TWI624571B - Single-layer or multi-layer polyester long fiber non-woven fabric and food filter using the same - Google Patents
Single-layer or multi-layer polyester long fiber non-woven fabric and food filter using the same Download PDFInfo
- Publication number
- TWI624571B TWI624571B TW105110377A TW105110377A TWI624571B TW I624571 B TWI624571 B TW I624571B TW 105110377 A TW105110377 A TW 105110377A TW 105110377 A TW105110377 A TW 105110377A TW I624571 B TWI624571 B TW I624571B
- Authority
- TW
- Taiwan
- Prior art keywords
- layer
- polyester long
- nonwoven fabric
- fiber
- woven fabric
- Prior art date
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- 239000000835 fiber Substances 0.000 title claims abstract description 304
- 239000004745 nonwoven fabric Substances 0.000 title claims abstract description 276
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- 239000010410 layer Substances 0.000 title claims abstract description 92
- 239000002356 single layer Substances 0.000 title claims abstract description 39
- 235000013305 food Nutrition 0.000 title claims abstract description 27
- 239000011148 porous material Substances 0.000 claims abstract description 26
- 239000010954 inorganic particle Substances 0.000 claims abstract description 17
- 238000002844 melting Methods 0.000 claims description 80
- 230000008018 melting Effects 0.000 claims description 75
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- 239000011347 resin Substances 0.000 claims description 73
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 55
- 239000010936 titanium Substances 0.000 claims description 48
- 229910052719 titanium Inorganic materials 0.000 claims description 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 238000009835 boiling Methods 0.000 claims description 12
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 claims description 12
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 11
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims description 9
- 238000001237 Raman spectrum Methods 0.000 claims description 3
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- 235000013616 tea Nutrition 0.000 description 10
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- 238000004519 manufacturing process Methods 0.000 description 6
- 238000012545 processing Methods 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
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- 229910052618 mica group Inorganic materials 0.000 description 5
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- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 4
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 4
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 description 4
- 125000003118 aryl group Chemical group 0.000 description 4
- 238000002788 crimping Methods 0.000 description 4
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- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 description 4
- 239000006224 matting agent Substances 0.000 description 4
- 239000005022 packaging material Substances 0.000 description 4
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- 238000001069 Raman spectroscopy Methods 0.000 description 3
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- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 3
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- 238000000354 decomposition reaction Methods 0.000 description 3
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- 235000014113 dietary fatty acids Nutrition 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 238000000113 differential scanning calorimetry Methods 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 239000000194 fatty acid Substances 0.000 description 3
- 229930195729 fatty acid Natural products 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000009616 inductively coupled plasma Methods 0.000 description 3
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
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- 239000005995 Aluminium silicate Substances 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 2
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- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 235000012211 aluminium silicate Nutrition 0.000 description 2
- 239000003242 anti bacterial agent Substances 0.000 description 2
- 235000020279 black tea Nutrition 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
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- 239000000155 melt Substances 0.000 description 2
- KYTZHLUVELPASH-UHFFFAOYSA-N naphthalene-1,2-dicarboxylic acid Chemical compound C1=CC=CC2=C(C(O)=O)C(C(=O)O)=CC=C21 KYTZHLUVELPASH-UHFFFAOYSA-N 0.000 description 2
- 150000004767 nitrides Chemical class 0.000 description 2
- 229920001707 polybutylene terephthalate Polymers 0.000 description 2
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- 238000011160 research Methods 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 238000001228 spectrum Methods 0.000 description 2
- 150000003609 titanium compounds Chemical class 0.000 description 2
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 1
- SHKPLYHDOBTMCI-UHFFFAOYSA-I Cl(=O)[O-].[Al+3].[Fe+2].Cl(=O)[O-].Cl(=O)[O-].Cl(=O)[O-].Cl(=O)[O-] Chemical compound Cl(=O)[O-].[Al+3].[Fe+2].Cl(=O)[O-].Cl(=O)[O-].Cl(=O)[O-].Cl(=O)[O-] SHKPLYHDOBTMCI-UHFFFAOYSA-I 0.000 description 1
- 240000007154 Coffea arabica Species 0.000 description 1
- 241000218631 Coniferophyta Species 0.000 description 1
- 229920001634 Copolyester Polymers 0.000 description 1
- 239000004609 Impact Modifier Substances 0.000 description 1
- 239000005909 Kieselgur Substances 0.000 description 1
- 240000007817 Olea europaea Species 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 229920000954 Polyglycolide Polymers 0.000 description 1
- 229920000265 Polyparaphenylene Polymers 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 description 1
- 229910052581 Si3N4 Inorganic materials 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- NRTOMJZYCJJWKI-UHFFFAOYSA-N Titanium nitride Chemical compound [Ti]#N NRTOMJZYCJJWKI-UHFFFAOYSA-N 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 229910000611 Zinc aluminium Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 229940061720 alpha hydroxy acid Drugs 0.000 description 1
- 150000001280 alpha hydroxy acids Chemical class 0.000 description 1
- KCZFLPPCFOHPNI-UHFFFAOYSA-N alumane;iron Chemical compound [AlH3].[Fe] KCZFLPPCFOHPNI-UHFFFAOYSA-N 0.000 description 1
- HXFVOUUOTHJFPX-UHFFFAOYSA-N alumane;zinc Chemical compound [AlH3].[Zn] HXFVOUUOTHJFPX-UHFFFAOYSA-N 0.000 description 1
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- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
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- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
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- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- NJLLQSBAHIKGKF-UHFFFAOYSA-N dipotassium dioxido(oxo)titanium Chemical compound [K+].[K+].[O-][Ti]([O-])=O NJLLQSBAHIKGKF-UHFFFAOYSA-N 0.000 description 1
- YGANSGVIUGARFR-UHFFFAOYSA-N dipotassium dioxosilane oxo(oxoalumanyloxy)alumane oxygen(2-) Chemical compound [O--].[K+].[K+].O=[Si]=O.O=[Al]O[Al]=O YGANSGVIUGARFR-UHFFFAOYSA-N 0.000 description 1
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- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
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Classifications
-
- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING 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
- D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
- D04H3/005—Synthetic yarns or filaments
- D04H3/009—Condensation or reaction polymers
- D04H3/011—Polyesters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
- B01D39/1607—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous
- B01D39/1623—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin
- B01D39/163—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin sintered or bonded
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS 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
- B65D77/00—Packages formed by enclosing articles or materials in preformed containers, e.g. boxes, cartons, sacks or bags
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- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING 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
- D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
- D04H3/08—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating
- D04H3/14—Non-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
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/04—Additives and treatments of the filtering material
- B01D2239/0407—Additives and treatments of the filtering material comprising particulate additives, e.g. adsorbents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/06—Filter cloth, e.g. knitted, woven non-woven; self-supported material
- B01D2239/065—More than one layer present in the filtering material
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2239/00—Aspects relating to filtering material for liquid or gaseous fluids
- B01D2239/12—Special parameters characterising the filtering material
- B01D2239/1241—Particle diameter
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W90/00—Enabling technologies or technologies with a potential or indirect contribution to greenhouse gas [GHG] emissions mitigation
- Y02W90/10—Bio-packaging, e.g. packing containers made from renewable resources or bio-plastics
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Textile Engineering (AREA)
- Mechanical Engineering (AREA)
- Nonwoven Fabrics (AREA)
- Apparatus For Making Beverages (AREA)
- Tea And Coffee (AREA)
- Filtering Materials (AREA)
- Packages (AREA)
Abstract
本發明提供一種透明性、尺寸穩定性、粉體滲漏性、及成分提取性優異之單層或複層聚酯長纖維不織布、及使用其之食品用過濾器。本發明之單層或複層聚酯長纖維不織布之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。 The present invention provides a single-layer or multi-layer polyester long fiber non-woven fabric excellent in transparency, dimensional stability, powder leakage, and component extractability, and a food filter using the same. The content of the inorganic particles of the single-layer or multi-layer polyester long-fiber nonwoven fabric of the present invention is 0-100 ppm, the 10% point pore size is less than 1000 μm, the difference between the 10% point pore size and 2.3% point pore size is less than 500, and the unit area The weight is 10 ~ 30g / m 2 .
