富鎂黑雲母、針葉雲母鐵雲母、鱗雲母、富矽鱗雲母、白雲母、綠鱗石富鎂黑雲母、鐵綠鱗石、鐵鋁綠鱗石、矽酸鈣、矽酸鎂、矽藻土及矽砂等陶瓷及玻璃纖維。該等無機粒子係單獨使用1種,或將2種以上組合後使用。就對樹脂之反應活性之觀點而言,所使用之無機粒子較佳為氧化鈦、硬脂酸鎂、硬脂酸鈣等惰性無機粒子。 As the inorganic particles used as the matting agent, any of a synthetic product and a natural product can be used without particular limitation. Examples of the inorganic particles include oxide ceramics such as alumina, cerium oxide, titanium oxide, zirconium oxide, magnesium oxide, cerium oxide, cerium oxide, zinc oxide, and iron oxide; tantalum nitride, titanium nitride, and nitriding; Nitride ceramics such as boron; tantalum carbide, calcium carbonate, aluminum sulfate, aluminum hydroxide, magnesium hydroxide, potassium titanate, talc, kaolin clay, kaolinite, dickite, diaphoric olivine-free vermiculite, multi-water Kaolin, pyrophyllite, glazed porphyry, montmorillonite, aluminum bentonite, nontronite, chrome ore, saponite, zinc bentonite, hectorite, vermiculite, iron-aluminum serpentine, sericite, Magnesia chlorite, manganese-aluminum serpentine, zinc-aluminum serpentine, nickel-aluminum serpentine, bentonite, zeolite, biotite, phlogopite, iron mica, magnesium-rich biotite, conifer mica, mica, scale mica, rich scale Mica, muscovite, chlorite rich magnesium biotite, iron green scale stone, iron aluminum green scale stone, calcium citrate, magnesium silicate, diatomaceous earth and strontium sand ceramics and glass fiber. These inorganic particles are used singly or in combination of two or more. From the viewpoint of the reactivity of the resin, the inorganic particles to be used are preferably inert inorganic particles such as titanium oxide, magnesium stearate or calcium stearate.

構成本實施形態之聚酯長纖維之聚酯系樹脂之無機系粒子之較佳之粒徑之範圍為1.0μm以下,較佳為0.8μm以下,更佳為0.7μm以下。若粒徑超過1.0μm,則作為不織布,不僅透明性降低,紡絲之穩定性亦變差,故而斷頭等紡絲缺點亦增加。 The preferred particle diameter of the inorganic particles constituting the polyester-based resin of the polyester long fiber of the present embodiment is 1.0 μm or less, preferably 0.8 μm or less, and more preferably 0.7 μm or less. When the particle diameter exceeds 1.0 μm, as a non-woven fabric, not only the transparency is lowered, but also the stability of spinning is deteriorated, so that the disadvantage of spinning such as breakage is also increased.

於構成本實施形態之聚酯長纖維之聚酯系樹脂中,無機系粒子之較佳之含量為0~100ppm,較佳為0~50ppm,更佳為0~0.1ppm。藉由將纖維中之無機粒子之含量設為上述範圍內,可充分地確保不織布之透明性。進而,於將無機系粒子用作觸媒之情形時,藉由設為上述範圍內,熔融擠出時之樹脂之分解反應被抑制,從而可抑制斷頭等紡絲缺點。 In the polyester resin constituting the polyester long fiber of the present embodiment, the content of the inorganic particles is preferably from 0 to 100 ppm, preferably from 0 to 50 ppm, more preferably from 0 to 0.1 ppm. By setting the content of the inorganic particles in the fibers within the above range, the transparency of the nonwoven fabric can be sufficiently ensured. In the case where the inorganic particles are used as the catalyst, the decomposition reaction of the resin during melt extrusion is suppressed, and the disadvantage of spinning such as breakage can be suppressed.

作為於構成本實施形態之聚酯長纖維之聚酯系樹脂中用作消光劑之無機系粒子,就廉價且為通用之方面而言,較佳為使用使反應活性失活後之氧化鈦等鈦系粒子。於在構成本實施形態之聚酯長纖維之聚酯系樹脂中使用鈦元素作為無機系粒子之情形時,較佳之含量為0~100ppm,較佳為0~50ppm,更佳為0~0.1ppm。 The inorganic particles used as the matting agent in the polyester-based resin constituting the polyester long fiber of the present embodiment are preferably inexpensive and generally used, and titanium oxide or the like which deactivates the reaction activity is preferably used. Titanium particles. In the case where a titanium element is used as the inorganic particles in the polyester resin constituting the polyester long fiber of the present embodiment, the content is preferably 0 to 100 ppm, preferably 0 to 50 ppm, more preferably 0 to 0.1 ppm. .

具體而言,較佳為未添加用作消光劑之二氧化鈦等無機系惰性粒子之無色透明之超亮樹脂,進而較佳為未使用鈦化合物作為觸媒之樹脂。藉由不使用鈦化合物作為觸媒,熔融擠出時之樹脂之分解反應被抑制,從而可抑制斷頭等紡絲缺點。 Specifically, it is preferably a colorless and transparent super bright resin to which inorganic inert particles such as titanium dioxide used as a matting agent are not added, and further preferably a resin which does not use a titanium compound as a catalyst. By not using a titanium compound as a catalyst, the decomposition reaction of the resin at the time of melt extrusion is suppressed, and the disadvantage of spinning such as breakage can be suppressed.

將本實施形態之聚酯長纖維不織布作為包裝材時之內包物之滲漏性可藉由孔徑之分佈而定義。 The leakage property of the inner bag when the polyester long fiber nonwoven fabric of the present embodiment is used as a packaging material can be defined by the distribution of the pore diameter.

孔徑之代表值能以對於不織布圖像中之各孔之面積,自最大面積向較小之面積依序累計時之面積率10%點處之孔徑而體現,必須為1000μm以下。較佳之範圍為30μm以上且6000μm以下,更佳之範圍為400μm以下,進而較佳之範圍為300μm以下,最佳為250μm以下。若為該範圍以上,則布帛之縫變稀,故而無法抑止內包物之粉體滲漏。另一方面,若為該範圍以下,則布帛之縫變細,故而過濾器之透明性降低。又,過濾器之抑止流體阻力上升,故而用作食品用過濾器時,提取時間增加而不實用。 The representative value of the aperture can be expressed as an aperture of 10% of the area ratio when the area of each hole in the non-woven image is sequentially accumulated from the largest area to the smaller area, and must be 1000 μm or less. A preferred range is 30 μm or more and 6000 μm or less, more preferably 400 μm or less, further preferably 300 μm or less, and most preferably 250 μm or less. If it is more than this range, the seam of the fabric becomes thin, and the powder leakage of the inner bag cannot be suppressed. On the other hand, if it is below this range, the seam of the fabric becomes fine, and the transparency of the filter is lowered. Further, since the filter suppresses the increase in the fluid resistance, when the filter is used as a food filter, the extraction time is increased and it is not practical.

將直徑較大之孔徑分佈自最大孔徑累計時之2.3%與10%點之差必 須為0μm以上且500μm以下。較佳之範圍為300μm以下,更佳之範圍為200μm以下,進而較佳之範圍為150μm以下。於如不織布之孔徑分佈較大之布帛之情形時,藉由將直徑較大之孔之頻率設為該範圍內,可製成粉體滲漏性優異之不織布。進而,藉由與上述10%孔徑之範圍合併,可對用於包裝茶葉而最佳之孔徑分佈進行定義。 The difference between the larger diameter pore size distribution from the maximum pore size of 2.3% and 10% points must It must be 0 μm or more and 500 μm or less. A preferred range is 300 μm or less, more preferably 200 μm or less, and still more preferably 150 μm or less. In the case of a fabric having a large pore size distribution of the non-woven fabric, by setting the frequency of the hole having a large diameter to be within this range, a nonwoven fabric excellent in powder leakage property can be obtained. Further, by combining with the above range of 10% pore diameter, the optimum pore size distribution for packaging tea leaves can be defined.

又,於相同孔面積之孔之情形時,關於形狀,相比於真圓,較佳為如橢圓般存在較長之直徑與較短之直徑者。於包裝茶葉等內容物之情形時,因並非為表面光滑之真球,故而即便為相同孔面積,於存在較長之直徑與較短之直徑之孔之情形時,茶葉卡在孔周邊而不易滲漏。對茶葉等之滲漏之影響尤其較大的是該不織布所含之相對較大之孔之形狀。該孔之形狀能以2.3%孔徑至10%孔徑之孔之長徑之平均值除以2.3%孔徑至10%孔徑之孔徑之平均值所得之值表示。該值較佳為1.3以上。通常只要樹脂之透明性相同,則若一面保持透明性一面抑制內容物之滲漏,則會處於折衷之關係,透明性係固定面積內所含之纖維表面積、即纖維直徑越細且單位面積重量越大而越差,內容物之滲漏性減小。根據該關係一面確保透明性一面抑制內容物之滲漏性之一個方法係減少不織布所含之大孔徑,另一個方法係將孔之形狀設為內容物不易滲漏之形狀。藉由同時利用該兩個方法,可獲得進一步滿足透明性與內容物之滲漏性抑制之兩者之不織布。 Further, in the case of a hole having the same hole area, as for the shape, it is preferable to have a longer diameter and a shorter diameter as an ellipse than a true circle. In the case of packaging contents such as tea leaves, since it is not a true ball with a smooth surface, even if it is the same hole area, when there is a hole having a long diameter and a short diameter, the tea leaves are stuck around the hole. leakage. The effect on the leakage of tea leaves and the like is particularly large in the shape of the relatively large pores contained in the nonwoven fabric. The shape of the pores can be expressed as a value obtained by dividing the average of the major diameters of the pores of the pores of 2.3% to 10% by the average of the pore diameters of the pores of 2.3% and 10%. This value is preferably 1.3 or more. Generally, as long as the transparency of the resin is the same, if the transparency of the resin is suppressed while maintaining the transparency, the resin will have a trade-off relationship, and the surface area of the fiber contained in the transparent fixing area, that is, the finer the fiber diameter and the weight per unit area. The larger and worse, the leakage of the contents is reduced. One method of suppressing the leakage of the contents while ensuring transparency in accordance with this relationship is to reduce the large pore diameter of the nonwoven fabric, and the other method is to make the shape of the pores into a shape in which the contents are less likely to leak. By simultaneously using the two methods, a non-woven fabric that further satisfies both the transparency and the leakage inhibition of the contents can be obtained.

本實施形態之聚酯長纖維之形狀除通常之圓形剖面以外,可根據其目的與用途而選擇中空剖面、芯鞘型複合剖面、分割型複合剖面、扁平剖面等任意之纖維剖面形狀。 The shape of the polyester long fiber of the present embodiment may be any fiber cross-sectional shape such as a hollow cross section, a core-sheath type composite cross section, a split type composite cross section, or a flat cross section, in addition to the usual circular cross section.

本實施形態之聚酯長纖維不織布為了製成茶葉袋等袋形狀而使用,較佳為於利用製袋機進行之熱密封加工中接著強度較高。為了獲得接著強度良好之熱密封性,將包含熔點240℃以下之低熔點樹脂之纖維積層於聚酯長纖維不織布之至少一面並設置熔點差,藉此於熱密 封加工時僅低熔點樹脂成分軟化或熔融而作為接著劑發揮功能,從而可有效地獲得較高之熱密封強度。 The polyester long-fiber nonwoven fabric of the present embodiment is used for forming a bag shape such as a tea bag, and is preferably high in strength in heat sealing processing by a bag making machine. In order to obtain a heat sealability with good adhesion strength, a fiber comprising a low melting point resin having a melting point of 240 ° C or less is laminated on at least one side of the polyester long fiber nonwoven fabric, and a difference in melting point is set, thereby being thermally dense. At the time of sealing processing, only the low-melting-point resin component softens or melts and functions as an adhesive, so that high heat-sealing strength can be effectively obtained.

上述低熔點樹脂之熔點較高熔點樹脂之熔點低30~150℃,較佳為低30~100℃。作為低熔點樹脂,例如可列舉:對苯二甲酸、間苯二甲酸、鄰苯二甲酸、萘二羧酸等芳香族二羧酸與乙二醇、二乙二醇、1,4-丁二醇、環己烷二甲醇等二醇聚合而成之共聚聚酯系樹脂或聚乳酸等脂肪族聚酯系樹脂等。進而,作為纖維結構,除單成分以外,較佳為包含鞘芯結構或並列結構等2種成分之複合纖維結構,例如芯為高熔點且鞘為低熔點之複合纖維結構,具體而言,芯為聚對苯二甲酸乙二酯或聚對苯二甲酸丁二酯等高熔點樹脂,鞘為共聚聚酯或脂肪族聚酯等低熔點樹脂。將低熔點纖維積層之方法例如可列舉如下方法,即:使上述樹脂熔解,並將半熔融狀態之樹脂或其纖維狀物塗佈於不織布之簾式噴霧方式,使熔解之樹脂自噴嘴噴出並塗佈於不織布之塗佈方式,或者將高熔點纖維網與低熔點纖維網積層並利用熱輥等進行接合而獲得積層不織布之方法等。 The melting point of the above low melting point resin is higher than the melting point of the melting point resin by 30 to 150 ° C, preferably 30 to 100 ° C lower. Examples of the low melting point resin include aromatic dicarboxylic acids such as terephthalic acid, isophthalic acid, phthalic acid, and naphthalene dicarboxylic acid, and ethylene glycol, diethylene glycol, and 1,4-butane. A copolymerized polyester resin obtained by polymerizing a glycol such as an alcohol or cyclohexane dimethanol or an aliphatic polyester resin such as polylactic acid. Further, the fiber structure is preferably a composite fiber structure including two components such as a sheath core structure or a side-by-side structure, in addition to a single component, for example, a core having a high melting point and a sheath having a low melting point composite fiber structure, specifically, a core It is a high melting point resin such as polyethylene terephthalate or polybutylene terephthalate, and the sheath is a low melting point resin such as a copolymerized polyester or an aliphatic polyester. The method of laminating the low-melting-point fibers may be, for example, a method in which the resin is melted, and a semi-molten resin or a fibrous material thereof is applied to a curtain spray method of a non-woven fabric, and the melted resin is ejected from the nozzle. A method of applying a non-woven fabric, or a method of laminating a high-melting-point fiber web and a low-melting-point fiber web, and joining them by a heat roll or the like to obtain a laminated non-woven fabric.