Description
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 nonwoven fabric excellent in transparency, dimensional stability, powder leakage, 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, non-woven fabrics containing resins such as polyethylene, polypropylene, polyester, and polyamide were used as packaging materials. 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 fiber dense, so that the inside cannot be confirmed. In addition, when 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 bags often use paper, but there are problems such as poor transparency, inability to see the contents of the packaging materials, and the inability to perform heat sealing processing.
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。 The following Patent Document 1 discloses a nonwoven fabric for tea bags with improved transparency, but there is no description related to dimensional stability, and no special attention is paid. Furthermore, 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 suitable for measurement is in the range of nanometers to micrometers, and the pore diameter is expressed after converting the pressure, Therefore, it is not an evaluation method suitable for the actual tea used.
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。 In addition, Patent Document 2 below discloses that a biodegradable monofilament for tea bags containing poly L-lactic acid with a fineness of 15 to 35 dtex has a high fineness and high transparency, but the boiled water shrinkage rate of the monofilament exists. The problem of less than 20% and 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。 Furthermore, it is disclosed in Patent Document 3 below that the polyolefin-based polymer is included as A nonwoven fabric with a sheath component and a core sheath type composite long fiber with a polyester polymer having a melting point higher than the above sheath component as a core component, which has excellent heat sealability, but has low dimensional stability and is not related to transparency Records, but not pay special attention to.
[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 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. 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。 In view of the above-mentioned problems of the prior art, the present invention provides a polyester long-fiber nonwoven fabric excellent in transparency, dimensional stability, powder leakage, 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。 In order to solve the above problems, the inventors of the present invention conducted intensive research and repeated experiments. As a result, it was found that a polyester resin having a titanium content in a specific range was selected, and the structure, fiber diameter, and unit area of the fiber constituting the nonwoven fabric were selected. A detailed study was carried out from the viewpoint of weight and thermocompression bonding area ratio to obtain a nonwoven fabric with good spinnability, excellent component extractability as a filter for food, and good transparency and dimensional stability. Furthermore, the use of the pore diameter calculated by directly observing the nonwoven fabric was defined as the evaluation of the powder leakage property, thereby completing the present invention.
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 nonwoven fabric, in which the content of inorganic particles is 0-100 ppm, the 10% point pore size is less than 1000 μm, and the difference between the 10% point pore size and 2.3% point pore size 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 as described in [1] above 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 non-woven fabric as described in [1] or [2] above has an average fiber diameter of 13-40 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 nonwoven fabric as described in any one of the above [1] to [3], wherein at least one layer is composed of C = around 1740cm -1 observed in the Raman spectrum Fibers with an average value of the half-peak full amplitude of the peak width generated by the O group are 18 ~ 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 the above [1] to [4], wherein at least one layer contains fibers with 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 with 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], whose transparency is 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] has a boiling water shrinkage rate 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] 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 the above [1] to [9], wherein at least one layer 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 the above [1] to [10], wherein at least one layer contains low-melting-point fibers having a melting point of 240 ° C or lower.
[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 the above [1] to [11], which includes a laminated nonwoven 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 Layer a: Polyester long-fiber non-woven fabric containing low-melting point resin with a melting point difference of 30-150 ° C from the 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-mentioned 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 nonwoven fabric according to any one of the above [1] to [12], It has a structure in which the orientation of the fibers of the polyester long fiber nonwoven fabric 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 the above [1] to [13], 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 the above [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 as described in [15] above, which contains a resin with a titanium 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 non-woven fabric according to any one of the above [1] to [16], wherein the IV value of the resin after making the non-woven fabric is 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 food filter comprising the single-layer or multi-layer polyester long-fiber nonwoven fabric according to any one of the above [1] to [17].
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 fibers constituting the single-layer or multi-layer polyester long-fiber non-woven fabric of the present invention have good spinnability, and the food filter manufactured using the non-woven fabric containing the fiber has excellent extractability of components, 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 diagram showing an example of a device for controlling airflow 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。 Figure 2 is a graph showing the relationship between boiling water shrinkage 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 stretch ratio and 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 spinning temperature and 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 IV value of the resin and the crystallinity of the alignment.
以下,對本發明之實施形態詳細地進行說明。 Hereinafter, the 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 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. Butyl dicarboxylate or polytrimethylene terephthalate is a typical example, and it may also be a polyester obtained by polymerizing or copolymerizing phthalic acid, phthalic acid, or the like between acid components forming an ester. The thermoplastic polyester may further be a resin having biodegradability, such as polyglycolic acid or polylactic acid-like poly (α-hydroxy acid), or a copolymer containing these as a main repeating unit element. These resins may be used alone, or two or more kinds may be combined.
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 higher transparency (lower concealment) of the polyester long-fiber nonwoven fabric of the present embodiment is better. Therefore, the lower the content of inorganic particles generally used as a matting agent in the thermoplastic synthetic fiber nonwoven fabric, the better.
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, either synthetic products or natural products can be used without particular limitation. Examples of the inorganic particles include oxide-based ceramics such as aluminum oxide, silicon oxide, titanium oxide, zirconium oxide, magnesium oxide, ceria, yttrium oxide, zinc oxide, and iron oxide; silicon nitride, titanium nitride, and nitride Boron and other nitride-based ceramics; silicon carbide, calcium carbonate, aluminum sulfate, aluminum hydroxide, magnesium hydroxide, potassium titanate, talc, kaolin clay, kaolinite, dickite, translucent olive achondrite, water Kaolin, pyrophyllite, magnificent porphyry, montmorillonite, aluminon bentonite, nontronite, chromite, saponite, zinc bentonite, hectorite, vermiculite, iron aluminum serpentine, sericite, Magnesite, manganese aluminum serpentine, zinc aluminum serpentine, nickel aluminum serpentine, bentonite, zeolite, biotite, phlogopite, iron mica, magnesium rich biotite, conifer mica iron mica, scale mica, silicon rich scale Mica, muscovite, chlorite, magnesium-rich biotite, ferrochlorite, iron aluminum chlorite, calcium silicate, magnesium silicate, diatomaceous earth, silica sand and other ceramic and glass fibers. These inorganic particles are used alone or in combination of two or more. From the viewpoint of the reactivity with the resin, the inorganic particles used are preferably inert inorganic particles such as titanium oxide, magnesium stearate, and 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 size range of the inorganic particles of the polyester resin constituting the polyester long fibers of this embodiment is 1.0 μm or less, preferably 0.8 μm or less, and more preferably 0.7 μm or less. If the particle diameter exceeds 1.0 μm, as a nonwoven fabric, not only the transparency is lowered, but also the spinning stability is deteriorated, so spinning defects such as end breakage also increase.
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 preferable content of the inorganic particles is 0 to 100 ppm, preferably 0 to 50 ppm, and more preferably 0 to 0.1 ppm. By setting the content of the inorganic particles in the fiber within the above range, the transparency of the nonwoven fabric can be sufficiently ensured. Furthermore, when inorganic particles are used as a catalyst, the decomposition reaction of the resin at the time of melt extrusion is suppressed within the above-mentioned range, and spinning defects such as thread 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。 As the inorganic particles used as a matting agent in the polyester resin constituting the polyester long fiber of the present embodiment, it is preferable to use titanium oxide after inactivating the reaction activity in view of being inexpensive and versatile. Titanium particles. When the titanium element is used as the inorganic particle in the polyester resin constituting the polyester long fiber of this embodiment, the preferred content is 0 to 100 ppm, preferably 0 to 50 ppm, and 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 that 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, so that spinning defects such as end 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。 When the polyester long-fiber nonwoven fabric of this embodiment is used as a packaging material, the leakage of the inclusions can be defined by the distribution of pore diameters.