低熔點樹脂例如於將以對苯二甲酸為主之芳香族二羧酸作為成分時,可使間苯二甲酸、鄰苯二甲酸、萘二羧酸等第2種芳香族二羧酸進行共聚後使用。此時之第二種芳香族二羧酸相對於總芳香族二羧酸之量為0~25%,較佳為0~22%,更佳為0~18%。若添加超過該範圍之量,則結晶性降低,進而不會產生延伸所形成之分子配向,故而紡絲穩定性或製成不織布時之機械強度或尺寸穩定性降低。 For example, when a low-melting-point resin contains a terephthalic acid-based aromatic dicarboxylic acid as a component, a second aromatic dicarboxylic acid such as isophthalic acid, phthalic acid or naphthalene dicarboxylic acid can be copolymerized. After use. The amount of the second aromatic dicarboxylic acid at this time is 0 to 25%, preferably 0 to 22%, more preferably 0 to 18%, based on the total amount of the aromatic dicarboxylic acid. When the amount exceeds this range, the crystallinity is lowered, and the molecular orientation formed by the stretching does not occur, so that the spinning stability or the mechanical strength or dimensional stability when the nonwoven fabric is formed is lowered.

本實施形態之聚酯長纖維不織布較佳為可進行超音波熔斷或熱密封。密封強度較佳為0.1N/30mm以上,更佳為0.2N/30mm以上。熱密封條件可適當選擇,例如熱密封之溫度條件較佳為較密封面之樹脂之熔點低5~80℃。 The polyester long fiber nonwoven fabric of the present embodiment is preferably ultrasonically fusible or heat-sealed. The sealing strength is preferably 0.1 N/30 mm or more, more preferably 0.2 N/30 mm or more. The heat sealing condition can be appropriately selected. For example, the temperature condition of the heat sealing is preferably 5 to 80 ° C lower than the melting point of the resin of the sealing surface.

進而,可於不妨礙所需效果之範圍內添加其他常用之各種添加 成分,例如各種彈性體類等衝擊性改良劑、結晶成核劑、著色防止劑、抗氧化劑、熱穩定劑、塑化劑、潤滑劑、耐候劑、抗菌劑、著色劑、顏料、染料等添加劑。 Furthermore, other common additions can be added without hindering the desired effect. Ingredients such as impact modifiers such as various elastomers, crystal nucleating agents, coloring inhibitors, antioxidants, heat stabilizers, plasticizers, lubricants, weathering agents, antibacterial agents, colorants, pigments, dyes, etc. .

本實施形態之聚酯長纖維不織布可利用紡黏法高效率地製造。即,使上述聚酯系樹脂加熱熔融並自紡絲頭噴出,使用公知之冷卻裝置使所獲得之紡出絲線冷卻,並利用吸氣盤(Air Sucker)等抽吸裝置進行牽引細化。繼而,於使自抽吸裝置排出之絲線群開纖後,堆積於輸送帶上而製成網。繼而,使用經加熱之壓紋輥等局部熱壓接裝置對形成於該輸送帶上之網局部實施熱壓接,藉此獲得長纖維紡黏不織布。 The polyester long fiber nonwoven fabric of the present embodiment can be efficiently produced by a spunbonding method. In other words, the polyester resin is heated and melted and ejected from the spinneret, and the obtained spun yarn is cooled by a known cooling device, and is drawn and refined by a suction device such as an air suction plate (Air Sucker). Then, after the filament group discharged from the suction device is opened, it is deposited on a conveyor belt to form a net. Then, a portion of the web formed on the conveyor belt is thermocompression bonded using a local thermocompression bonding apparatus such as a heated embossing roll, thereby obtaining a long-fiber spunbonded nonwoven fabric.

於使用紡黏法之情形時,並無特別限定,為了提高網之均勻性,例如使用如日本專利特開平11-131355所揭示之利用電暈設備等使纖維帶電之方法,或使用如平板狀之分散板等控制氣流之裝置(參照圖1)調整噴射器之噴出部分之氣流之速度分佈等,使纖維開纖後,吹送網,一面抑制網之飛散,一面積層於捕捉面之方法,藉此成為進而較佳之製法。 In the case of using the spunbonding method, there is no particular limitation, and in order to improve the uniformity of the web, for example, a method of charging a fiber by a corona device or the like as disclosed in Japanese Patent Laid-Open No. Hei 11-131355, or a flat plate is used. The device for controlling the air flow such as the dispersing plate (refer to FIG. 1) adjusts the velocity distribution of the airflow in the ejecting portion of the ejector, and after the fiber is opened, the mesh is blown, and the scattering of the net is suppressed, and the area of the capturing surface is borrowed. This becomes a further preferred method.

利用紡黏法而獲得之不織布具有布強度較強且不存在由接合部之破損所導致之短纖維之脫落等物性上之特徵,又,低成本且生產性較高,故而用於以衛生、土木、建築、農業/園藝、生活材料為中心之廣泛之用途。 The non-woven fabric obtained by the spunbonding method has characteristics of physical properties such as strong cloth strength and absence of breakage of short fibers caused by breakage of the joint portion, and low cost and high productivity, so that it is used for hygiene, A wide range of uses centered on civil engineering, construction, agriculture/horticulture, and living materials.

本實施形態之聚酯長纖維之纖維直徑為13~40μm,較佳為15~40μm,更佳為18~35μm,尤佳之範圍為21~30μm。若纖維直徑為13μm以上,則可設計使透明性充分。又,若為紡絲時纖維無法充分地耐受噴射器之張力而導致纖維之一部分斷裂之虞較少的纖維直徑為40μm以下,則於製成不織布並用作食品用過濾器時,機械強度或剛性、成分提取性、透明性、密封性優異,適合作為食品用過濾器。 The polyester long fibers of the present embodiment have a fiber diameter of 13 to 40 μm, preferably 15 to 40 μm, more preferably 18 to 35 μm, and particularly preferably 21 to 30 μm. When the fiber diameter is 13 μm or more, the transparency can be designed to be sufficient. Further, if the fiber is insufficiently resistant to the tension of the ejector during spinning, and the fiber having a small portion of the fiber is broken, the fiber diameter is 40 μm or less, and when it is made into a non-woven fabric and used as a filter for food, mechanical strength or It is excellent in rigidity, component extraction property, transparency, and sealing property, and is suitable as a food filter.

本實施形態之聚酯長纖維不織布之每單位面積之表面積(即長纖維不織布之比表面積m2/g×單位面積重量g/m2)為1.0~3.5(m2/m2),更佳為1.2~3.0(m2/m2),尤佳之範圍為1.3~2.7(m2/m2)。若每單位面積之表面積為3.5(m2/m2)以下,則可設計使透明性充分。又,若每單位面積之表面積為1.0以上,則於製成不織布時,可獲得充足之纖維條數,故而於用作食品用過濾器時,機械強度或剛性、成分提取性、密封性優異,適合作為食品用過濾器。 The surface area per unit area of the polyester long fiber nonwoven fabric of the present embodiment (that is, the specific surface area m 2 /g × unit area weight g/m 2 of the long fiber nonwoven fabric) is 1.0 to 3.5 (m 2 /m 2 ), more preferably It is 1.2 to 3.0 (m 2 /m 2 ), and particularly preferably in the range of 1.3 to 2.7 (m 2 /m 2 ). When the surface area per unit area is 3.5 (m 2 /m 2 ) or less, the transparency can be designed to be sufficient. In addition, when the surface area per unit area is 1.0 or more, a sufficient number of fibers can be obtained when the nonwoven fabric is formed. Therefore, when used as a food filter, it is excellent in mechanical strength, rigidity, component extraction property, and sealing property. Suitable as a food filter.

關於本實施形態之聚酯長纖維不織布之層構成,只要為經熱/化學一體化而成為不織布之方法,則並無特別限定,可為積層不織布。此時,較佳為設為將各層所承擔之作用區分之層構成。例如,將第1層設為熱密封強度較高之層,將其他層設為拉伸強度、剛性、尺寸穩定性等機械強度優異之層,藉此,可製成製袋時所要求之密封特性優異且機械物性亦優異之不織布。又,於將不織布製成袋狀之步驟中,若使用以僅1層之構成兼具機械強度與密封特性之構成之不織布,則於藉由熱接著加工製造袋狀物之步驟中,於高溫下實施加熱、壓接處理,故而熱塑性樹脂熔融、附著於製袋設備之熱輥或熱板加熱器而導致製品品質降低或加工速度降低,若欲改善此情況,則無法獲得所需之密封強度。與此相對,若為本實施形態之不織布構成,則藉由將密封層配置於內表面,可表現出良好之密封強度,並且可不降低品質、生產速度地進行生產。 The layer structure of the polyester long fiber nonwoven fabric of the present embodiment is not particularly limited as long as it is a nonwoven fabric by thermal/chemical integration, and may be a laminated nonwoven fabric. In this case, it is preferable to form a layer which distinguishes the roles assumed by the respective layers. For example, the first layer is a layer having a high heat-sealing strength, and the other layer is a layer having excellent mechanical strength such as tensile strength, rigidity, dimensional stability, etc., whereby a seal required for bag making can be obtained. Non-woven fabric with excellent properties and excellent mechanical properties. Further, in the step of forming the non-woven fabric into a bag shape, if a non-woven fabric having a structure of only one layer and having both mechanical strength and sealing properties is used, the step of producing the bag by heat subsequent processing is high. The heating and pressure bonding treatment is carried out, so that the thermoplastic resin is melted and adhered to the heat roller or the hot plate heater of the bag making apparatus, resulting in a decrease in the quality of the product or a decrease in the processing speed. If this condition is to be improved, the desired sealing strength cannot be obtained. . On the other hand, in the nonwoven fabric of the present embodiment, by providing the sealing layer on the inner surface, it is possible to exhibit good sealing strength and to produce without lowering the quality and production speed.

於將積層不織布用作本實施形態之聚酯長纖維不織布之情形時,承擔密封性之層之結構可使用紡黏法、熔噴法等之單纖維結構或鞘芯結構或並列結構、分割割纖等包含2種成分之複合纖維結構,較佳為承擔密封性能之低熔點樹脂配置於纖維表面之結構。例如係芯為高熔點且鞘為低熔點之複合纖維結構,具體而言,係由芯為聚對苯二甲酸乙二酯或聚對苯二甲酸丁二酯等高熔點樹脂且鞘為共聚聚酯或脂 肪族聚酯等上述低熔點樹脂所構成之鞘芯結構之不織布。 In the case where a laminated nonwoven fabric is used as the polyester long-fiber nonwoven fabric of the present embodiment, the structure of the layer which is responsible for the sealing property may be a single fiber structure or a sheath core structure or a side-by-side structure or a split-cut structure such as a spunbonding method or a melt-blown method. The fiber or the like has a composite fiber structure of two components, and preferably has a structure in which a low melting point resin which is capable of sealing properties is disposed on the surface of the fiber. For example, the core fiber has a high melting point and the sheath has a low melting point composite fiber structure. Specifically, the core is a high melting point resin such as polyethylene terephthalate or polybutylene terephthalate, and the sheath is copolymerized. Ester or fat A non-woven fabric of a sheath core structure composed of the above-mentioned low-melting resin such as a fatty polyester.

於將積層不織布用作本實施形態之聚酯長纖維不織布之情形時,承擔機械強度之層之製法並無特別限定,就生產性等之觀點而言,較佳為紡黏法。 In the case where the laminated nonwoven fabric is used as the polyester long-fiber nonwoven fabric of the present embodiment, the method for producing the layer of mechanical strength is not particularly limited, and from the viewpoint of productivity and the like, a spunbonding method is preferred.

尤其是於將積層不織布用作本實施形態之聚酯長纖維不織布之情形時,關於承擔機械強度之層之製法、物性,藉由利用上述方法進行生產,可製成尺寸穩定性、機械強度更優異之不織布。 In particular, when a laminated nonwoven fabric is used as the polyester long-fiber nonwoven fabric of the present embodiment, the production method and physical properties of the layer for mechanical strength can be produced by the above method, and dimensional stability and mechanical strength can be obtained. Excellent non-woven fabric.

於將積層不織布用作本實施形態之聚酯長纖維不織布之情形時之壓接方法只要為可使纖維彼此一體化而進行製成不織布者,則並無特別限定,較佳為於使各層積層後利用熱輥等對其等進行熱壓接而進行製成不織布。藉由於使各層積層後進行熱壓接,可使層間之接著強度更牢固,從而可更有效地體現出機械強度或密封性能。 In the case where the laminated nonwoven fabric is used as the polyester long-fiber nonwoven fabric of the present embodiment, the pressure-bonding method is not particularly limited as long as the fibers can be integrated with each other, and it is preferable to laminate the layers. Thereafter, it is subjected to thermocompression bonding using a heat roller or the like to form a nonwoven fabric. By thermocompression bonding after laminating the layers, the strength between the layers can be made stronger, and the mechanical strength or sealing performance can be more effectively exhibited.

藉由將本實施形態中之積層不織布之層構成設為如上述般之積層構成,可將密封強度設為進而較佳之範圍。作為具體之密封強度,為1.5N/30mm以上,較佳為2.0N/30mm以上,更佳為2.5N/30mm以上。 By forming the layer structure of the laminated non-woven fabric in the present embodiment as a laminated structure as described above, the sealing strength can be further improved. The specific sealing strength is 1.5 N/30 mm or more, preferably 2.0 N/30 mm or more, and more preferably 2.5 N/30 mm or more.

又,亦可將機械強度、即拉伸強度設為進而較佳之範圍,其範圍為15N/30mm以上,較佳為20N/30mm以上,更佳為23N/30mm以上。 Further, the mechanical strength, that is, the tensile strength may be further preferably in the range of 15 N/30 mm or more, preferably 20 N/30 mm or more, and more preferably 23 N/30 mm or more.

關於本實施形態之聚酯長纖維不織布之熱壓接,只要為利用熱使不織布之絲與絲進行壓接之方法,則並無特別限定,可藉由使不織布通過包含具有凹凸之表面結構之壓紋輥與平滑輥之一對加熱輥間,而形成均等地分散於整個不織布之熱壓接部而較佳地進行。於利用壓紋輥進行熱壓接之情形時,相對於不織布總面積,較佳為進行5~40%之範圍內之熱壓接面積率下之熱壓接,更佳為7~30%,進而較佳為7~20%。 The thermocompression bonding of the polyester long-fiber nonwoven fabric of the present embodiment is not particularly limited as long as it is a method of pressure-bonding the nonwoven fabric yarn to the yarn by heat, and the nonwoven fabric can be passed through a surface structure including irregularities. It is preferable that one of the embossing roll and the smooth roll is formed between the heating rolls to form a thermocompression-bonding portion which is uniformly dispersed throughout the nonwoven fabric. In the case of thermocompression bonding using an embossing roll, it is preferable to carry out thermocompression bonding at a thermocompression bonding area ratio of 5 to 40% with respect to the total area of the non-woven fabric, and more preferably 7 to 30%. Further preferably, it is 7 to 20%.

若熱壓接面積率為該範圍內,則可進行良好之纖維相互間之熱壓接處理,於實現所獲得之不織布之適度之機械強度或剛性、透明性、成分提取性、尺寸穩定性之方面較佳。熱壓接處理溫度及壓力應根據所供給之網之單位面積重量、速度等條件而適當選擇,並非一概而論,較佳為較聚酯系樹脂之熔點低10~90℃之溫度,更佳為低20~60℃之溫度。 If the thermocompression bonding area ratio is within this range, good thermal compression bonding treatment of the fibers can be performed to achieve moderate mechanical strength or rigidity, transparency, component extractability, dimensional stability of the obtained non-woven fabric. The aspect is better. The temperature and pressure of the thermocompression bonding treatment should be appropriately selected according to the basis weight and speed of the supplied network, and it is not intended to be general. It is preferably a temperature lower than the melting point of the polyester resin by 10 to 90 ° C, more preferably lower. Temperature of 20~60 °C.

於上述熱壓接步驟中,除使用壓紋輥以外,亦可使用藉由使熱風通過網而利用熱對絲與絲進行壓接之風吹法。於利用風吹法進行熱壓接之情形時,由於布帛表面不存在壓紋形狀般之局部凹凸,故而可使不織布之看上去之透明感更高。 In the thermocompression bonding step, in addition to the embossing roll, a wind blowing method in which the hot air is passed through the net to press the wire with the wire by heat may be used. In the case of thermocompression bonding by the wind blowing method, since the surface of the fabric does not have local irregularities such as embossed shapes, the non-woven fabric can be made more transparent.

本實施形態之聚酯長纖維不織布之沸水收縮率較佳為2.0%以下,更佳為1.6%以下,進而較佳為1.0%,尤佳之範圍為0.5%以下。若沸水收縮率為2.0%以下,則幾乎不存在熱成型加工等中之收縮,而步驟穩定性優異,又,即便於如曝露於接近100℃之高溫環境下之使用形態中,形態保持性亦優異。下限較佳為0%,實際上為0.2%以上。 The boiling water shrinkage ratio of the polyester long-fiber nonwoven fabric of the present embodiment is preferably 2.0% or less, more preferably 1.6% or less, further preferably 1.0%, and particularly preferably 0.5% or less. When the boiling water shrinkage ratio is 2.0% or less, there is almost no shrinkage in the thermoforming process or the like, and the step stability is excellent, and even in the form of use such as exposure to a high temperature environment close to 100 ° C, the form retention property is also Excellent. The lower limit is preferably 0%, and is actually 0.2% or more.

本實施形態之聚酯長纖維不織布之透明性較佳為60%以上,更佳為65%以上,進而較佳為70%以上。若透明性未達60%,則難以透過不織布看見內容物之狀態而變得不鮮明。 The transparency of the polyester long-fiber nonwoven fabric of the present embodiment is preferably 60% or more, more preferably 65% or more, still more preferably 70% or more. If the transparency is less than 60%, it is difficult to see the state of the contents through the nonwoven fabric and it becomes unclear.

本實施形態之聚酯長纖維不織布之單位面積重量為10~30g/m2,較佳為12~25g/m2。若單位面積重量為10g/m2以上,則可保持透明性‧成分提取性,並且亦可充分地確保機械強度。另一方面,若單位面積重量為30g/m2以下,則可獲得透明性‧成分提取性。 The polyester long-fiber nonwoven fabric of the present embodiment has a basis weight of 10 to 30 g/m 2 , preferably 12 to 25 g/m 2 . When the basis weight is 10 g/m 2 or more, the transparency and the component extractability can be maintained, and the mechanical strength can be sufficiently ensured. On the other hand, when the basis weight is 30 g/m 2 or less, transparency and component extractability can be obtained.

本實施形態之聚酯長纖維不織布之厚度較佳為0.02~0.50mm,更佳為0.03~0.30mm。若單位面積重量與厚度為該範圍內,則可獲得用作食品用過濾器時優異之透明性、機械強度、成分提取性。 The thickness of the polyester long fiber nonwoven fabric of the present embodiment is preferably 0.02 to 0.50 mm, more preferably 0.03 to 0.30 mm. When the weight per unit area and the thickness are within this range, transparency, mechanical strength, and component extractability which are excellent when used as a food filter can be obtained.

本實施形態之聚酯長纖維不織布之平均視密度較佳為0.10~0.50g/cm3,更佳為0.12~0.30g/cm3。平均視密度與不織布之剛性、透明性、粉體滲漏性及成分提取性相關,若為上述範圍,則纖維間隙適度,故而適合作為食品用過濾器。若平均視密度為0.10g/cm3以上,則可調整纖維間隙而適度地抑制粉體滲漏量,並且亦可使機械強度充分。另一方面,若平均視密度為0.50g/cm3以下,則不會使纖維間隙過小,從而可適度地保持成分提取性,並可使製品品質充分。 The average apparent density of the polyester long-fiber nonwoven fabric of the present embodiment is preferably from 0.10 to 0.50 g/cm 3 , more preferably from 0.12 to 0.30 g/cm 3 . The average apparent density is related to the rigidity, transparency, powder leakage property, and component extraction property of the nonwoven fabric. When the ratio is within the above range, the fiber gap is moderate, and thus it is suitable as a food filter. When the average apparent density is 0.10 g/cm 3 or more, the fiber gap can be adjusted to appropriately suppress the amount of powder leakage, and the mechanical strength can be made sufficient. On the other hand, when the average apparent density is 0.50 g/cm 3 or less, the fiber gap is not excessively small, and the component extractability can be appropriately maintained, and the product quality can be made sufficient.

本實施形態之聚酯長纖維不織布之MD(Machine Direction,縱向)方向之拉伸強度較佳為5~40N/30mm,更佳為6~40N/30mm,進而較佳為7~40N/30mm。若拉伸強度為該範圍以上,則製袋加工時之生產穩定性或用作食品用過濾器時之破損防止等優異。 The tensile strength in the MD (Machine Direction) direction of the polyester long fiber nonwoven fabric of the present embodiment is preferably 5 to 40 N/30 mm, more preferably 6 to 40 N/30 mm, still more preferably 7 to 40 N/30 mm. When the tensile strength is at least the above range, it is excellent in production stability at the time of bag making processing, damage prevention when used as a filter for foods, and the like.

本實施形態之聚酯長纖維不織布之質地係數較佳為0.5~2.0,更佳為0.5~1.5。質地係數表示不織布之均勻性,故而與強度、剛性、透明性、粉體滲漏性及成分提取性相關。若為上述範圍,則不織布之均勻性最佳,故而作為食品用過濾器之強度、剛性、透明性、加工成袋形狀之適應性及粉體滲漏性優異。 The texture coefficient of the polyester long fiber nonwoven fabric of the present embodiment is preferably from 0.5 to 2.0, more preferably from 0.5 to 1.5. The texture coefficient indicates the uniformity of the non-woven fabric, and thus is related to strength, rigidity, transparency, powder leakage, and component extractability. When it is in the above range, the uniformity of the non-woven fabric is optimal, and therefore it is excellent in the strength, rigidity, transparency, suitability for processing into a bag shape, and powder leakage property as a food filter.

獲得本實施形態之聚酯長纖維時之紡絲溫度較佳為較聚酯系樹脂之熔點高10~60℃之溫度,更佳為高10~30℃之溫度。若紡絲溫度為該範圍,則不會產生單絲斷頭等,且配向結晶性適度,從而可獲得機械強度或尺寸穩定性優異之不織布。 The spinning temperature at which the polyester long fibers of the present embodiment are obtained is preferably a temperature higher by 10 to 60 ° C than the melting point of the polyester resin, more preferably 10 to 30 ° C higher. When the spinning temperature is in this range, the monofilament breakage or the like does not occur, and the alignment crystallinity is moderate, and a nonwoven fabric excellent in mechanical strength or dimensional stability can be obtained.

本實施形態之聚酯長纖維不織布製成不織布後之樹脂之固有黏度(IV值)較佳為0.6以上,更佳為0.65以上,進而較佳為0.7以上。於將樹脂顆粒物熔融擠出時,會因熔融時之熱負載或混練時之剪切負載等而導致樹脂分解。若熔融後、即製成不織布後之樹脂之IV值為該範圍以上之情形,則可較佳地抑制樹脂之分解而促進紡絲時之樹脂之延伸、結晶化,故而可製成機械強度、尺寸穩定性優異之不織布。 The inherent viscosity (IV value) of the resin after the polyester long-fiber nonwoven fabric of the present embodiment is made into a non-woven fabric is preferably 0.6 or more, more preferably 0.65 or more, still more preferably 0.7 or more. When the resin pellets are melt-extruded, the resin is decomposed due to heat load during melting or shear load during kneading. When the IV value of the resin after the non-woven fabric is melted, the IV value of the resin is more than or equal to the above range, the decomposition of the resin can be preferably suppressed, and the elongation and crystallization of the resin during spinning can be promoted, so that mechanical strength can be obtained. Non-woven fabric with excellent dimensional stability.

獲得本實施形態之聚酯長纖維時之紡絲速度較佳為3000~6000m/min,更佳為3500~5000m/min。若對紡出絲線進行牽引細化時之牽引速度為上述範圍內,則聚酯長纖維之配向結晶化充分而可獲得機械特性或尺寸穩定性優異之不織布,且於紡絲中產生斷頭之可能性較少,就不織布之生產性之方面而言亦較佳。 The spinning speed at which the polyester long fibers of the present embodiment are obtained is preferably from 3,000 to 6,000 m/min, more preferably from 3,500 to 5,000 m/min. When the pulling speed in the drawing refining of the spun yarn is within the above range, the alignment crystallization of the polyester long fibers is sufficient, and a non-woven fabric excellent in mechanical properties or dimensional stability can be obtained, and breakage occurs in the spinning. There are fewer possibilities and it is better in terms of the productivity of non-woven fabrics.

獲得本實施形態之聚酯長纖維時之拉伸比較佳為400~2500,更佳為700~2200。若對紡出絲線進行牽引細化時之拉伸比為上述範圍內,則聚酯長纖維之配向結晶化充分而可獲得機械特性或尺寸穩定性優異之不織布,且於紡絲中產生斷頭或熱壓接時之「纏繞於輥」之可能性較低,故而就不織布之生產性之方面而言亦較佳。 The stretching of the polyester long fiber of the present embodiment is preferably from 400 to 2,500, more preferably from 700 to 2,200. When the draw ratio in the case of drawing and refining the spun yarn is within the above range, the alignment crystallization of the polyester long fibers is sufficient, and a non-woven fabric excellent in mechanical properties or dimensional stability can be obtained, and breakage occurs in the spinning. Or the possibility of "winding on the roll" at the time of thermocompression bonding is low, and therefore it is also preferable in terms of the productivity of the non-woven fabric.

本實施形態之聚酯長纖維之雙折射率△n為0.04~0.12,較佳為0.06~0.1。若雙折射率為該範圍,則纖維之配向性適度,從而可獲得機械強度或尺寸穩定性優異之不織布。 The birefringence Δn of the polyester long fibers of the present embodiment is from 0.04 to 0.12, preferably from 0.06 to 0.1. When the birefringence is in this range, the orientation of the fibers is moderate, and a nonwoven fabric excellent in mechanical strength or dimensional stability can be obtained.

對結晶性進行評價之方法並無特別限定,例如可利用基於DSC(Differential scanning calorimetry,示差掃描熱量測定)之結晶度測定或拉曼分光測定法等進行測定。 The method for evaluating the crystallinity is not particularly limited, and for example, it can be measured by a crystallinity measurement by DSC (Differential Scanning Calorimetry) or a Raman spectrometry.

本實施形態之聚酯長纖維之結晶度為30~50%,較佳為40~50%。若結晶度為該範圍內,則可獲得機械強度或尺寸穩定性優異之纖維。 The polyester long fiber of the present embodiment has a crystallinity of 30 to 50%, preferably 40 to 50%. When the degree of crystallinity is within this range, fibers excellent in mechanical strength or dimensional stability can be obtained.

於利用拉曼分光法實施本實施形態之聚酯長纖維之結晶性之情形時,可利用纖維剖面之於拉曼光譜中所觀測到之1740cm-1附近之由C=O基所產生之波峰寬度之半峰全幅值之平均值進行評價。波峰寬度之半峰全幅值之平均值為18~24cm-1,較佳為19~24cm-1,更佳之範圍為20~23cm-1。若波峰寬度之半峰全幅值之平均值為該範圍,則可獲得機械強度或尺寸穩定性優異之纖維。 When the crystallinity of the polyester long fiber of the present embodiment is carried out by Raman spectroscopy, the peak of the C=O group in the vicinity of 1740 cm -1 observed in the Raman spectrum of the fiber profile can be utilized. The average of the full amplitude of the half-width of the width was evaluated. The average value of the full width at half maximum of the peak width is 18 to 24 cm -1 , preferably 19 to 24 cm -1 , and more preferably 20 to 23 cm -1 . If the average value of the full width at half maximum of the peak width is within this range, fibers excellent in mechanical strength or dimensional stability can be obtained.