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 pore diameter can be represented by the pore diameter at the point of 10% of the area ratio when the area of each hole in the non-woven image is accumulated from the largest area to the smaller area in sequence, and must be 1000 μm or less. The preferred range is 30 μm or more and 6000 μm or less, the more preferred range is 400 μm or less, and the more preferred range is 300 μm or less, and the most preferred is 250 μm or less. If it is above this range, the seam of the fabric becomes thinner, so the powder leakage of the inclusions cannot be suppressed. On the other hand, if it is below this range, the seam of the fabric becomes thinner, so the transparency of the filter decreases. In addition, the filter suppresses the increase in fluid resistance, so when used as a filter for food, the extraction time increases and 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 2.3% and 10% points when the diameter of the larger diameter is accumulated from the maximum diameter Must be 0μm or more and 500μm or less. The preferred range is 300 μm or less, the more preferred range is 200 μm or less, and the further preferred range is 150 μm or less. In the case of a fabric with a large pore size distribution of the nonwoven fabric, by setting the frequency of the hole with a larger diameter within this range, a nonwoven fabric with excellent powder leakage can be produced. Furthermore, by combining with the above 10% pore size range, the optimal pore size distribution for packaging tea 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。 Furthermore, in the case of holes with the same hole area, the shape preferably has a longer diameter and a shorter diameter like an ellipse compared to a true circle. In the case of packing tea and other contents, it is not a real ball with a smooth surface, so even if it is the same hole area, when there is a hole with a longer diameter and a shorter diameter, it is not easy for the tea to get stuck around the hole leakage. The shape of the relatively large pores contained in the non-woven fabric is particularly important for the leakage of tea etc. The shape of the hole can be expressed by the average value of the long diameter of the hole with a diameter of 2.3% to 10% divided by the average value of the hole with a diameter of 2.3% to 10%. This value is preferably 1.3 or more. Generally, as long as the transparency of the resin is the same, if the transparency is kept while suppressing the leakage of the content, there will be a trade-off relationship. The transparency is the surface area of the fiber contained in the fixed area, that is, the thinner the fiber diameter and the weight per unit area The larger and worse, the leakage of the content is reduced. According to this relationship, one method of ensuring the transparency while suppressing the leakage of the content is to reduce the large pore size contained in the nonwoven fabric, and the other method is to set the shape of the hole to a shape where the content does not easily leak. By using these two methods at the same time, a nonwoven fabric can be obtained that further satisfies both the transparency and the leakage of the content.
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。 In addition to the general circular cross-section, the shape of the polyester long fiber of this embodiment can be selected from any fiber cross-sectional shape such as a hollow cross-section, a core-sheath composite cross-section, a split composite cross-section, and a flat cross-section according to its purpose and application.
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 to form a bag shape such as a tea bag, and it is preferably high in strength during heat sealing processing by a bag making machine. In order to obtain heat sealability with good adhesive strength, fibers containing a low-melting point resin with a melting point of 240 ° C or less are laminated on at least one side of the polyester long-fiber nonwoven fabric and a melting point difference is set, thereby heat-sealing During the sealing process, only the low-melting-point resin component softens or melts and functions as an adhesive, so that a high heat seal 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-mentioned low melting point resin is higher than that of the melting point resin by 30 to 150 ° C, preferably 30 to 100 ° C. Examples of low melting point resins include aromatic dicarboxylic acids such as terephthalic acid, isophthalic acid, phthalic acid, and naphthalene dicarboxylic acid, and ethylene glycol, diethylene glycol, and 1,4-butanedi. Copolymerized polyester resin or aliphatic polyester resin, such as polylactic acid, polymerized by glycols such as alcohol and cyclohexane dimethanol. Furthermore, as the fiber structure, in addition to a single component, a composite fiber structure including two components such as a sheath-core structure or a parallel structure is preferable. For example, the core has a high melting point and the sheath has a low melting point. Specifically, the 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 copolyester or aliphatic polyester. The method of laminating low-melting-point fibers includes, for example, a method of melting the above resin and applying a semi-molten resin or its fibrous material to a non-woven curtain spray method to spray the melted resin from the nozzle and A coating method for applying to a non-woven fabric, or a method of obtaining a laminated non-woven fabric by laminating a high-melting-point fiber web and a low-melting-point fiber web and joining them with a heat roller or the like.
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。 Low-melting-point resin, for example, when an aromatic dicarboxylic acid mainly containing terephthalic acid is used as a component, a second aromatic dicarboxylic acid such as isophthalic acid, phthalic acid, and naphthalene dicarboxylic acid can be copolymerized After use. In this case, the amount of the second aromatic dicarboxylic acid relative to the total aromatic dicarboxylic acid is 0-25%, preferably 0-22%, and more preferably 0-18%. If added in an amount exceeding this range, the crystallinity is lowered, and the molecular alignment formed by extension does not occur, so the spinning stability or the mechanical strength or dimensional stability of the nonwoven fabric is reduced.
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 this embodiment is preferably capable of ultrasonic fusing or heat sealing. The seal strength is preferably 0.1 N / 30 mm or more, and more preferably 0.2 N / 30 mm or more. The heat sealing conditions 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 on 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 commonly used additions can be added within a range that does not hinder the desired effect Ingredients, such as various elastomers, impact modifiers, crystal nucleating agents, coloring inhibitors, antioxidants, heat stabilizers, plasticizers, lubricants, weathering agents, antibacterial agents, colorants, pigments, dyes and other additives .
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 this embodiment can be efficiently produced by the spun bond method. That is, the polyester-based resin is heated and melted and discharged from the spinning head, the obtained spun yarn is cooled using a known cooling device, and is drawn and refined by a suction device such as an air tray (Air Sucker). Then, after the fiber group discharged from the suction device is opened, it is deposited on a conveyor belt to form a net. Then, a local thermocompression bonding device such as a heated embossing roller is used to locally thermally press-bond the web formed on the conveyor belt, 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。 When the spunbond method is used, it is not particularly limited. In order to improve the uniformity of the mesh, for example, a method of charging the fiber using a corona device, etc., as disclosed in Japanese Patent Laid-Open No. 11-131355, or a flat plate shape is used. The airflow control device (see Figure 1) such as the dispersing plate adjusts the velocity distribution of the airflow of the ejection part of the ejector, etc., after the fiber is opened, the net is blown, while suppressing the scattering of the net, an area is on the catching surface. This becomes a better 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 nonwoven fabric obtained by the spunbond method has the characteristics of strong cloth strength and no physical properties such as the shedding of short fibers caused by the damage of the joint, and it has low cost and high productivity, so it is used for hygiene, Civil engineering, construction, agriculture / horticulture, and living materials are widely used.
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 fiber diameter of the polyester long fiber of this embodiment is 13-40 μm, preferably 15-40 μm, more preferably 18-35 μm, and a particularly preferable range is 21-30 μm. If the fiber diameter is 13 μm or more, it can be designed to have sufficient transparency. In addition, if the fiber diameter is less than 40 μm when the fiber cannot fully withstand the tension of the ejector during spinning and less likely to break a part of the fiber, when it is made into a nonwoven fabric and used as a filter for food, the mechanical strength or It is excellent in rigidity, component extractability, transparency, and sealability, 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 this embodiment (that is, the specific surface area m 2 / g of the long-fiber nonwoven fabric × unit weight g / m 2 ) is 1.0 to 3.5 (m 2 / m 2 ), more preferably It is 1.2 ~ 3.0 (m 2 / m 2 ), especially the range is 1.3 ~ 2.7 (m 2 / m 2 ). If the surface area per unit area is 3.5 (m 2 / m 2 ) or less, it can be designed to have sufficient transparency. In addition, if the surface area per unit area is 1.0 or more, a sufficient number of fibers can be obtained when making a nonwoven fabric, so when used as a food filter, it has excellent mechanical strength or rigidity, component extractability, and sealability. Suitable as a filter for food.
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 configuration of the polyester long-fiber nonwoven fabric of this embodiment is not particularly limited as long as it is a method of forming a nonwoven fabric through thermal / chemical integration, and it may be a laminated nonwoven fabric. In this case, it is preferable to set the layer structure to distinguish the roles assumed by the layers. For example, the first layer is a layer with high heat seal strength, and the other layer is a layer with excellent mechanical strength such as tensile strength, rigidity, and dimensional stability, which can be used to make the seal required for bag making Non-woven fabric with excellent characteristics and excellent mechanical properties. In addition, in the step of making the non-woven fabric into a bag shape, if a non-woven fabric with a structure of only one layer having both mechanical strength and sealing characteristics is used, in the step of manufacturing the bag by heat bonding, the high temperature The heating and pressure bonding process is carried out under the condition that the thermoplastic resin melts and adheres to the hot roller or hot plate heater of the bag-making equipment, which leads to a reduction in product quality or a reduction in processing speed. . On the other hand, if it is the nonwoven fabric structure of this embodiment, by arranging the sealing layer on the inner surface, good sealing strength can be exhibited, and production can be performed without reducing 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。 When the laminated non-woven fabric is used as the polyester long-fiber non-woven fabric of this embodiment, the structure of the layer that bears the sealing property can be a single fiber structure or a sheath core structure or a parallel structure, split cutting, etc. The composite fiber structure containing two kinds of components, such as fiber, is preferably a structure in which a low-melting-point resin that bears sealing performance is disposed on the surface of the fiber. For example, the core is a composite fiber structure with a high melting point and the sheath is a low melting point. Specifically, the core is made of a high melting point resin such as polyethylene terephthalate or polybutylene terephthalate and the sheath is a copolymer. Ester or fat Nonwoven fabric of sheath core structure composed of aliphatic polyester and other low melting point resins.
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 of producing the layer that bears mechanical strength is not particularly limited, and from the viewpoint of productivity, the spunbond 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。 Especially when the laminated non-woven fabric is used as the polyester long-fiber non-woven fabric of the present embodiment, the production method and physical properties of the layer that bears mechanical strength can be made dimensionally stable and mechanically strong by using the above method for production 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。 When the laminated non-woven fabric is used as the polyester long-fiber non-woven fabric of this embodiment, the pressure bonding method is not particularly limited as long as the fibers are integrated with each other to make the non-woven fabric, and it is preferable to laminate each layer After that, they are thermo-compression-bonded with a hot roller or the like to make a non-woven fabric. By thermocompression bonding each layer after lamination, the bonding strength between the layers can be made stronger, so that the mechanical strength or sealing performance can be more effectively reflected.
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 setting the layer structure of the laminated nonwoven fabric in the present embodiment to the layered structure as described above, the seal strength can be set to a more preferable range. As a specific sealing strength, it 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。 In addition, the mechanical strength, that is, the tensile strength may be set to a more preferable range, and the range is 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 this embodiment is not particularly limited as long as it is a method of crimping the filaments of the nonwoven fabric with heat, and the nonwoven fabric may be passed through a surface structure having irregularities A pair of embossing rollers and smoothing rollers is heated between the heating rollers to form a thermocompression-bonded portion that is evenly distributed over the entire nonwoven fabric and is preferably performed. When using embossing rollers for thermal compression bonding, it is preferable to perform thermal compression bonding at a thermal compression bonding area ratio in the range of 5-40% relative to the total area of the nonwoven fabric, more preferably 7-30%. Furthermore, it is preferably 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 area of thermocompression bonding is within this range, good thermocompression bonding between fibers can be performed to achieve moderate mechanical strength or rigidity, transparency, component extraction, and dimensional stability of the obtained nonwoven fabric The aspect is better. The temperature and pressure of the thermocompression bonding process should be appropriately selected according to the conditions such as the weight per unit area and the speed of the supplied net, and are not generalized. It is preferably a temperature lower than the melting point of the polyester resin by 10 to 90 ° C, and more preferably lower 20 ~ 60 ℃ temperature.
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 above-mentioned thermocompression bonding step, in addition to using an embossing roller, an air blowing method in which the filaments are crimped with heat by passing hot air through a net can also be used. In the case of thermocompression bonding by the air blowing method, since there is no local unevenness like the embossed shape on the surface of the fabric, the appearance of the nonwoven 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 of the polyester long-fiber nonwoven fabric of the present embodiment is preferably 2.0% or less, more preferably 1.6% or less, and further preferably 1.0%, and a particularly preferable range is 0.5% or less. If the shrinkage of boiling water is 2.0% or less, there is almost no shrinkage in thermoforming, etc., and the step stability is excellent. Even in the form of use such as exposure to high temperatures near 100 ° C, the shape retention Excellent. The lower limit is preferably 0%, 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 this embodiment is preferably 60% or more, more preferably 65% or more, and still more preferably 70% or more. If the transparency is less than 60%, it is difficult to see the content through the non-woven fabric and become 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 weight per unit area of the polyester long fiber nonwoven fabric of this embodiment is 10 to 30 g / m 2 , preferably 12 to 25 g / m 2 . If the weight per unit area is 10 g / m 2 or more, the transparency and component extractability can be maintained, and the mechanical strength can be sufficiently ensured. On the other hand, if the weight per unit area 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 this embodiment is preferably 0.02 to 0.50 mm, and more preferably 0.03 to 0.30 mm. When the weight per unit area and the thickness are within this range, excellent transparency, mechanical strength, and component extractability when used as a filter for food 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 this embodiment is preferably 0.10 to 0.50 g / cm 3 , and more preferably 0.12 to 0.30 g / cm 3 . The average apparent density is related to the rigidity, transparency, powder leakage and component extractability of the non-woven fabric. If it is within the above range, the fiber gap is moderate, so it is suitable as a food filter. If 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 also be sufficient. On the other hand, if the average apparent density is 0.50 g / cm 3 or less, the fiber gap is not too small, the component extractability can be appropriately maintained, and the product quality can be 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 MD (Machine Direction, MD) direction tensile strength of the polyester long fiber nonwoven fabric of the present embodiment is preferably 5-40N / 30mm, more preferably 6-40N / 30mm, and further preferably 7-40N / 30mm. If the tensile strength is above this range, the production stability at the time of bag-making processing or the prevention of breakage when used as a food filter is excellent.
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 this embodiment is preferably 0.5 to 2.0, and more preferably 0.5 to 1.5. The texture coefficient indicates the uniformity of the non-woven fabric, so it is related to the strength, rigidity, transparency, powder leakage and component extractability. Within the above range, the uniformity of the non-woven fabric is the best, so it has excellent strength, rigidity, transparency, adaptability to a bag shape, and powder leakage 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 when obtaining the polyester long fiber of the present embodiment is preferably a temperature higher than the melting point of the polyester resin by 10 to 60 ° C, and more preferably a temperature higher by 10 to 30 ° C. If the spinning temperature is within this range, monofilament breakage and the like will not occur, and the orientation crystallinity is moderate, so that 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 this embodiment is made into a nonwoven fabric is preferably 0.6 or more, more preferably 0.65 or more, and still more preferably 0.7 or more. When the resin pellets are melt-extruded, the resin will decompose due to heat load during melting or shear load during kneading. If the IV value of the resin after melting, that is, after being made into a non-woven fabric is above this range, the decomposition of the resin can be better suppressed and the extension and crystallization of the resin during spinning can be promoted, so the mechanical strength, 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 when obtaining the polyester long fiber of the present embodiment is preferably 3000 to 6000 m / min, more preferably 3500 to 5000 m / min. If the drawing speed of the spun yarn is refined within the above range, the orientation crystallization of the polyester long fiber is sufficient to obtain a nonwoven fabric with excellent mechanical properties or dimensional stability, and breakage occurs during spinning There is less possibility, and it is better in terms of 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。 When the polyester long fiber of the present embodiment is obtained, the stretching is preferably 400 to 2500, and more preferably 700 to 2200. If the draw ratio of the spun yarn is refined within the above range, the orientation crystallization of the polyester long fiber is sufficient to obtain a nonwoven fabric with excellent mechanical properties or dimensional stability, and breakage occurs during spinning Or the possibility of "winding around the roller" during thermocompression bonding is low, so it is also preferable in terms of productivity of nonwoven fabrics.