本實施形態之聚酯長纖維可使纖維之半徑方向上不同之結晶 性、例如外周部之結晶性較高,使內部之結晶性較低。藉由使外周部之結晶性較高,可製成不易收縮且機械強度優異之纖維,且藉由使內部之結晶性較低,於熱壓接時可充分地獲得纖維彼此之壓接強度,其結果為,可製成機械強度或尺寸穩定性優異之不織布。該情況可藉由於利用DSC測定結晶度時對熔解峰值進行評價而確認。 The polyester long fiber of the present embodiment can crystallize differently in the radial direction of the fiber. For example, the crystallinity of the outer peripheral portion is high, and the internal crystallinity is low. By making the crystallinity of the outer peripheral portion high, it is possible to produce a fiber which is less likely to shrink and has excellent mechanical strength, and by making the internal crystallinity low, the crimp strength of the fibers can be sufficiently obtained at the time of thermocompression bonding. As a result, it is possible to produce a non-woven fabric excellent in mechanical strength or dimensional stability. This case can be confirmed by evaluating the melting peak when the crystallinity is measured by DSC.

於圖2中表示本發明之實施例中之聚酯長纖維不織布之沸水收縮率與透明性之關係。若增大纖維直徑,則可使透明性增高,但不易進行配向結晶化,故而沸水收縮率變大而尺寸穩定性降低。 Fig. 2 shows the relationship between the boiling water shrinkage ratio and the transparency of the polyester long-fiber nonwoven fabric in the examples of the present invention. When the fiber diameter is increased, the transparency can be increased, but the alignment crystallization is less likely to occur, so that the boiling water shrinkage ratio is increased and the dimensional stability is lowered.

於圖3與4中分別表示本發明之實施例中之聚酯長纖維不織布之拉伸比及紡絲溫度與由雙折射率(△n)及結晶度所表示之配向結晶性之關係。越是增大拉伸比,纖維之配向結晶性越增加。又,於粗纖維直徑之紡絲條件下,越是使紡絲溫度低溫化,冷卻性越增高,藉此延伸效率上升,從而可進行纖維之配向結晶化。 The relationship between the draw ratio and the spinning temperature of the polyester long-fiber nonwoven fabric in the examples of the present invention and the alignment crystallinity represented by the birefringence (?n) and the crystallinity are shown in Figs. 3 and 4, respectively. The more the draw ratio is increased, the more the alignment crystallinity of the fiber increases. Further, under the spinning conditions of the coarse fiber diameter, the spinning temperature is lowered, and the cooling property is increased, whereby the elongation efficiency is increased, and the alignment crystallization of the fibers can be performed.

於圖5中表示本發明之實施例中之聚酯長纖維不織布之樹脂之固有黏度(IV值)與由雙折射率(△n)及結晶度所表示之配向結晶性之關係。藉由使樹脂之IV值增高,可促進樹脂之配向結晶化,從而可進行纖維之配向結晶化。 Fig. 5 shows the relationship between the intrinsic viscosity (IV value) of the resin of the polyester long-fiber nonwoven fabric in the embodiment of the present invention and the alignment crystallinity expressed by the birefringence (?n) and crystallinity. By increasing the IV value of the resin, the alignment crystallization of the resin can be promoted, and the alignment crystallization of the fibers can be performed.

根據該等資料,並以發揮本發明所需之效果之方式進行了努力研究,結果,本案發明者等人利用紡絲溫度之低溫化與拉伸比擴大而維持粗纖維直徑,並且提高配向結晶性,藉此同時實現提高透明性與沸水收縮率。即,於不織布中透明性之提高與沸水收縮率所表示之尺寸穩定性之提高呈相反之關係,但本發明者等人藉由將纖維之粗纖維直徑化與配向結晶性設為最佳範圍而同時實現提高透明性與尺寸穩定性。 In the light of the above, the inventors of the present invention have used the low temperature of the spinning temperature and the expansion ratio to maintain the coarse fiber diameter and improve the alignment crystallization. Sex, thereby achieving improved transparency and boiling water shrinkage. That is, the improvement of the transparency in the nonwoven fabric is inversely related to the improvement of the dimensional stability represented by the boiling water shrinkage ratio, but the inventors of the present invention have made the fiber coarse fiber diameter and the alignment crystallinity into an optimum range. At the same time, it achieves improved transparency and dimensional stability.

進而,藉由將本發明中所使用之樹脂之固有黏度(IV值)最佳化,亦可達成配向結晶之最佳範圍。用以達成本目的之IV值之範圍為0.7 以上,較佳為0.85以下,進而較佳為0.72~0.8之範圍。若固有黏度處於該範圍,則不會產生單絲斷頭等而可確保穩定之生產性,且於對熔融之樹脂進行牽引細化時獲得較高之配向結晶性,藉此可獲得更高之尺寸穩定性及機械強度。 Further, by optimizing the intrinsic viscosity (IV value) of the resin used in the present invention, the optimum range of the alignment crystallization can be achieved. The range of IV values used to achieve this purpose is 0.7 The above is preferably 0.85 or less, and more preferably in the range of 0.72 to 0.8. When the intrinsic viscosity is in this range, the monofilament breakage or the like is not generated, and stable productivity can be ensured, and higher alignment crystallinity can be obtained when the molten resin is subjected to drawing refinement, whereby a higher degree can be obtained. Dimensional stability and mechanical strength.

本實施形態之聚酯長纖維不織布較佳為親水性優異,使得放入熱水中時不會浮出至表面而是迅速下沉。作為親水劑,較佳為用作食品用之界面活性劑,例如山梨醇酐脂肪酸酯、聚甘油脂肪酸酯、蔗糖脂肪酸酯等水溶液、乙醇溶液、或乙醇與水之混合溶液等。塗佈方法可應用凹版輥方式、接觸輥方式、浸漬方式、噴霧方式等公知之方法。 The polyester long-fiber nonwoven fabric of the present embodiment is preferably excellent in hydrophilicity, so that it does not float to the surface when it is placed in hot water but sinks quickly. The hydrophilic agent is preferably used as a surfactant for foods, for example, an aqueous solution such as sorbitan fatty acid ester, polyglycerin fatty acid ester or sucrose fatty acid ester, an ethanol solution, or a mixed solution of ethanol and water. The coating method can be applied to a known method such as a gravure roll method, a contact roll method, a dipping method, or a spray method.

亦可於不損及本發明所需之效果之範圍內對本實施形態之聚酯長纖維不織布進行常用之後加工,例如賦予除臭劑、抗菌劑等,亦可實施染色、撥水加工、透水加工等。 The polyester long-fiber non-woven fabric of the present embodiment may be subjected to conventional post-processing, such as a deodorant, an antibacterial agent, etc., and may be subjected to dyeing, water-repellent processing, and water-permeable processing, without damaging the effects required by the present invention. Wait.

本實施形態之聚酯長纖維不織布由於透明性優異,故而可鮮明地看見內容物,因此設計性優異,且由於尺寸穩定性優異,故而具有非常適合作為綠茶、紅茶、咖啡等之食品用過濾器之特性。作為食品用過濾器,亦可為平袋,但若為立體形狀,則可更清楚地看見內容物,從而有效地進行提取,因此較佳。作為立體形狀,較佳為四面體形狀、三角錐立體形狀等。 Since the polyester long-fiber nonwoven fabric of the present embodiment is excellent in transparency, the content can be clearly seen, and therefore, it is excellent in design and excellent in dimensional stability, and therefore is suitable as a food filter for green tea, black tea, coffee, and the like. Characteristics. The food filter may be a flat bag. However, if it is a three-dimensional shape, the content can be more clearly seen and extracted efficiently, which is preferable. The three-dimensional shape is preferably a tetrahedral shape, a triangular pyramid three-dimensional shape or the like.

立體形狀之食品用過濾器係於將被提取物填充並封入後裝入袋中而銷售,但要求於購買之消費者自袋中取出後使用時迅速地恢復至原本之立體形狀。本發明之長纖維不織布具有彈性,從而具有適度之剛性,故而可充分地滿足上述般之要求。 The three-dimensional shape food filter is sold by being filled and sealed in an extract, and then sold in a bag, but it is required to quickly return to the original three-dimensional shape when the consumer who has purchased it is taken out from the bag. The long-fiber non-woven fabric of the present invention has elasticity and thus has moderate rigidity, so that the above-mentioned requirements can be sufficiently satisfied.

[實施例] [Examples]

以下,利用實施例對本發明具體地進行說明,但本發明並不受該等任何限定。再者,所使用之測定方法、評價方法等如下所述。 Hereinafter, the present invention will be specifically described by way of examples, but the present invention is not limited thereto. Further, the measurement methods, evaluation methods, and the like used are as follows.

(1)鈦元素含量(ppm) (1) Titanium content (ppm)

使用Thermo Fisher Scientific公司製造之ICP(Inductively Coupled Plasma,感應耦合電漿)發光分析裝置求出聚酯樹脂中之鈦元素含量。 The content of titanium element in the polyester resin was determined using an ICP (Inductively Coupled Plasma) luminescence analyzer manufactured by Thermo Fisher Scientific.

(2)平均纖維直徑(μm) (2) Average fiber diameter (μm)

使用KEYENCE公司製造之Microscope顯微鏡(VH-8000)將纖維之直徑放大成1000倍後進行測定,並利用各20條之平均值求出平均纖維直徑。 The diameter of the fiber was magnified 1000 times using a Microscope microscope (VH-8000) manufactured by KEYENCE, and the average fiber diameter was determined from the average of 20 pieces.

(3)雙折射率(△n) (3) Birefringence (Δn)

使用OLYMPUS公司製造之BH2型偏光顯微鏡補償壓力,利用通常之干擾條紋法並根據延遲與纖維直徑求出剛牽引後之纖維之雙折射率。 The pressure was compensated using a BH2 type polarizing microscope manufactured by OLYMPUS, and the birefringence of the fiber immediately after drawing was determined by the usual interference fringe method and based on the retardation and the fiber diameter.

(4)結晶度(%) (4) Crystallinity (%)

使用PerkinElmer公司製造之示差掃描熱量計DSC6000,以升溫速度10℃/min自40℃升溫至300℃後測定結晶化發熱量△Hc、結晶熔解熱量△Hm。結晶度(%)係根據下述式而求出:結晶度χc(%)=(△Hm-△Hc)/126.4×100 Using a differential scanning calorimeter DSC6000 manufactured by PerkinElmer Co., Ltd., the temperature was raised from 40 ° C to 300 ° C at a temperature increase rate of 10 ° C / min, and the crystallization heat generation amount ΔHc and the crystal melting heat amount ΔHm were measured. The degree of crystallinity (%) was determined according to the following formula: crystallinity χc (%) = (ΔHm - ΔHc) / 126.4 × 100

*126.4J/g係聚對苯二甲酸乙二酯之完全結晶之熔解熱量。 *126.4 J/g is the heat of fusion of the complete crystallization of polyethylene terephthalate.

(5)半峰全幅值(cm-1) (5) Half-peak full amplitude (cm -1 )

使用Renishaw公司製造之顯微拉曼分光裝置,以激發光532nm、激發光強度10%測定光譜。求出於光譜中所觀察到之1740cm-1附近之由C=O基所產生之波峰寬度之半峰全幅值。 The spectrum was measured using a micro-Raman spectroscopic device manufactured by Renishaw Co., Ltd. with excitation light of 532 nm and excitation light intensity of 10%. The full width at half maximum of the peak width generated by the C=O group in the vicinity of 1740 cm -1 observed in the spectrum was determined.

(6)固有黏度(IV值) (6) Intrinsic viscosity (IV value)

依據JIS K-7367-5進行測定。 The measurement was carried out in accordance with JIS K-7367-5.

(7)單位面積重量(g/m2) (7) Unit weight (g/m 2 )

依據JIS L-1906進行測定。 The measurement was carried out in accordance with JIS L-1906.

(8)厚度(mm) (8) Thickness (mm)

利用JIS L-1906所規定之方法測定負載100g/cm2之厚度。 The thickness of the load of 100 g/cm 2 was measured by the method specified in JIS L-1906.

(9)平均視密度(g/cm3) (9) Average apparent density (g/cm 3 )

根據利用JIS L-1906所規定之方法而測定之單位面積重量與厚度求出每單位體積之質量:平均視密度(g/cm3)=(單位面積重量g/m2)/((厚度mm)×1000) The mass per unit volume was determined according to the basis weight and thickness measured by the method specified in JIS L-1906: average apparent density (g/cm 3 ) = (unit weight g/m 2 ) / ((thickness mm) )×1000)

(10)熱壓接面積率(%) (10) Thermocompression bonding area ratio (%)

對1cm見方之試片進行取樣並利用電子顯微鏡拍攝照片,根據該各照片測定熱壓接部之面積,並將其平均值作為熱壓接部之面積。又,於MD方向及CD(Cross Direction,橫向)方向上測定熱壓接部之圖案之間距,並根據該等之值算出熱壓接面積占不織布之每單位面積之比率作為熱壓接面積率。 A 1 cm square test piece was sampled, and a photograph was taken by an electron microscope, and the area of the thermocompression bonded portion was measured based on the respective photographs, and the average value thereof was defined as the area of the thermocompression bonded portion. Further, the distance between the patterns of the thermocompression bonding portions is measured in the MD direction and the CD (Cross Direction) direction, and the ratio of the thermocompression bonding area to the area per unit area of the non-woven fabric is calculated as the thermocompression bonding area ratio based on the values. .

(11)透明性(%) (11) Transparency (%)

利用麥克貝思分光光度計(CE-7000A型:Sakata Inx公司製造)測定反射率(L值),求出標準白板之L值(Lw0)與標準黑板之L值(Lb0)之差作為基準,根據將試樣放置於白板上之L值(Lw)與同樣地放置於黑板上之L值(Lb)並根據下述式求出透明性:透明性(%)={(Lw-Lb)/(Lw0-Lb0)}×100 The reflectance (L value) was measured using a Macbeth spectrophotometer (CE-7000A type: manufactured by Sakata Inx Co., Ltd.), and the difference between the L value (L w0 ) of the standard whiteboard and the L value (L b0 ) of the standard blackboard was obtained as The basis is based on the L value (L w ) on which the sample is placed on the whiteboard and the L value (L b ) placed on the blackboard in the same manner and the transparency is obtained according to the following formula: transparency (%) = {(L) w -L b )/(L w0 -L b0 )}×100

(12)沸水收縮率(%) (12) boiling water shrinkage rate (%)

依據JIS L-1906,於寬度為1m之試樣上採取3處縱25cm×橫25cm之試片,將其等於沸騰水中浸漬3分鐘,並於自然乾燥後求出MD方向及CD方向之收縮率。算出各者之平均值,將MD方向與CD方向之其中較大一者之收縮率作為該不織布之沸水收縮率。 According to JIS L-1906, three test pieces of 25 cm in length and 25 cm in width were taken on a sample having a width of 1 m, which was immersed in boiling water for 3 minutes, and the shrinkage ratio in the MD direction and the CD direction was determined after natural drying. . The average value of each was calculated, and the shrinkage ratio of the larger one of the MD direction and the CD direction was taken as the boiling water shrinkage ratio of the nonwoven fabric.