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 fiber of this embodiment is 0.04 to 0.12, preferably 0.06 to 0.1. If the birefringence is in this range, the alignment of the fiber 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 crystallinity measurement based on DSC (Differential scanning calorimetry) or 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 crystallinity of the polyester long fiber of this embodiment is 30-50%, preferably 40-50%. If the crystallinity is within this range, fibers with excellent 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 this embodiment is implemented by Raman spectroscopy, the peak generated by the C = O group near 1740 cm -1 observed in the Raman spectrum of the fiber profile can be used The average value of the full amplitude at half maximum of the width is evaluated. The average value of the half-peak amplitude of the peak width is 18 ~ 24cm -1 , preferably 19 ~ 24cm -1 , and the more preferable range is 20 ~ 23cm -1 . If the average value of the full width at half maximum of the peak width is within this range, a fiber with excellent 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 this embodiment can crystallize differently in the radial direction of the fiber For example, the crystallinity of the outer periphery is higher, and the crystallinity of the interior is lower. By making the crystallinity of the outer peripheral part higher, it is possible to make fibers that are less likely to shrink and have excellent mechanical strength, and by making the internal crystallinity low, the crimping strength of the fibers can be sufficiently obtained during thermocompression bonding. As a result, a nonwoven fabric excellent in mechanical strength and dimensional stability can be produced. This case can be confirmed by evaluating the melting peak when measuring the crystallinity 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 and transparency of the polyester long-fiber nonwoven fabric in the embodiment of the present invention. If the fiber diameter is increased, the transparency can be increased, but alignment crystallization is not easy, so the shrinkage of boiling water becomes larger and the dimensional stability decreases.
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。 3 and 4 respectively show the relationship between the draw ratio and spinning temperature of the polyester long fiber nonwoven fabric and the alignment crystallinity expressed by the birefringence (Δn) and crystallinity in the examples of the present invention. The greater the draw ratio, the more the orientation crystallinity of the fiber increases. In addition, under the spinning conditions of the thick fiber diameter, the lower the spinning temperature, the higher the cooling performance, thereby increasing the elongation efficiency, and aligning and crystallizing the fibers.
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 and the alignment crystallinity expressed by the birefringence (Δn) and crystallinity in the embodiment of the present invention. By increasing the IV value of the resin, the orientation crystallization of the resin can be promoted, so that the orientation crystallization of the fiber 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。 Based on these data, and diligent research was conducted in such a way as to exert the effects required by the present invention, as a result, the inventors of the present invention used the lowering of the spinning temperature and the expansion of the draw ratio to maintain the diameter of the coarse fiber and improve the alignment crystal To improve transparency and boiling water shrinkage at the same time. That is, the improvement in transparency in the nonwoven fabric is inversely related to the improvement in dimensional stability indicated by the shrinkage rate of boiling water, but the inventors of the present invention set the optimal range of the diameter of the coarse fiber and the alignment crystallinity of the fiber At the same time, it improves 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。 Furthermore, by optimizing the intrinsic viscosity (IV value) of the resin used in the present invention, an optimal range of alignment crystallization can also be achieved. The range of IV values used for cost purposes is 0.7 The above is preferably 0.85 or less, and more preferably 0.72 to 0.8. If the inherent viscosity is within this range, monofilament breakage and the like will not occur and stable productivity can be ensured, and higher alignment crystallinity can be obtained when the molten resin is drawn and refined, thereby obtaining higher 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 but sinks quickly when placed in hot water. The hydrophilic agent is preferably used as a surfactant for food, 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. As the coating method, known methods such as a gravure roll method, a touch roll method, a dipping method, and a spray method can be applied.
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 this embodiment can also be subjected to common post-processing, such as deodorant, antibacterial agent, etc., dyeing, water repellent processing, water permeable processing can also be performed within the range that does not impair 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。 The polyester long-fiber nonwoven fabric of the present embodiment has excellent transparency, so the contents can be clearly seen, so it has excellent designability, and because of its excellent dimensional stability, it has a filter suitable for foods such as green tea, black tea, coffee, etc. The characteristics. The filter for food may be a flat bag, but if it has a three-dimensional shape, the contents can be seen more clearly and extraction can be performed 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 of the food filter is filled with the extract and sealed and put into a bag for sale. However, it is required that the purchased consumer quickly restore the original three-dimensional shape when taken out of the bag and use it. The long-fiber non-woven fabric of the present invention has elasticity and thus has moderate rigidity, so it can fully meet the above-mentioned requirements.
[實施例] [Example]
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。 The present invention will be specifically described below using examples, but the present invention is not limited to these. In addition, the measurement method and evaluation method 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 ICP (Inductively Coupled Plasma, Inductively Coupled Plasma) luminescence analyzer manufactured by Thermo Fisher Scientific was used to determine the titanium content in the polyester resin.
(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 by 1000 times using a Microscope microscope (VH-8000) manufactured by KEYENCE Corporation, and the average fiber diameter was determined using the average value of each 20.
(3)雙折射率(△n) (3) Birefringence (△ n)
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 of the BH2 polarizing microscope manufactured by OLYMPUS is used to compensate the pressure, and the birefringence of the fiber immediately after the traction is determined according to the retardation and fiber diameter using the usual interference fringe method.
(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 The differential scanning calorimeter DSC6000 manufactured by PerkinElmer was used to measure the calorific value △ Hc and the crystal melting amount △ Hm after the temperature was increased from 40 ° C to 300 ° C at a heating rate of 10 ° C / min. The crystallinity (%) is determined according to the following formula: Crystallinity χc (%) = (△ Hm- △ Hc) /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。 * 126.4J / g is the heat of fusion for the complete crystallization of polyethylene terephthalate.
(5)半峰全幅值(cm-1) (5) Full amplitude at half peak (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 with the excitation light of 532 nm and the excitation light intensity of 10% using a microscope Raman spectroscopic device manufactured by Renishaw. Find the half-peak full amplitude of the peak width generated by the C = O base around 1740 cm -1 observed in the spectrum.
(6)固有黏度(IV值) (6) Intrinsic viscosity (IV value)
依據JIS K-7367-5進行測定。 Measured according to JIS K-7367-5.
(7)單位面積重量(g/m2) (7) Weight per unit area (g / m 2 )
依據JIS L-1906進行測定。 Measured according to 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 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) Determine the mass per unit volume based on the weight per unit area and thickness measured by the method specified in JIS L-1906: average apparent density (g / cm 3 ) = (weight per unit area g / m 2 ) / ((thickness mm ) × 1000)
(10)熱壓接面積率(%) (10) Thermal compression 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 with an electron microscope, and the area of the thermocompression-bonded part was measured from each photo, and the average value was used as the area of the thermocompression-bonded part. In addition, the distance between the patterns of the thermocompression bonding part in the MD direction and CD (cross direction) direction is measured, and the ratio of the thermocompression bonding area to the unit area of the nonwoven fabric is calculated based on these values as the thermocompression bonding area ratio .
(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 Measure the reflectance (L value) using a Macbeth spectrophotometer (CE-7000A model: manufactured by Sakata Inx Corporation) to find the difference between the L value of the standard whiteboard (L w0 ) and the L value of the standard blackboard (L b0 ) As a reference, based on the L value (L w ) of the sample placed on the whiteboard and the L value (L b ) placed on the blackboard in the same way, the transparency is calculated 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 (%)
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 specimens with a length of 25 cm and a width of 25 cm were taken on a sample with a width of 1 m, which was immersed in boiling water for 3 minutes, and the shrinkage in the MD and CD directions was obtained after natural drying . The average value of each is calculated, and the shrinkage rate of the larger one of the MD direction and the CD direction is taken as the boiling water shrinkage rate 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 Auto Stereograph AGS-5G manufactured by Shimadzu Corporation, a 30mm wide sample is extended with a grip length of 100mm and a tensile speed of 300mm / min, and the load at break obtained is used as the strength. Make 5 measurements in the MD direction and find Its average.
(14)質地係數 (14) Texture factor
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。 Take a 20cm × 30cm test piece, use Nomura Corporation ’s Formation Tester (FMT-MIII) measuring device, and decompose the transmission image obtained by shooting a range of 18cm × 25cm with a CCD (Charge Coupled Device) camera For 128 × 128 pixels, measure the intensity of light received by each pixel and calculate the transmittance. The texture coefficient is the value obtained by dividing the standard deviation (σ) of the transmittance of each minute part (5mm × 5mm) of the measured sample by the average transmittance (E), which represents the deviation of the unit weight per unit area. The higher the uniformity.
質地係數=σ/E×100 Texture factor = σ / E × 100
(15)熱密封強度(N/30mm) (15) Heat seal 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 manufactured by Shimadzu Corporation, the heat-sealed part of the 30mm wide sample is peeled up and down by about 50mm, and then installed, and it is stretched by holding the length of 50mm and the stretching speed of 100mm / min Take the obtained load at break as the strength, and measure the MD direction of the non-woven fabric 5 times to determine the average value. 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) Stretching 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) Calculate the draw ratio according to the following formula: draw ratio = spinning speed (m / min) / ejection linear 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} Linear ejection speed (m / min) = single-hole ejection amount (g / min) / {melt density (g / cm 3 ) × [spin nozzle diameter (cm) / 2] 2 × π}
*聚酯之熔融密度:使用1.20g/cm3 * Melt density of polyester: use 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 non-woven 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 is determined from the specific surface area m 2 / g of the long-fiber nonwoven fabric × the weight per unit area g / m 2 .
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 non-woven fabric was obtained by using Gemini 2360, an automatic specific surface area measuring machine of Shimadzu Corporation. In addition, when the specific surface area is less than 0.1 m 2 / g, it is determined 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 two or more fiber diameter sheets, 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 pieces of 2 cm square samples were cut out from one sample, and platinum sputtering was performed using an ion sputtering device for SEM (scanning electron microscope) observation, and the test was conducted at a magnification of 100 times using transmitted light 10 nonwoven images in the sample were taken. The image analysis software is used to binarize the non-woven part into black, and the hole part into white, and to quantify the area and longest diameter of all holes in the image. The image analysis soft system uses "A Xiangjun (TM)" manufactured by Asahi Kasei Engineering. Accumulate all holes in a sample image from the largest area to a smaller area in sequence, according to the hole area that reaches the point of 10% of the total hole area, as the diameter of the circle with the area equal to the area by the following The formula calculates the aperture.
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 hole area (μm ^ 2), and " ^ 0.5" means "multiply 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-mentioned 10% pore size, the pore size is obtained from the pore area that reaches the point of 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。 Accumulate all the holes in a sample image from the largest area to the smaller area in sequence, and find the long diameter of all the holes included between the holes that reach 2.3% of the total hole area and the holes that reach 10% The average value and the average value of the pore diameter are 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 long diameter / average diameter
[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 with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a commonly used melt spinning device and melted at 275 ° C, 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 polyester long fibers with a fiber diameter of 20.5 μm. Then, a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °] was used to disperse the fibers to produce a mesh with a weight per unit area of 12 g / m 2 . During the local thermal compression bonding at a thermal compression bonding area rate of 15%, a polyester long fiber nonwoven fabric was obtained. The physical properties of the obtained nonwoven fabric are shown in Table 1 below.
[實施例2] [Example 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 Example 1, a polyester long fiber nonwoven fabric was obtained in the same manner as in Example 1, except that the polyester long fiber was spun so that the fiber diameter became 25.7 μm. The physical properties of the obtained nonwoven 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。 In Example 1, a polyester long fiber nonwoven fabric was obtained in the same manner as in Example 1 except that the polyester long fiber was spun so that the fiber diameter became 30.0 μm. The physical properties of the obtained nonwoven 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。 In Example 3, except that the resin having an IV value of 0.8 and a titanium oxide content of 12 ppm was used, a polyester long fiber nonwoven fabric was obtained in the same manner as in Example 3. The physical properties of the obtained nonwoven 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。 In Example 3, except that the resin having an IV value of 0.8 and a titanium oxide content of 70 ppm was used, a polyester long fiber nonwoven fabric was obtained in the same manner as in Example 3. The physical properties of the obtained nonwoven fabric are shown in Table 1 below.
[實施例6] [Example 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。 Except that the resin having an IV value of 0.72 and a titanium oxide content of 0 ppm was used in Example 3, a polyester long fiber nonwoven fabric was obtained in the same manner as in Example 3. The physical properties of the obtained nonwoven fabric are shown in Table 1 below.
[實施例7] [Example 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。 Except that the resin having an IV value of 0.77 and a titanium oxide content of 0 ppm was used in Example 3, a polyester long fiber nonwoven fabric was obtained in the same manner as in Example 3. The physical properties of the obtained nonwoven fabric are shown in Table 1 below.
[實施例8] [Example 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。 In Example 3, the polyester long-fiber nonwoven fabric was spun so that the basis weight of the polyester long-fiber nonwoven fabric was 20 g / m 2 , except that the polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 3. The physical properties of the obtained nonwoven fabric are shown in Table 1 below.
[實施例9] [Example 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 Example 1, melt spinning was carried out at a spinning speed of 3770 m / min and a draw ratio of 707, and spinning was carried out in such a way that the fiber diameter of the polyester long fiber became 34.9 μm, except that it was the same as Example 1. Way to obtain polyester long fiber non-woven fabric. The physical properties of the obtained nonwoven fabric are shown in Table 1 below.
[實施例10] [Example 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 Example 2, it was spun in such a way that the weight per unit area of the polyester long-fiber nonwoven fabric became 20 g / m 2 , and the entire surface was thermally pressure-bonded with a smooth roll, except that it was obtained in the same manner as in Example 2. Polyester long fiber non-woven fabric. The physical properties of the obtained nonwoven 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 with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a commonly used melt spinning device and melted at 275 ° C, from a spinning hole with 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 polyester long fibers with a fiber diameter of 30.1 μm. Then, a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °] was used to disperse the fibers to produce a net with a basis weight of 20 g / m 2 , which was applied to the embossing roll and smoothing roll. During the local thermal compression bonding at a thermal compression bonding area rate of 5%, polyester long fiber nonwoven fabric was obtained. The physical properties of the obtained nonwoven fabric are shown in Table 1 below.
[實施例12] [Example 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 with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a commonly used melt spinning device and melted at 275 ° C, from a spinning hole with 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 polyester long fibers with a fiber diameter of 30.0 μm. Then, the fibers were opened and dispersed to produce a web with a weight per unit area of 12 g / m 2 , and a local thermocompression bonding was performed between the embossing roll and the smoothing roll at a thermal compression bonding area ratio of 15% to obtain polyester long fibers Non-woven. The physical properties of the obtained nonwoven 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 with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a commonly used melt spinning device and melted at 275 ° C, from a spinning hole with a circular cross section The spinning head is melt-spun at a spinning speed of 4000 m / min and a draw ratio of 942, using a flat-plate-shaped dispersion device that controls airflow [the inclination angle of the flat plate with respect to the filament is 4 °] so that the fiber diameter is 26.7 μm Polyester long fibers are opened and dispersed to produce a net with a basis weight of 18 g / m 2 . Then, a polyester resin with 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 device and melted at 275 ° C, from a spinning hole having a circular cross section The spinning head is melt-spun at a spinning speed of 4150 m / min and a draw ratio of 412 and uses a flat-plate-shaped dispersion device that controls the air flow [the inclination angle of the flat plate with respect to the filament is 4 °] so that the fiber diameter is 15 μm The long polyester fibers are spread and dispersed to produce a net having a basis weight of 3 g / m 2 . The two-layer web was locally thermally pressure-bonded between the embossing roller and the smoothing roller at a thermal compression bonding area ratio of 15%, thereby obtaining a polyester long-fiber nonwoven fabric. The physical properties of the obtained nonwoven fabric are shown in Table 1 below.