(13)拉伸強度(N/30mm) (13) Tensile strength (N/30mm)

使用島津製作所公司製造之自動立體測圖儀AGS-5G型,以抓握長度100mm、拉伸速度300mm/min使30mm寬之試樣伸長,將所獲得之斷裂時之負載作為強度,對不織布之MD方向進行5次測定,求出 其平均值。 Using an automatic stereographer AGS-5G model manufactured by Shimadzu Corporation, the specimen of 30 mm width was stretched with a grip length of 100 mm and a tensile speed of 300 mm/min, and the obtained load at break was used as the strength, and the non-woven fabric was used. Five measurements in the MD direction The average value.

(14)質地係數 (14) Texture coefficient

採取20cm×30cm之試片,使用野村商事製造之Formation Tester(FMT-MIII)測定器,將利用CCD(Charge Coupled Device,電荷耦合器)照相機對18cm×25cm之範圍進行拍攝所得之透過像分解為128×128之像素,測定各個像素所接受之光之強度,並算出透過率。質地係數係將測定樣本之各微小部位(5mm×5mm)之透過率之標準偏差(σ)除以平均透過率(E)所得之值,表示微小單位單位面積重量之偏差,值越小,表示均勻性越高。 A test piece of 20 cm × 30 cm was used, and a transmission image obtained by photographing a range of 18 cm × 25 cm by a CCD (Charge Coupled Device) camera was decomposed into a measurement tester (FMT-MIII) measuring instrument manufactured by Nomura Corporation. A pixel of 128 × 128 is measured for the intensity of light received by each pixel, and the transmittance is calculated. The texture coefficient is a value obtained by dividing the standard deviation (σ) of the transmittance of each minute portion (5 mm × 5 mm) of the sample by the average transmittance (E), and indicates the deviation of the weight per unit area. The smaller the value, the smaller the value. The higher the uniformity.

質地係數=σ/E×100 Texture coefficient = σ / E × 100

(15)熱密封強度(N/30mm) (15) Heat sealing strength (N/30mm)

使用島津製作所公司製造之自動立體測圖儀AGS-5G型,將30mm寬之試樣之熱密封部分沿上下方向剝離約50mm後安裝,以握持長度50mm、拉伸速度100mm/min使其伸長,將所獲得之斷裂時之負載作為強度,並對不織布之MD方向進行5次測定,求出其平均值。熱密封條件係密封溫度210℃,密封時間1秒,壓力0.5MPa,密封面積7mm×25mm。 Using the auto-stereograph AGS-5G model manufactured by Shimadzu Corporation, the heat-sealed portion of the 30 mm-wide specimen was peeled off by about 50 mm in the up-and-down direction, and then mounted to hold the length of 50 mm and the tensile speed of 100 mm/min. The load at the time of the fracture obtained was taken as the strength, and the MD direction of the non-woven fabric was measured five times, and the average value was obtained. The heat sealing condition is a sealing temperature of 210 ° C, a sealing time of 1 second, a pressure of 0.5 MPa, and a sealing area of 7 mm × 25 mm.

(16)拉伸比 (16) Stretch ratio

根據下述式算出拉伸比:拉伸比=紡絲速度(m/min)/噴出線速度(m/min) The draw ratio was calculated according to the following formula: draw ratio = spinning speed (m/min) / discharge line speed (m/min)

噴出線速度(m/min)=單孔噴出量(g/min)/{熔融密度(g/cm3)×[紡絲嘴直徑(cm)/2]2×π} Ejection line speed (m/min) = single hole discharge amount (g/min) / {melt density (g/cm 3 ) × [spinning nozzle diameter (cm) / 2] 2 × π}

*聚酯之熔融密度:使用1.20g/cm3 * Melt density of polyester: 1.20g/cm 3

(17)聚酯長纖維不織布之每單位面積之表面積 (17) Surface area per unit area of polyester long fiber nonwoven fabric

根據長纖維不織布之比表面積m2/g×單位面積重量g/m2而求出。 It was determined from the specific surface area m 2 /g × unit area weight g/m 2 of the long fiber nonwoven fabric.

長纖維不織布之比表面積(m2/g)係利用島津製作所(股)之自動比 表面積測定機Gemini 2360而求出。又,於比表面積低於0.1m2/g之情形時,係藉由下述式而求出。 The specific surface area (m 2 /g) of the long-fiber nonwoven fabric was determined by using an automatic specific surface area measuring machine Gemini 2360 of Shimadzu Corporation. Moreover, when the specific surface area is less than 0.1 m 2 /g, it is obtained by the following formula.

表面積(m2/m2)=4×單位面積重量(g/m2)/樹脂之密度(g/cm3)/纖維直徑(μm) Surface area (m 2 /m 2 ) = 4 × weight per unit area (g/m 2 ) / density of resin (g/cm 3 ) / fiber diameter (μm)

於2種以上纖維直徑之片材之情形時,對各纖維直徑之表面積進行合計。 In the case of a sheet of two or more kinds of fiber diameters, the surface area of each fiber diameter is totaled.

(18)10%孔徑 (18) 10% aperture

自1個樣本切出10片2cm見方之試樣,利用SEM(scanning electron microscope,掃描式電子顯微鏡)觀察用之離子濺鍍裝置進行鉑蒸鍍,並利用透過光以100倍之倍率對1試樣中之10處不織布圖像進行拍攝。對圖像利用圖像解析軟體將不織布部分二值化成黑色,將孔部分二值化成白色,並對圖像中之所有孔之面積與最長徑進行數值化。圖像解析軟體係使用Asahi Kasei Engineering製造之「A像君(TM)」。將1個樣本圖像中之所有孔自最大面積向較小之面積依序排列累計,根據達到總孔面積之10%之點之孔面積,作為面積與該面積相等之圓之直徑藉由下述式求出孔徑。 Ten samples of 2 cm square were cut out from one sample, and platinum vapor deposition was performed by an ion sputtering apparatus using an SEM (scanning electron microscope), and the light was transmitted at 100 times magnification by using transmitted light. 10 non-woven images in the sample were taken. The image analysis software is used to binarize the non-woven portion into black, the hole portion is binarized to white, and the area and the longest path of all the holes in the image are quantized. The image analysis software system uses "A Like Jun (TM)" manufactured by Asahi Kasei Engineering. All the holes in one sample image are sequentially arranged from the largest area to the smaller area. According to the area of the hole reaching the point of 10% of the total hole area, the diameter of the circle equal to the area is used. The aperture is determined by the above equation.

孔徑(μm)=((4×S)/π)^0.5 Aperture (μm) = ((4 × S) / π) ^ 0.5

於上述式中,S意指孔面積(μm^2),「^0.5」意指「乘以0.5」。 In the above formula, S means the pore area (μm ^ 2), and " ^ 0.5" means "multiplied by 0.5".

(19)2.3%孔徑 (19) 2.3% aperture

代替上述10%孔徑,根據達到總孔面積之2.3%之點之孔面積求出孔徑。 Instead of the above 10% pore diameter, the pore diameter was determined from the pore area at a point which reached 2.3% of the total pore area.

(20)長徑/孔徑 (20) Long diameter / aperture

將1個樣本圖像中之所有孔自最大面積向較小之面積依序排列累計,求出達到總孔面積之2.3%之孔至達到10%之孔之間所包含之所有孔之長徑之平均值與孔徑之平均值,並藉由下述式而求出。 All the holes in one sample image are sequentially arranged from the largest area to the smaller area, and the long diameter of all the holes included between the holes reaching 2.3% of the total hole area and the holes reaching 10% is determined. The average value and the average value of the pore diameters were obtained by the following formula.

長徑/孔徑=長徑之平均值/孔徑之平均值 Long diameter / aperture = average of long diameter / average of aperture

[實施例1] [Example 1]

將鈦元素含量為0ppm、固有黏度(IV)為0.8、熔點為247℃之聚酯系樹脂供給至常用之熔融紡絲裝置並以275℃熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比2120進行熔融紡絲而獲得纖維直徑為20.5μm之聚酯長纖維。繼而,使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使該纖維開纖分散而製作單位面積重量12g/m2之網,並於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning apparatus and melted at 275 ° C, and is spun from a spinning hole having a circular cross section. The head was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 2120 to obtain a polyester long fiber having a fiber diameter of 20.5 μm. Then, using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament is 4°], the fiber is opened and dispersed to produce a net having a basis weight of 12 g/m 2 , and is applied to the embossing roll and the smooth roll. A partial thermocompression bonding was carried out at a thermocompression bonding area ratio of 15%, whereby a polyester long fiber non-woven fabric was obtained. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例2] [Embodiment 2]

於實施例1中以聚酯長纖維之纖維直徑成為25.7μm之方式進行紡絲,除此以外,以與實施例1相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 In the same manner as in Example 1, a polyester long fiber nonwoven fabric was obtained in the same manner as in Example 1 except that the fiber diameter of the polyester long fibers was 25.7 μm. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例3] [Example 3]

於實施例1中以聚酯長纖維之纖維直徑成為30.0μm之方式進行紡絲,除此以外,以與實施例1相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 1 except that the fiber diameter of the polyester long fibers was 30.0 μm. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例4] [Example 4]

於實施例3中使用IV值0.8、氧化鈦含量為12ppm之樹脂,除此以外,以與實施例3相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 3 except that a resin having an IV value of 0.8 and a titanium oxide content of 12 ppm was used in Example 3. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例5] [Example 5]

於實施例3中使用IV值0.8、氧化鈦含量為70ppm之樹脂,除此以外,以與實施例3相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 3 except that a resin having an IV value of 0.8 and a titanium oxide content of 70 ppm was used in Example 3. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例6] [Embodiment 6]

於實施例3中使用IV值0.72、氧化鈦含量為0ppm之樹脂,除此以外,以與實施例3相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 3 except that a resin having an IV value of 0.72 and a titanium oxide content of 0 ppm was used in Example 3. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例7] [Embodiment 7]

於實施例3中使用IV值0.77、氧化鈦含量為0ppm之樹脂,除此以外,以與實施例3相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 3 except that a resin having an IV value of 0.77 and a titanium oxide content of 0 ppm was used in Example 3. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例8] [Embodiment 8]

於實施例3中以聚酯長纖維不織布之單位面積重量成為20g/m2之方式進行紡絲,除此以外,以與實施例3相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 3 except that the basis weight of the polyester long-fiber nonwoven fabric was 20 g/m 2 in Example 3. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例9] [Embodiment 9]

於實施例1中以紡絲速度3770m/min、拉伸比707進行熔融紡絲並以聚酯長纖維之纖維直徑成為34.9μm之方式進行紡絲,除此以外,以與實施例1相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 In the same manner as in Example 1, except that the spinning was carried out at a spinning speed of 3,770 m/min and a draw ratio of 707, and the fiber diameter of the polyester long fibers was 34.9 μm. The way to obtain polyester long fiber non-woven fabric. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例10] [Embodiment 10]

於實施例2中以聚酯長纖維不織布之單位面積重量成為20g/m2之方式進行紡絲,並利用平滑輥進行整面熱壓接,除此以外,以與實施例2相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 In the same manner as in Example 2, except that the basis weight of the polyester long-fiber nonwoven fabric was 20 g/m 2 , and the entire surface was thermocompression bonded by a smooth roll. Polyester long fiber non-woven fabric. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例11] [Example 11]

將鈦元素含量為0ppm、固有黏度(IV)為0.8、熔點為246℃之聚酯系樹脂供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4000m/min、且拉伸比942進行熔融紡絲而獲得纖維直徑為30.1μm之聚酯長纖維。繼而,使用平 板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使該纖維開纖分散而製作單位面積重量20g/m2之網,並於壓紋輥與平滑輥間以熱壓接面積率5%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester resin having a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a conventional melt spinning apparatus and melted at 275 ° C from a spinning hole having a circular cross section. The spinning head was melt-spun at a spinning speed of 4000 m/min and a draw ratio of 942 to obtain a polyester long fiber having a fiber diameter of 30.1 μm. Then, using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament is 4°], the fiber is opened and dispersed to produce a net having a basis weight of 20 g/m 2 , and is applied to the embossing roll and the smooth roll. A partial thermocompression bonding was carried out at a thermocompression bonding area ratio of 5%, whereby a polyester long fiber non-woven fabric was obtained. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例12] [Embodiment 12]

將鈦元素含量為0ppm、固有黏度(IV)為0.8、熔點為246℃之聚酯系樹脂供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4000m/min、且拉伸比942進行熔融紡絲而獲得纖維直徑為30.0μm之聚酯長纖維。繼而,使該纖維開纖分散而製作單位面積重量12g/m2之網,並於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester resin having a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a conventional melt spinning apparatus and melted at 275 ° C from a spinning hole having a circular cross section. The spinning head was melt-spun at a spinning speed of 4000 m/min and a draw ratio of 942 to obtain a polyester long fiber having a fiber diameter of 30.0 μm. Then, the fiber was opened and dispersed to prepare a web having a basis weight of 12 g/m 2 , and a partial thermocompression bonding was performed between the embossing roll and the smooth roll at a thermocompression bonding area ratio of 15%, thereby obtaining a polyester long fiber. Not woven. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例13] [Example 13]

將鈦元素含量為0ppm、固有黏度(IV)為0.8、熔點為246℃之聚酯系樹脂供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4000m/min、且拉伸比942進行熔融紡絲,使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使纖維直徑為26.7μm之聚酯長纖維開纖分散而製作單位面積重量18g/m2之網。繼而,將鈦元素含量為12ppm、固有黏度(IV)為0.65、熔點為217℃之聚酯系樹脂供給至常用之熔融紡絲裝置並於275℃進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4150m/min、且拉伸比412進行熔融紡絲並使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使纖維直徑為15μm之聚酯長纖維開纖分散而製作單位面積重量3g/m2之網。將2層網於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester resin having a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a conventional melt spinning apparatus and melted at 275 ° C from a spinning hole having a circular cross section. The spinning head was melt-spun at a spinning speed of 4000 m/min and a draw ratio of 942, and a flat-shaped dispersion device for controlling the gas flow [the inclination angle of the flat plate with respect to the filament was 4°] was used to make the fiber diameter 26.7 μm. The polyester long fibers were opened and dispersed to produce a net having a basis weight of 18 g/m 2 . Then, a polyester resin having a titanium content of 12 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C was supplied to a conventional melt spinning apparatus and melted at 275 ° C from a spinning hole having a circular cross section. The spinning head was melt-spun at a spinning speed of 4150 m/min and a draw ratio of 412, and a flat-shaped dispersing device for controlling the gas flow [the inclination angle of the flat plate with respect to the filament was 4°] was used to make the fiber diameter 15 μm. The polyester long fibers were opened and dispersed to produce a net having a basis weight of 3 g/m 2 . A 2-layer net was partially thermocompression bonded between the embossing roll and the smooth roll at a thermocompression bonding area ratio of 15%, whereby a polyester long fiber non-woven fabric was obtained. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例14] [Embodiment 14]