[實施例14] [Example 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 with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a commonly used melt spinning device and melted at 275 ° C, from a spinning hole with a circular cross section The spinning head is melt-spun at a spinning speed of 4000 m / min and a draw ratio of 942, using a flat-plate-shaped dispersion device that controls the air flow [the inclination angle of the flat plate with respect to the filament is 4 °] so that the fiber diameter is 24.6 μm The polyester long fibers are spread and dispersed to produce a net having a basis weight of 10 g / m 2 . Next, a polyester resin with a titanium content of 12 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as the core, and a polymer with a titanium content of 12 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C The ester-based resin is supplied as a sheath to a conventional melt spinning device and melted at 275 ° C, and melt spinning is performed at a spinning speed of 4500 m / min and a draw ratio of 895 from a spinning head having a spinning hole with a circular cross section Using a flat-plate-shaped dispersing device for controlling airflow [the inclination angle of the flat plate with respect to the filament is 4 °], the polyester filaments with a fiber diameter of 20 μm are opened and dispersed to produce a net with a weight per unit area of 8 g / m 2 . The two-layer web was locally thermally pressure-bonded between the embossing roller and the smoothing roller at a thermal compression bonding area ratio of 15%, thereby obtaining a polyester long-fiber nonwoven fabric. The physical properties of the obtained nonwoven 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。 In Example 1, the polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 1 except that the polyester long-fiber nonwoven fabric had a spinning basis weight of 18 g / m 2 . The physical properties of the obtained nonwoven 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。 In Example 2, the 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 . The physical properties of the obtained nonwoven 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。 In Example 3, the polyester long-fiber non-woven fabric was obtained in the same manner as in Example 1 except that the polyester long-fiber non-woven fabric had a spinning basis weight of 18 g / m 2 . The physical properties of the obtained nonwoven fabric are shown in Table 1 below.
[實施例18] [Example 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 Example 1, the first layer of non-woven fabric was prepared such that the weight per unit area of the polyester long-fiber non-woven fabric became 18 g / m 2 . PET (polyethylene terephthalate) resin with an IV value of 0.65, a titanium content of 0 ppm, and a melting point of 217 ° C was used at a spinning temperature of 260 ° C and heated air of 500 Nm 3 / hr / m. After spinning, the obtained meltblown nonwoven fabric with a fiber diameter of 10 μm was blown onto the spunbond nonwoven fabric at a basis weight of 5 g / m 2 to obtain a laminate of nonwoven fabric. The physical properties of the obtained nonwoven fabric are shown in Table 1 below.
[實施例19] [Example 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, the first layer of non-woven fabric was prepared so that the weight per unit area of the polyester long-fiber non-woven fabric became 18 g / m 2 . A PET resin with 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 heated air of 400 Nm 3 / hr / m, and the resulting fiber was melted at a diameter of 15 μm. The sprayed nonwoven fabric was blown onto the above spunbond nonwoven fabric at a basis weight of 4 g / m 2 to obtain a laminate of nonwoven fabric. The physical properties of the obtained nonwoven 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, the first layer of non-woven fabric was prepared such that the weight per unit area of the polyester long-fiber non-woven fabric became 18 g / m 2 . A PET resin with 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 heated air of 1000 Nm 3 / hr / m, and the resulting fiber was melted at a diameter of 7 μm The sprayed nonwoven fabric was blown onto the above spunbond nonwoven fabric at a basis weight of 4 g / m 2 to obtain a laminate of nonwoven fabric. The physical properties of the obtained nonwoven 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 with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a commonly used melt spinning device and melted at 275 ° C, from a spinning hole with 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 polyester long fibers with a fiber diameter of 14 μm. Then, a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °] was used to spread and spread the fibers to prepare a net with a weight per unit area of 7.5 g / m 2 . Then, a polyester resin with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as the core, and a polymer with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C The ester-based resin is supplied as a sheath to a conventional melt spinning device and melted at 275 ° C, and melt spinning is performed at a spinning speed of 4500 m / min and a draw ratio of 380 from a spinning head having a spinning hole with a circular cross section Using a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °], a polyester filament with a fiber diameter of 14 μm is opened and dispersed to produce a net with a weight per unit area of 7.5 g / m 2 . The two-layer web was locally thermally pressure-bonded between the embossing roller and the smoothing roller at a thermal compression bonding area ratio of 15%, thereby obtaining a polyester long-fiber nonwoven fabric. The physical properties of the obtained nonwoven 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 with a titanium content of 12 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a commonly used melt spinning device and melted at 275 ° C, from a spinning hole with 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 polyester long fibers with a fiber diameter of 20.1 μm. Then, a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °] was used to spread and spread the fibers to prepare a net with a weight per unit area of 7.5 g / m 2 . Then, a polyester resin with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as the core, and a polymer with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C The ester-based resin is supplied as a sheath to a conventional melt spinning device and melted at 275 ° C, and melt spinning is performed at a spinning speed of 4500 m / min and a draw ratio of 380 from a spinning head having a spinning hole with a circular cross section Using a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °], a polyester filament with a fiber diameter of 14 μm is opened and dispersed to produce a net with a weight per unit area of 7.5 g / m 2 . The two-layer web was locally thermally pressure-bonded between the embossing roller and the smoothing roller at a thermal compression bonding area ratio of 15%, thereby obtaining a polyester long-fiber nonwoven fabric. The physical properties of the obtained nonwoven 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 with a titanium content of 12 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a commonly used melt spinning device and melted at 275 ° C, from a spinning hole with 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 polyester long fibers with a fiber diameter of 24.6 μm. Then, a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °] was used to spread and spread the fibers to prepare a net with a weight per unit area of 7.5 g / m 2 . Then, a polyester resin with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as the core, and a polymer with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C The ester-based resin is supplied as a sheath to a conventional melt spinning device and melted at 275 ° C, and melt spinning is performed at a spinning speed of 4500 m / min and a draw ratio of 380 from a spinning head having a spinning hole with a circular cross section Using a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °], a polyester filament with a fiber diameter of 14 μm is opened and dispersed to produce a net with a weight per unit area of 7.5 g / m 2 . The two-layer web was locally thermally pressure-bonded between the embossing roller and the smoothing roller at a thermal compression bonding area ratio of 15%, thereby obtaining a polyester long-fiber nonwoven fabric. The physical properties of the obtained nonwoven 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 with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a commonly used melt spinning device and melted at 275 ° C, and is spun from a spinning hole having a circular cross section The yarn end was melt-spun at a spinning speed of 4500 m / min and a draw ratio of 550 to obtain polyester long fibers with a fiber diameter of 20.1 μm. Next, a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °] was used to spread and spread the fibers to produce a net having a basis weight of 10 g / m 2 . Then, a polyester resin with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as the core, and a polymer with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C The ester resin is supplied as a sheath to a commonly used melt spinning device and melted at 275 ° C, and melt spinning is performed at a spinning speed of 4500 m / min and a draw ratio of 450 from a spinning head having a spinning hole with a circular cross section The filament was used to disperse a flat airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °] to disperse the polyester filament with a fiber diameter of 16 μm to produce a net with a weight per unit area of 5 g / m 2 . The two-layer web was locally thermally pressure-bonded between the embossing roller and the smoothing roller at a thermal compression bonding area ratio of 15%, thereby obtaining a polyester long-fiber nonwoven fabric. The physical properties of the obtained nonwoven 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 with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a commonly used melt spinning device and melted at 275 ° C, and is spun from a spinning hole having a circular cross section The yarn end was melt-spun at a spinning speed of 4500 m / min and a draw ratio of 590 to obtain polyester long fibers with a fiber diameter of 20.1 μm. Then, a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °] was used to spread and spread the fibers to prepare a net with a weight per unit area of 7.5 g / m 2 . Then, a polyester resin with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as the core, and a polymer with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C The ester resin is supplied as a sheath to a commonly used melt spinning device and melted at 275 ° C, and melt spinning is performed at a spinning speed of 4500 m / min and a draw ratio of 450 from a spinning head having a spinning hole with a circular cross