將鈦元素含量為0ppm、固有黏度(IV)為0.8、熔點為246℃之聚酯系樹脂供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4000m/min、且拉伸比942進行熔融紡絲,使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使纖維直徑為24.6μm之聚酯長纖維開纖分散而製作單位面積重量10g/m2之網。繼而,將鈦元素含量為12ppm、固有黏度(IV)為0.65、熔點為254℃之聚酯系樹脂作為芯,將鈦元素含量為12ppm、固有黏度(IV)為0.65、熔點為217℃之聚酯系樹脂作為鞘供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比895進行熔融紡絲並使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使纖維直徑20μm之聚酯長纖維開纖分散而製作單位面積重量8g/m2之網。將2層網於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester resin having a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a conventional melt spinning apparatus and melted at 275 ° C from a spinning hole having a circular cross section. The spinning head was melt-spun at a spinning speed of 4000 m/min and a draw ratio of 942, and a flat-shaped dispersion device for controlling the gas flow [the inclination angle of the flat plate with respect to the filament was 4°] was used to make the fiber diameter 24.6 μm. The polyester long fibers were opened and dispersed to produce a net having a basis weight of 10 g/m 2 . Then, a polyester resin having a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as a core, and the titanium element content was 12 ppm, the intrinsic viscosity (IV) was 0.65, and the melting point was 217 ° C. The ester resin was supplied as a sheath to a conventional melt spinning apparatus and melted at 275 ° C, and a spinning head having a circular cross section of the spinning hole was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 895. The filament was expanded and dispersed using a flat-shaped dispersing device for controlling the gas flow [the inclination angle of the flat plate with respect to the filament was 4°] to produce a web having a basis weight of 8 g/m 2 by disintegrating the polyester long fibers having a fiber diameter of 20 μm. A 2-layer net was partially thermocompression bonded between the embossing roll and the smooth roll at a thermocompression bonding area ratio of 15%, whereby a polyester long fiber non-woven fabric was obtained. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例15] [Example 15]

於實施例1中以聚酯長纖維不織布之單位面積重量成為18g/m2之方式進行紡絲,除此以外,以與實施例1相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 1 except that the basis weight of the polyester long-fiber nonwoven fabric was 18 g/m 2 in the first embodiment. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例16] [Example 16]

於實施例2中以聚酯長纖維不織布之單位面積重量成為18g/m2之方式進行紡絲,除此以外,以與實施例1相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 1 except that the basis weight of the polyester long-fiber nonwoven fabric was 18 g/m 2 in the second embodiment. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例17] [Example 17]

於實施例3中以聚酯長纖維不織布之單位面積重量成為18g/m2之 方式進行紡絲,除此以外,以與實施例1相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 1 except that the basis weight of the polyester long-fiber nonwoven fabric was 18 g/m 2 in Example 3. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例18] [Embodiment 18]

於實施例1中以聚酯長纖維不織布之單位面積重量成為18g/m2之方式製成第一層不織布。於其上使用IV值0.65、鈦含量0ppm、熔點217℃之PET(polyethylene terephthalate,聚對苯二甲酸乙二酯)樹脂於紡絲溫度260℃、加熱空氣500Nm3/hr/m之條件下進行紡絲,將所獲得之纖維直徑10μm之熔噴不織布以單位面積重量5g/m2吹送至上述紡黏不織布上而獲得不織布之積層體。將所獲得之不織布之物性示於以下之表1。 In the first embodiment, the first layer nonwoven fabric was produced in such a manner that the basis weight of the polyester long fiber nonwoven fabric was 18 g/m 2 . A PET (polyethylene terephthalate) resin having an IV value of 0.65, a titanium content of 0 ppm, and a melting point of 217 ° C was used thereon at a spinning temperature of 260 ° C and a heated air of 500 Nm 3 /hr/m. In the spinning, the obtained melt-blown nonwoven fabric having a fiber diameter of 10 μm was blown onto the spunbonded nonwoven fabric at a basis weight of 5 g/m 2 to obtain a laminate of the nonwoven fabric. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例19] [Embodiment 19]

於實施例2中以聚酯長纖維不織布之單位面積重量成為18g/m2之方式製成第一層不織布。於其上使用IV值0.65、鈦含量0ppm、熔點217℃之PET樹脂於紡絲溫度255℃、加熱空氣400Nm3/hr/m之條件下進行紡絲,並將所獲得之纖維直徑15μm之熔噴不織布以單位面積重量4g/m2吹送至上述紡黏不織布上而獲得不織布之積層體。將所獲得之不織布之物性示於以下之表1。 In Example 2, a first layer of nonwoven fabric was produced in such a manner that the basis weight of the polyester long fiber nonwoven fabric was 18 g/m 2 . The PET resin having an IV value of 0.65, a titanium content of 0 ppm, and a melting point of 217 ° C was used for spinning at a spinning temperature of 255 ° C and a heated air of 400 Nm 3 /hr/m, and the obtained fiber having a diameter of 15 μm was melted. The non-woven fabric was blown onto the spunbonded nonwoven fabric at a basis weight of 4 g/m 2 to obtain a laminate of non-woven fabric. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例20] [Example 20]

於實施例3中以聚酯長纖維不織布之單位面積重量成為18g/m2之方式製成第一層不織布。於其上使用IV值0.65、鈦含量0ppm、熔點217℃之PET樹脂於紡絲溫度265℃、加熱空氣1000Nm3/hr/m之條件下進行紡絲,並將所獲得之纖維直徑7μm之熔噴不織布以單位面積重量4g/m2吹送至上述紡黏不織布上而獲得不織布之積層體。將所獲得之不織布之物性示於以下之表1。 In Example 3, a first layer of nonwoven fabric was produced in such a manner that the basis weight of the polyester long-fiber nonwoven fabric was 18 g/m 2 . The PET resin having an IV value of 0.65, a titanium content of 0 ppm, and a melting point of 217 ° C was used for spinning at a spinning temperature of 265 ° C and a heated air of 1000 Nm 3 /hr/m, and the obtained fiber having a diameter of 7 μm was melted. The non-woven fabric was blown onto the spunbonded nonwoven fabric at a basis weight of 4 g/m 2 to obtain a laminate of non-woven fabric. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例21] [Example 21]

將鈦元素含量為0ppm、固有黏度(IV)為0.8、熔點為247℃之聚 酯系樹脂供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比230進行熔融紡絲而獲得纖維直徑為14μm之聚酯長纖維。繼而,使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使該纖維開纖分散而製作單位面積重量7.5g/m2之網。繼而,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為254℃之聚酯系樹脂作為芯,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為217℃之聚酯系樹脂作為鞘供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比380進行熔融紡絲並使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使纖維直徑為14μm之聚酯長纖維開纖分散而製作單位面積重量7.5g/m2之網。將2層網於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester resin having a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning apparatus and melted at 275 ° C, from a spinning hole having a circular cross section. The spinning head was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 230 to obtain a polyester long fiber having a fiber diameter of 14 μm. Then, using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament was 4°], the fibers were opened and dispersed to produce a net having a basis weight of 7.5 g/m 2 . Then, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as a core, and the titanium element content was 0 ppm, the intrinsic viscosity (IV) was 0.65, and the melting point was 217 ° C. The ester resin was supplied as a sheath to a conventional melt spinning apparatus and melted at 275 ° C, and the spinning head of a spinning hole having a circular cross section was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 380. The filaments were spread using a flat-shaped dispersing device for controlling the gas flow [the inclination angle of the flat plate with respect to the filaments was 4°], and the polyester long fibers having a fiber diameter of 14 μm were opened to prepare a web having a basis weight of 7.5 g/m 2 . A 2-layer net was partially thermocompression bonded between the embossing roll and the smooth roll at a thermocompression bonding area ratio of 15%, whereby a polyester long fiber non-woven fabric was obtained. The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例22] [Example 22]

將鈦元素含量為12ppm、固有黏度(IV)為0.8、熔點為247℃之聚酯系樹脂供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比590進行熔融紡絲而獲得纖維直徑為20.1μm之聚酯長纖維。繼而,使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使該纖維開纖分散而製作單位面積重量7.5g/m2之網。繼而,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為254℃之聚酯系樹脂作為芯,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為217℃之聚酯系樹脂作為鞘供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比380進行熔融紡絲並使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾 斜角為4°]使纖維直徑為14μm之聚酯長纖維開纖分散而製作單位面積重量7.5g/m2之網。將2層網於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester resin having a titanium content of 12 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C was supplied to a conventional melt spinning apparatus and melted at 275 ° C from a spinning hole having a circular cross section. The spinning head was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 590 to obtain a polyester long fiber having a fiber diameter of 20.1 μm. Then, using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament was 4°], the fibers were opened and dispersed to produce a net having a basis weight of 7.5 g/m 2 . Then, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as a core, and the titanium element content was 0 ppm, the intrinsic viscosity (IV) was 0.65, and the melting point was 217 ° C. The ester resin was supplied as a sheath to a conventional melt spinning apparatus and melted at 275 ° C, and the spinning head of a spinning hole having a circular cross section was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 380. The filaments were spread using a flat-shaped dispersing device for controlling the gas flow [the inclination angle of the flat plate with respect to the filaments was 4°], and the polyester long fibers having a fiber diameter of 14 μm were opened to prepare a web having a basis weight of 7.5 g/m 2 . A 2-layer net was partially thermocompression bonded between the embossing roll and the smooth roll at a thermocompression bonding area ratio of 15%, whereby a polyester long fiber non-woven fabric was obtained. The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例23] [Example 23]

將鈦元素含量為12ppm、固有黏度(IV)為0.8、熔點為247℃之聚酯系樹脂供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比740進行熔融紡絲而獲得纖維直徑為24.6μm之聚酯長纖維。繼而,使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使該纖維開纖分散而製作單位面積重量7.5g/m2之網。繼而,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為254℃之聚酯系樹脂作為芯,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為217℃之聚酯系樹脂作為鞘供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比380進行熔融紡絲並使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使纖維直徑為14μm之聚酯長纖維開纖分散而製作單位面積重量7.5g/m2之網。將2層網於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester resin having a titanium content of 12 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C was supplied to a conventional melt spinning apparatus and melted at 275 ° C from a spinning hole having a circular cross section. The spinning head was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 740 to obtain a polyester long fiber having a fiber diameter of 24.6 μm. Then, using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament was 4°], the fibers were opened and dispersed to produce a net having a basis weight of 7.5 g/m 2 . Then, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as a core, and the titanium element content was 0 ppm, the intrinsic viscosity (IV) was 0.65, and the melting point was 217 ° C. The ester resin was supplied as a sheath to a conventional melt spinning apparatus and melted at 275 ° C, and the spinning head of a spinning hole having a circular cross section was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 380. The filaments were spread using a flat-shaped dispersing device for controlling the gas flow [the inclination angle of the flat plate with respect to the filaments was 4°], and the polyester long fibers having a fiber diameter of 14 μm were opened to prepare a web having a basis weight of 7.5 g/m 2 . A 2-layer net was partially thermocompression bonded between the embossing roll and the smooth roll at a thermocompression bonding area ratio of 15%, whereby a polyester long fiber non-woven fabric was obtained. The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例24] [Example 24]

將鈦元素含量為0ppm、固有黏度(IV)為0.8、熔點為247℃之聚酯系樹脂供給至常用之熔融紡絲裝置並於275℃下熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比550進行熔融紡絲而獲得纖維直徑為20.1μm之聚酯長纖維。繼而,使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使該纖維開纖 分散而製作單位面積重量10g/m2之網。繼而,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為254℃之聚酯系樹脂作為芯,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為217℃之聚酯系樹脂作為鞘供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比450進行熔融紡絲並使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使纖維直徑為16μm之聚酯長纖維開纖分散而製作單位面積重量5g/m2之網。將2層網於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester resin having a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning apparatus and melted at 275 ° C, and is spun from a spinning hole having a circular cross section. The filament was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 550 to obtain a polyester long fiber having a fiber diameter of 20.1 μm. Then, using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament was 4°], the fibers were opened and dispersed to produce a net having a basis weight of 10 g/m 2 . Then, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as a core, and the titanium element content was 0 ppm, the intrinsic viscosity (IV) was 0.65, and the melting point was 217 ° C. The ester resin was supplied as a sheath to a conventional melt spinning apparatus and melted at 275 ° C, and the spinning head having a circular cross section of the spinning hole was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 450. The filaments were dispersed in a flat-shaped polyester fiber having a fiber diameter of 16 μm by using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament was 4°] to produce a net having a basis weight of 5 g/m 2 . A 2-layer net was partially thermocompression bonded between the embossing roll and the smooth roll at a thermocompression bonding area ratio of 15%, whereby a polyester long fiber non-woven fabric was obtained. The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例25] [Example 25]

將鈦元素含量為0ppm、固有黏度(IV)為0.8、熔點為247℃之聚酯系樹脂供給至常用之熔融紡絲裝置並於275℃下熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比590進行熔融紡絲而獲得纖維直徑為20.1μm之聚酯長纖維。繼而,使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使該纖維開纖分散而製作單位面積重量7.5g/m2之網。繼而,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為254℃之聚酯系樹脂作為芯,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為217℃之聚酯系樹脂作為鞘供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比450進行熔融紡絲並使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使纖維直徑為16μm之聚酯長纖維開纖分散而製作單位面積重量7.5g/m2之網。將2層網於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester resin having a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning apparatus and melted at 275 ° C, and is spun from a spinning hole having a circular cross section. The filament was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 590 to obtain a polyester long fiber having a fiber diameter of 20.1 μm. Then, using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament was 4°], the fibers were opened and dispersed to produce a net having a basis weight of 7.5 g/m 2 . Then, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as a core, and the titanium element content was 0 ppm, the intrinsic viscosity (IV) was 0.65, and the melting point was 217 ° C. The ester resin was supplied as a sheath to a conventional melt spinning apparatus and melted at 275 ° C, and the spinning head having a circular cross section of the spinning hole was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 450. The filaments were dispersed in a flat-shaped polyester fiber having a fiber diameter of 16 μm by using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament was 4°] to produce a net having a basis weight of 7.5 g/m 2 . A 2-layer net was partially thermocompression bonded between the embossing roll and the smooth roll at a thermocompression bonding area ratio of 15%, whereby a polyester long fiber non-woven fabric was obtained. The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例26] [Example 26]

將鈦元素含量為0ppm、固有黏度(IV)為0.8、熔點為247℃之聚酯系樹脂供給至常用之熔融紡絲裝置並於275℃下熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比740進行熔融紡絲而獲得纖維直徑為24.6μm之聚酯長纖維。繼而,使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使該纖維開纖分散而製作單位面積重量7.5g/m2之網。繼而,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為254℃之聚酯系樹脂作為芯,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為217℃之聚酯系樹脂作為鞘供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比450進行熔融紡絲並使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使纖維直徑為16μm之聚酯長纖維開纖分散而製作單位面積重量7.5g/m2之網。將2層網於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester resin having a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning apparatus and melted at 275 ° C, and is spun from a spinning hole having a circular cross section. The filament was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 740 to obtain a polyester long fiber having a fiber diameter of 24.6 μm. Then, using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament was 4°], the fibers were opened and dispersed to produce a net having a basis weight of 7.5 g/m 2 . Then, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as a core, and the titanium element content was 0 ppm, the intrinsic viscosity (IV) was 0.65, and the melting point was 217 ° C. The ester resin was supplied as a sheath to a conventional melt spinning apparatus and melted at 275 ° C, and the spinning head having a circular cross section of the spinning hole was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 450. The filaments were dispersed in a flat-shaped polyester fiber having a fiber diameter of 16 μm by using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament was 4°] to produce a net having a basis weight of 7.5 g/m 2 . A 2-layer net was partially thermocompression bonded between the embossing roll and the smooth roll at a thermocompression bonding area ratio of 15%, whereby a polyester long fiber non-woven fabric was obtained. The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例27] [Example 27]

將鈦元素含量為12ppm、固有黏度(IV)為0.8、熔點為247℃之聚酯系樹脂供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比590進行熔融紡絲而獲得纖維直徑為20.1μm之聚酯長纖維。繼而,使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角0°]使該纖維開纖分散而製作單位面積重量7.5g/m2之網。繼而,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為254℃之聚酯系樹脂作為芯,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為217℃之聚酯系樹脂作為鞘供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓 形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比450進行熔融紡絲並使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角0°]使纖維直徑為16μm之聚酯長纖維開纖分散而製作單位面積重量7.5g/m2之網。將2層網於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester resin having a titanium content of 12 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C was supplied to a conventional melt spinning apparatus and melted at 275 ° C from a spinning hole having a circular cross section. The spinning head was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 590 to obtain a polyester long fiber having a fiber diameter of 20.1 μm. Then, the fiber was opened and dispersed using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament of 0°] to prepare a net having a basis weight of 7.5 g/m 2 . Then, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as a core, and the titanium element content was 0 ppm, the intrinsic viscosity (IV) was 0.65, and the melting point was 217 ° C. The ester resin was supplied as a sheath to a conventional melt spinning apparatus and melted at 275 ° C, and the spinning head having a circular cross section of the spinning hole was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 450. The filaments were opened and dispersed using a flat-shaped dispersing device for controlling the gas flow [the inclination angle of the flat plate with respect to the filaments by 0°] to produce a polyester long fiber having a fiber diameter of 16 μm to prepare a web having a basis weight of 7.5 g/m 2 . A 2-layer net was partially thermocompression bonded between the embossing roll and the smooth roll at a thermocompression bonding area ratio of 15%, whereby a polyester long fiber non-woven fabric was obtained. The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例28] [Example 28]

將平板狀之控制氣流之分散裝置之平板相對於長絲之傾斜角設為0°,除此以外,利用與實施例22相同之方法獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 22 except that the inclination angle of the flat plate of the flat air flow control device was set to 0° with respect to the filament. The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例29] [Example 29]

將使用低熔點樹脂之層自鞘芯結構設為並列結構,除此以外,利用與實施例21相同之方法獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 21 except that the layer of the low melting point resin was used as a side-by-side structure. The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例30] [Example 30]

將使用低熔點樹脂之層自鞘芯結構設為並列結構,除此以外,利用與實施例24相同之方法獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester long fiber nonwoven fabric was obtained by the same method as in Example 24 except that the layer of the low melting point resin was used in a side-by-side structure. The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例31] [Example 31]

將使用低熔點樹脂之層自鞘芯結構設為並列結構,除此以外,利用與實施例22相同之方法獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 22 except that the layer of the low melting point resin was used as a side-by-side structure. The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例32] [Example 32]

將各層之單位面積重量設為6g/m2,除此以外,利用與實施例21相同之方法獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 21 except that the weight per unit area of each layer was 6 g/m 2 . The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例33] [Example 33]

將各層之單位面積重量設為6g/m2,除此以外,利用與實施例22相同之方法獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 22 except that the weight per unit area of each layer was 6 g/m 2 . The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例34] [Example 34]

將各層之單位面積重量設為6g/m2,除此以外,利用與實施例23相同之方法獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 23 except that the basis weight of each layer was 6 g/m 2 . The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例35] [Example 35]

將鈦元素含量為0ppm、固有黏度(IV)為0.8、熔點為247℃之聚酯系樹脂供給至常用之熔融紡絲裝置並於275℃下熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比590進行熔融紡絲而獲得纖維直徑為20.1μm之聚酯長纖維。繼而,使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使該纖維開纖分散而製作單位面積重量12g/m2之網。繼而,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為254℃之聚酯系樹脂作為芯,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為217℃之聚酯系樹脂作為鞘供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比450進行熔融紡絲並使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使纖維直徑為16μm之聚酯長纖維開纖分散而製作單位面積重量6g/m2之網。將2層網於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester resin having a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a conventional melt spinning apparatus and melted at 275 ° C, and is spun from a spinning hole having a circular cross section. The filament was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 590 to obtain a polyester long fiber having a fiber diameter of 20.1 μm. Then, using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament was 4°], the fibers were opened and dispersed to produce a net having a basis weight of 12 g/m 2 . Then, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as a core, and the titanium element content was 0 ppm, the intrinsic viscosity (IV) was 0.65, and the melting point was 217 ° C. The ester resin was supplied as a sheath to a conventional melt spinning apparatus and melted at 275 ° C, and the spinning head having a circular cross section of the spinning hole was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 450. The filaments were dispersed in a flat-shaped polyester fiber having a fiber diameter of 16 μm by using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament was 4°] to produce a net having a basis weight of 6 g/m 2 . A 2-layer net was partially thermocompression bonded between the embossing roll and the smooth roll at a thermocompression bonding area ratio of 15%, whereby a polyester long fiber non-woven fabric was obtained. The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例36] [Example 36]

將各層之單位面積重量設為9g/m2,除此以外,利用與實施例25 相同之方法獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 25 except that the basis weight of each layer was changed to 9 g/m 2 . The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例37] [Example 37]

將各層之單位面積重量設為9g/m2,除此以外,利用與實施例21相同之方法獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表1。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 21 except that the weight per unit area of each layer was changed to 9 g/m 2 . The physical properties of the obtained non-woven fabric are shown in Table 1 below.

[實施例38] [Example 38]

將鈦元素含量為12ppm、固有黏度(IV)為0.8、熔點為247℃之聚酯系樹脂供給至常用之熔融紡絲裝置並於305℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比230進行熔融紡絲而獲得纖維直徑為10μm之聚酯長纖維。繼而,使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使該纖維開纖分散而製作單位面積重量7.5g/m2之網。繼而,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為254℃之聚酯系樹脂作為芯,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為217℃之聚酯系樹脂作為鞘供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min、且拉伸比380進行熔融紡絲並使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使纖維直徑為14μm之聚酯長纖維開纖分散而製作單位面積重量7.5g/m2之網。將2層網於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester resin having a titanium content of 12 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C was supplied to a conventional melt spinning apparatus and melted at 305 ° C from a spinning hole having a circular cross section. The spinning head was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 230 to obtain a polyester long fiber having a fiber diameter of 10 μm. Then, using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament was 4°], the fibers were opened and dispersed to produce a net having a basis weight of 7.5 g/m 2 . Then, a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as a core, and the titanium element content was 0 ppm, the intrinsic viscosity (IV) was 0.65, and the melting point was 217 ° C. The ester resin was supplied as a sheath to a conventional melt spinning apparatus and melted at 275 ° C, and the spinning head of a spinning hole having a circular cross section was melt-spun at a spinning speed of 4500 m/min and a draw ratio of 380. The filaments were spread using a flat-shaped dispersing device for controlling the gas flow [the inclination angle of the flat plate with respect to the filaments was 4°], and the polyester long fibers having a fiber diameter of 14 μm were opened to prepare a web having a basis weight of 7.5 g/m 2 . A 2-layer net was partially thermocompression bonded between the embossing roll and the smooth roll at a thermocompression bonding area ratio of 15%, whereby a polyester long fiber non-woven fabric was obtained. The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[實施例39] [Example 39]

將各層之纖維直徑設為13μm,除此以外,利用與實施例32相同之方法獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表2。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 32 except that the fiber diameter of each layer was changed to 13 μm. The physical properties of the obtained non-woven fabric are shown in Table 2 below.

[比較例1] [Comparative Example 1]

於實施例1中將聚酯系樹脂之鈦元素含量設為3000ppm,並以聚酯長纖維之單位面積重量成為20.0g/m2之方式進行紡絲,除此以外,以與實施例1相同之方式獲得聚酯長纖維不織布,但不織布之透明性較低,作為食品用過濾器無法獲得充分之透明性。將所獲得之不織布之物性示於以下之表3。 In the first embodiment, the content of the titanium element of the polyester resin is 3,000 ppm, and the basis weight of the polyester long fiber is 20.0 g/m 2 , and the same as in the first embodiment. In this way, polyester long-fiber non-woven fabric is obtained, but the non-woven fabric has low transparency, and sufficient transparency cannot be obtained as a food filter. The physical properties of the obtained non-woven fabric are shown in Table 3 below.

[比較例2] [Comparative Example 2]

於實施例1中將以拉伸比545進行熔融紡絲後之聚酯長纖維之纖維直徑設為12.0μm,並以聚酯長纖維之單位面積重量成為20g/m2之方式進行紡絲,除此以外,以與實施例1相同之方式獲得聚酯長纖維不織布,但不織布之透明性較低,作為食品用過濾器無法獲得充分之透明性。將所獲得之不織布之物性示於以下之表3。 In the first embodiment, the fiber length of the polyester long fibers after melt-spinning at a draw ratio of 545 was set to 12.0 μm, and the basis weight of the polyester long fibers was 20 g/m 2 . Except for this, a polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 1, but the nonwoven fabric was low in transparency, and sufficient transparency could not be obtained as a food filter. The physical properties of the obtained non-woven fabric are shown in Table 3 below.

[比較例3] [Comparative Example 3]

使用鈦元素含量為12ppm、固有黏度(IV)為0.65、熔點為253℃之聚酯系樹脂,除此以外,以與實施例1相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表3。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 1 except that a polyester resin having a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 253 ° C was used. The physical properties of the obtained non-woven fabric are shown in Table 3 below.

[比較例4] [Comparative Example 4]

使用鈦元素含量為12ppm、固有黏度(IV)為0.65、熔點為253℃之聚酯系樹脂,除此以外,以與實施例2相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表3。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 2 except that a polyester resin having a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 253 ° C was used. The physical properties of the obtained non-woven fabric are shown in Table 3 below.

[比較例5] [Comparative Example 5]

使用鈦元素含量為12ppm、固有黏度(IV)為0.65、熔點為253℃之聚酯系樹脂,除此以外,以與實施例3相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表3。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 3 except that a polyester resin having a titanium element content of 12 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 253 ° C was used. The physical properties of the obtained non-woven fabric are shown in Table 3 below.

[比較例6] [Comparative Example 6]

使用鈦元素含量為12ppm、固有黏度(IV)為0.65、熔點為253℃ 之聚酯系樹脂,除此以外,以與實施例4相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表3。 The titanium content is 12 ppm, the intrinsic viscosity (IV) is 0.65, and the melting point is 253 °C. A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 4 except for the polyester resin. The physical properties of the obtained non-woven fabric are shown in Table 3 below.

[比較例7] [Comparative Example 7]

使用鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為253℃之聚酯系樹脂,除此以外,以與實施例3相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表3。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 3 except that a polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 253 ° C was used. The physical properties of the obtained non-woven fabric are shown in Table 3 below.

[比較例8] [Comparative Example 8]

將鈦元素含量為0ppm、固有黏度(IV)為0.8、熔點為246℃之聚酯系樹脂供給至常用之熔融紡絲裝置並於295℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4000m/min、且拉伸比191進行熔融紡絲而獲得纖維直徑為30.3μm之聚酯長纖維。繼而,使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使該纖維開纖分散而製作單位面積重量20/m2之網,並於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布,但作為食品用過濾器無法獲得充分之尺寸穩定性。將所獲得之不織布之物性示於以下之表3。 A polyester resin having a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a conventional melt spinning apparatus and melted at 295 ° C from a spinning hole having a circular cross section. The spinning head was melt-spun at a spinning speed of 4000 m/min and a draw ratio of 191 to obtain a polyester long fiber having a fiber diameter of 30.3 μm. Then, using a flat-shaped dispersing device for controlling the air flow [the inclination angle of the flat plate with respect to the filament is 4°], the fiber is opened and dispersed to produce a net having a basis weight of 20/m 2 , and is applied to the embossing roller and the smoothing roller. The partial thermocompression bonding was carried out at a thermocompression bonding area ratio of 15%, whereby a polyester long fiber nonwoven fabric was obtained, but sufficient dimensional stability could not be obtained as a food filter. The physical properties of the obtained non-woven fabric are shown in Table 3 below.

[比較例9] [Comparative Example 9]

於比較例8中將以拉伸比345進行熔融紡絲後之聚酯長纖維之纖維直徑設為50.0μm,並以聚酯長纖維之單位面積重量成為20g/m2之方式進行紡絲,但於輥之收縮較大而無法獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表3。 In Comparative Example 8, the fiber diameter of the polyester long fibers which were melt-spun at a draw ratio of 345 was set to 50.0 μm, and the basis weight of the polyester long fibers was 20 g/m 2 . However, the shrinkage of the roll is large and the polyester long fiber non-woven fabric cannot be obtained. The physical properties of the obtained non-woven fabric are shown in Table 3 below.

[比較例10] [Comparative Example 10]

於實施例3中以聚酯長纖維之單位面積重量成為40g/m2之方式製作網,除此以外,以與實施例3相同之方式獲得聚酯長纖維不織布,但不織布之透明性較低,作為食品用過濾器無法獲得充分之透明性。將所獲得之不織布之物性示於以下之表3。 In the third embodiment, a polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 3 except that the basis weight of the polyester long fibers was 40 g/m 2 , but the nonwoven fabric was low in transparency. As a food filter, sufficient transparency cannot be obtained. The physical properties of the obtained non-woven fabric are shown in Table 3 below.

[比較例11] [Comparative Example 11]

將樹脂之鈦含量設為3000ppm,除此以外,以與實施例21相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表3。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 21 except that the titanium content of the resin was 3,000 ppm. The physical properties of the obtained non-woven fabric are shown in Table 3 below.

[比較例12] [Comparative Example 12]

將樹脂之IV值設為0.7,除此以外,以與比較例11相同之方式獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表3。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Comparative Example 11, except that the IV value of the resin was changed to 0.7. The physical properties of the obtained non-woven fabric are shown in Table 3 below.

[比較例13] [Comparative Example 13]

將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為254℃之聚酯系樹脂作為芯,將鈦元素含量為0ppm、固有黏度(IV)為0.65、熔點為217℃之聚酯系樹脂作為鞘供給至常用之熔融紡絲裝置並於275℃下進行熔融,自具有圓形剖面之紡絲孔之紡絲頭以紡絲速度4500m/min進行熔融紡絲並使用平板狀之控制氣流之分散裝置[平板相對於長絲之傾斜角為4°]使纖維直徑為14μm之聚酯長纖維開纖分散,將單位面積重量15g/m2之網於壓紋輥與平滑輥間以熱壓接面積率15%進行局部熱壓接,藉此獲得聚酯長纖維不織布。將所獲得之不織布之物性示於以下之表3。再者,於對所獲得之不織布進行熱密封時,密封機產生嚴重之樹脂污染。 A polyester resin having a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, a melting point of 254 ° C as a core, a titanium element content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C. The resin was supplied as a sheath to a conventional melt spinning apparatus and melted at 275 ° C, and the spinning head of a spinning hole having a circular cross section was melt-spun at a spinning speed of 4500 m/min and a flat shaped controlled air flow was used. The dispersing device [the inclination angle of the flat plate with respect to the filament is 4°], the polyester long fiber having a fiber diameter of 14 μm is opened and dispersed, and the web having a basis weight of 15 g/m 2 is heated between the embossing roller and the smoothing roller. The crimping area ratio of 15% was subjected to partial thermocompression bonding, whereby a polyester long fiber nonwoven fabric was obtained. The physical properties of the obtained non-woven fabric are shown in Table 3 below. Furthermore, the sealing machine produces severe resin contamination when the obtained non-woven fabric is heat-sealed.

[比較例14] [Comparative Example 14]

將各層之單位面積重量設為10g/m2,除此以外,利用與實施例21相同之方法獲得聚酯長纖維不織布。將所獲得之不織布之物性示於表3。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 21 except that the weight per unit area of each layer was changed to 10 g/m 2 . The physical properties of the obtained non-woven fabric are shown in Table 3.

[比較例15] [Comparative Example 15]

將各層之單位面積重量設為4g/m2,除此以外,利用與實施例26相同之方法獲得聚酯長纖維不織布。將所獲得之不織布之物性示於表3。 A polyester long fiber nonwoven fabric was obtained in the same manner as in Example 26 except that the weight per unit area of each layer was 4 g/m 2 . The physical properties of the obtained non-woven fabric are shown in Table 3.

[產業上之可利用性] [Industrial availability]

本發明之單層或複層聚酯長纖維不織布由於透明性、尺寸穩定性、粉體滲漏性、及成分提取性優異,故而可較佳地用作食品用過濾器。 The single-layer or multi-layer polyester long-fiber nonwoven fabric of the present invention is preferably used as a food filter because it is excellent in transparency, dimensional stability, powder leakage property, and component extractability.

Claims (18)

一種單層或複層聚酯長纖維不織布,其無機系粒子之含量為0~100ppm,10%點孔徑未達1000μm,10%點孔徑與2.3%點孔徑之差為500以下,且單位面積重量為10~30g/m2A single-layer or multi-layer polyester long-fiber non-woven fabric, wherein the content of inorganic particles is 0-100 ppm, the pore diameter of 10% is less than 1000 μm, the difference between the pore diameter of 10% point and the pore diameter of 2.3% is 500 or less, and the weight per unit area It is 10~30g/m 2 . 如請求項1之單層或複層聚酯長纖維不織布,其熱壓接面積率為5~40%,且平均視密度為0.1~0.5g/cm3The single-layer or multi-layer polyester long-fiber non-woven fabric of claim 1 has a thermocompression bonding area ratio of 5 to 40% and an average apparent density of 0.1 to 0.5 g/cm 3 . 如請求項1或2之單層或複層聚酯長纖維不織布,其平均纖維直徑為13~40μm。 The single-layer or multi-layer polyester long-fiber non-woven fabric of claim 1 or 2 has an average fiber diameter of 13 to 40 μm. 如請求項1至3中任一項之單層或複層聚酯長纖維不織布,其中至少1層包含拉曼光譜中所觀測到之1740cm-1附近之由C=O基所產生之波峰寬度之半峰全幅值之平均值為18~24cm-1的纖維。 A single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of claims 1 to 3, wherein at least one layer contains a peak width generated by a C=O group in the vicinity of 1740 cm -1 observed in a Raman spectrum The average value of the full width at half maximum is 18 to 24 cm -1 of fiber. 如請求項1至4中任一項之單層或複層聚酯長纖維不織布,其中至少1層包含結晶度為30~50%之纖維。 A single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of claims 1 to 4, wherein at least one of the layers comprises fibers having a crystallinity of 30 to 50%. 如請求項1至5中任一項之單層或複層聚酯長纖維不織布,其中至少1層包含雙折射率0.04~0.12之纖維。 A single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of claims 1 to 5, wherein at least one of the layers comprises fibers having a birefringence of from 0.04 to 0.12. 如請求項1至6中任一項之單層或複層聚酯長纖維不織布,其透明性為60%以上。 The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of claims 1 to 6, which has a transparency of 60% or more. 如請求項1至7中任一項之單層或複層聚酯長纖維不織布,其沸水收縮率為2.0%以下。 The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of claims 1 to 7, which has a boiling water shrinkage ratio of 2.0% or less. 如請求項1至8中任一項之單層或複層聚酯長纖維不織布,其質地係數為0.5~2.0。 The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of claims 1 to 8, which has a texture coefficient of 0.5 to 2.0. 如請求項1至9中任一項之單層或複層聚酯長纖維不織布,其中至少1層之拉伸強度為5N/30mm以上。 The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of claims 1 to 9, wherein at least one of the layers has a tensile strength of 5 N/30 mm or more. 如請求項1至10中任一項之單層或複層聚酯長纖維不織布,其中至少1層含有熔點240℃以下之低熔點纖維。 A single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of claims 1 to 10, wherein at least one of the layers contains a low-melting fiber having a melting point of 240 ° C or less. 如請求項1至11中任一項之聚酯長纖維不織布,其包含藉由熱壓接而將下述a層與b層一體化而成之積層不織布,a層:包含與高熔點樹脂之熔點差為30℃~150℃之低熔點樹脂之聚酯長纖維不織布b層:包含上述高熔點樹脂之聚酯長纖維不織布。 The polyester long-fiber nonwoven fabric according to any one of claims 1 to 11, which comprises a laminated non-woven fabric obtained by integrating the following a layer and b layer by thermocompression bonding, and a layer: comprising a high melting point resin. Polyester long fiber non-woven fabric b layer of a low melting point resin having a melting point difference of 30 ° C to 150 ° C: a polyester long fiber nonwoven fabric comprising the above high melting point resin. 如請求項1至12中任一項之單層或複層聚酯長纖維不織布,其具有上述聚酯長纖維不織布之纖維之配向性於剖面方向上不同之結構。 The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of claims 1 to 12, which has a structure in which the orientation of the fibers of the above-mentioned polyester long-fiber nonwoven fabric is different in the cross-sectional direction. 如請求項1至13中任一項之單層或複層聚酯長纖維不織布,其中至少1層含有包含0~25%之間苯二甲酸之樹脂。 A single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of claims 1 to 13, wherein at least one of the layers contains a resin containing 0 to 25% of phthalic acid. 如請求項1至14中任一項之單層或複層聚酯長纖維不織布,其中上述無機系粒子為氧化鈦。 The single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of claims 1 to 14, wherein the inorganic-based particles are titanium oxide. 如請求項15之單層或複層聚酯長纖維不織布,其包含鈦元素含量0~0.1ppm之樹脂。 A single-layer or multi-layer polyester long-fiber non-woven fabric according to claim 15, which comprises a resin having a titanium content of 0 to 0.1 ppm. 如請求項1至16中任一項之單層或複層聚酯長纖維不織布,其中製成不織布後之樹脂之IV值為0.6以上。 The single-layer or multi-layer polyester long-fiber non-woven fabric according to any one of claims 1 to 16, wherein the resin having the non-woven fabric has an IV value of 0.6 or more. 一種食品用過濾器,其包含如請求項1至17中任一項之單層或複層聚酯長纖維不織布。 A food filter comprising the single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of claims 1 to 17.
TW105110377A 2015-04-03 2016-03-31 Single-layer or multi-layer polyester long fiber non-woven fabric and food filter using the same TWI624571B (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI733906B (en) * 2017-05-20 2021-07-21 日商大紀商事股份有限公司 Extraction sheet material, extraction filter and extraction bag

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020196340A1 (en) * 2019-03-22 2020-10-01 旭化成株式会社 Non-woven fabric for sterilization packaging material
CN111729403B (en) * 2019-03-25 2022-07-12 东丽纤维研究所(中国)有限公司 Air filtering material and application thereof
CN110079890A (en) * 2019-04-26 2019-08-02 绍兴喜能纺织科技有限公司 A kind of bicomponent composite fibre and preparation method thereof
CN110589245A (en) * 2019-10-14 2019-12-20 南昌蒸鼎科技开发有限公司 Closed self-heating container
JP6775863B1 (en) * 2020-06-19 2020-10-28 大紀商事株式会社 Sheet material for extraction
KR102497942B1 (en) 2021-11-12 2023-02-09 주식회사 제이케이상사 eco-friendly biodegradability manufacturing methods of non-woven filter
CN114762783B (en) * 2022-03-23 2024-04-02 杭州诗蓝过滤科技有限公司 Multilayer composite liquid filtering material

Family Cites Families (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0818414B2 (en) * 1986-12-26 1996-02-28 旭化成工業株式会社 Moldable composite sheet
JP2520888B2 (en) * 1986-12-26 1996-07-31 旭化成工業株式会社 Laminate sheet for thermoforming and method for producing the same
JPH1143855A (en) 1997-05-26 1999-02-16 Unitika Ltd Packing material composed of non-woven fabric of conjugate, continuous fiber
JP2001131826A (en) 1999-10-27 2001-05-15 Nippon Ester Co Ltd Biodegradable monofilament for tea bag
JP2001146671A (en) * 1999-11-16 2001-05-29 Toyobo Co Ltd Long fiber nonwoven fabric
JP4209629B2 (en) * 2002-04-23 2009-01-14 日本バイリーン株式会社 Oil blotting sheet
EP1553224B1 (en) 2002-07-01 2011-09-28 Asahi Kasei Fibers Corporation Nonwoven fabric and tea bag
JP2007152216A (en) * 2005-12-05 2007-06-21 Toray Ind Inc Nonwoven fabric for filter
JP5030427B2 (en) * 2006-01-25 2012-09-19 旭化成せんい株式会社 Bag
TWI349614B (en) * 2006-01-25 2011-10-01 Asahi Kasei Fibers Corp Non-woven fabric laminated by heat bonding
JP4944545B2 (en) * 2006-08-30 2012-06-06 旭化成せんい株式会社 FILTER FILTER MATERIAL AND METHOD FOR PRODUCING FOOD-INCLOSED PAG
JP5064898B2 (en) * 2007-06-11 2012-10-31 旭化成せんい株式会社 Food filter and food-enclosed bag body using the same
JP4866794B2 (en) * 2007-06-14 2012-02-01 旭化成せんい株式会社 Food filter and food enclosing bag body using the same
JP4916984B2 (en) * 2007-09-19 2012-04-18 株式会社クラレ Non-woven
JP5315776B2 (en) * 2008-04-30 2013-10-16 静岡県 Drip tea bags
WO2011040337A1 (en) * 2009-09-30 2011-04-07 株式会社Adeka Polyester resin composition, polyester fiber, polyester resin molded article, and process for production of nucleating agent for polyester resin
TWI618279B (en) * 2012-04-04 2018-03-11 Asahi Kasei Fibers Corp Divider material
KR20150043423A (en) * 2012-09-19 2015-04-22 아사히 가세이 가부시키가이샤 Separator, manufacturing method thereof, and lithium ion secondary cell
WO2014097462A1 (en) * 2012-12-20 2014-06-26 大紀商事株式会社 Extraction filter and extraction bag
JP2015076416A (en) * 2013-10-04 2015-04-20 旭化成せんい株式会社 Nonwoven cloth, separator using the same, and solid electrolytic capacitor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI733906B (en) * 2017-05-20 2021-07-21 日商大紀商事股份有限公司 Extraction sheet material, extraction filter and extraction bag

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