section Using a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °], the polyester filaments with a fiber diameter of 16 μm are opened and dispersed to produce a net with a weight per unit area of 7.5 g / m 2 . The two-layer web was locally thermally pressure-bonded between the embossing roller and the smoothing roller at a thermal compression bonding area ratio of 15%, thereby obtaining a polyester long-fiber nonwoven fabric. The physical properties of the obtained nonwoven 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 with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a commonly used melt spinning device and melted at 275 ° C, and is spun from a spinning hole having a circular cross section The yarn end was melt-spun at a spinning speed of 4500 m / min and a draw ratio of 740 to obtain polyester long fibers with a fiber diameter of 24.6 μm. Then, a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °] was used to spread and spread the fibers to prepare a net with a weight per unit area of 7.5 g / m 2 . Then, a polyester resin with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as the core, and a polymer with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C The ester resin is supplied as a sheath to a commonly used melt spinning device and melted at 275 ° C, and melt spinning is performed at a spinning speed of 4500 m / min and a draw ratio of 450 from a spinning head having a spinning hole with a circular cross section Using a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °], the polyester filaments with a fiber diameter of 16 μm are opened and dispersed to produce a net with a weight per unit area of 7.5 g / m 2 . The two-layer web was locally thermally pressure-bonded between the embossing roller and the smoothing roller at a thermal compression bonding area ratio of 15%, thereby obtaining a polyester long-fiber nonwoven fabric. The physical properties of the obtained nonwoven 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 with a titanium content of 12 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a commonly used melt spinning device and melted at 275 ° C, from a spinning hole with 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 polyester long fibers with a fiber diameter of 20.1 μm. Then, a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament 0 °] was used to spread and spread the fibers to produce a net with a weight per unit area of 7.5 g / m 2 . Then, a polyester resin with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as the core, and a polymer with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C The ester resin is supplied as a sheath to a commonly used melt spinning device and melted at 275 ° C, and melt spinning is performed at a spinning speed of 4500 m / min and a draw ratio of 450 from a spinning head having a spinning hole with a circular cross section Using a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 0 °], polyester filaments with a fiber diameter of 16 μm are opened and dispersed to produce a net with a weight per unit area of 7.5 g / m 2 . The two-layer web was locally thermally pressure-bonded between the embossing roller and the smoothing roller at a thermal compression bonding area ratio of 15%, thereby obtaining a polyester long-fiber nonwoven fabric. The physical properties of the obtained nonwoven 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。 Except that the inclination angle of the flat plate of the airflow-controlling dispersion device with respect to the filament was set to 0 °, the polyester filament nonwoven fabric was obtained by the same method as in Example 22. The physical properties of the obtained nonwoven 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。 Except that the self-sheath core structure using a low-melting-point resin is a side-by-side structure, a polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 21. The physical properties of the obtained nonwoven 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 layered self-sheathed core structure using a low-melting-point resin was used as a side-by-side structure, and a polyester long fiber nonwoven fabric was obtained in the same manner as in Example 24. The physical properties of the obtained nonwoven 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。 Except that the self-sheath core structure of the layer using a low-melting-point resin is a side-by-side structure, a polyester long fiber nonwoven fabric was obtained by the same method as in Example 22. The physical properties of the obtained nonwoven 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。 Except that the weight per unit area of each layer was 6 g / m 2 , a polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 21. The physical properties of the obtained nonwoven 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。 Except that the weight per unit area of each layer was 6 g / m 2 , a polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 22. The physical properties of the obtained nonwoven 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。 Except that the weight per unit area of each layer was 6 g / m 2 , a polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 23. The physical properties of the obtained nonwoven 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 with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a commonly used melt spinning device and melted at 275 ° C, and is spun from a spinning hole having a circular cross section The yarn end was melt-spun at a spinning speed of 4500 m / min and a draw ratio of 590 to obtain polyester long fibers with a fiber diameter of 20.1 μm. Then, a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °] was used to spread and spread the fibers to produce a net having a basis weight of 12 g / m 2 . Then, a polyester resin with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as the core, and a polymer with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C The ester resin is supplied as a sheath to a commonly used melt spinning device and melted at 275 ° C, and melt spinning is performed at a spinning speed of 4500 m / min and a draw ratio of 450 from a spinning head having a spinning hole with a circular cross section The filament was used to disperse a flat airflow-controlling dispersion device [the inclination angle of the flat plate with respect to the filament is 4 °] to disperse the polyester long fibers with a fiber diameter of 16 μm to produce a net weight of 6 g / m 2 . The two-layer web was locally thermally pressure-bonded between the embossing roller and the smoothing roller at a thermal compression bonding area ratio of 15%, thereby obtaining a polyester long-fiber nonwoven fabric. The physical properties of the obtained nonwoven 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。 The weight per unit area of each layer was set to 9 g / m 2 , except that the polyester long fiber nonwoven fabric was obtained in the same manner as in Example 25. The physical properties of the obtained nonwoven 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。 Except having set the weight per unit area of each layer to 9 g / m 2 , a polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 21. The physical properties of the obtained nonwoven 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 with a titanium content of 12 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 247 ° C is supplied to a commonly used melt spinning device 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 polyester long fibers with a fiber diameter of 10 μm. Then, a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °] was used to spread and spread the fibers to prepare a net with a weight per unit area of 7.5 g / m 2 . Then, a polyester resin with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 254 ° C was used as the core, and a polymer with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65, and a melting point of 217 ° C The ester-based resin is supplied as a sheath to a conventional melt spinning device and melted at 275 ° C, and melt spinning is performed at a spinning speed of 4500 m / min and a draw ratio of 380 from a spinning head having a spinning hole with a circular cross section Using a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °], a polyester filament with a fiber diameter of 14 μm is opened and dispersed to produce a net with a weight per unit area of 7.5 g / m 2 . The two-layer web was locally thermally pressure-bonded between the embossing roller and the smoothing roller at a thermal compression bonding area ratio of 15%, thereby obtaining a polyester long-fiber nonwoven fabric. The physical properties of the obtained nonwoven 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。 Except that the fiber diameter of each layer was 13 μm, a polyester long fiber nonwoven fabric was obtained in the same manner as in Example 32. The physical properties of the obtained nonwoven 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 Example 1, the content of the titanium element of the polyester-based resin was set to 3000 ppm, and spinning was carried out so that the weight per unit area of the polyester long fiber became 20.0 g / m 2 , except that it was the same as Example 1. The polyester long fiber nonwoven fabric is obtained by this method, but the transparency of the nonwoven fabric is low, and sufficient transparency cannot be obtained as a filter for food. The physical properties of the obtained nonwoven 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 Example 1, the fiber diameter of the polyester long fiber after melt spinning at a draw ratio of 545 was set to 12.0 μm, and spinning was performed so that the weight per unit area of the polyester long fiber became 20 g / m 2 , Other than this, the polyester long fiber nonwoven fabric was obtained in the same manner as in Example 1, but the transparency of the nonwoven fabric was low, and sufficient transparency could not be obtained as a filter for food. The physical properties of the obtained nonwoven 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 nonwoven 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 nonwoven 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 nonwoven 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。 Use titanium element content of 12ppm, inherent viscosity (IV) of 0.65, melting point of 253 ℃ Except for the polyester-based resin, a polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 4. The physical properties of the obtained nonwoven 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 nonwoven 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 with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.8, and a melting point of 246 ° C is supplied to a commonly used melt spinning device and melted at 295 ° C, from a spinning hole with 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 polyester long fibers with a fiber diameter of 30.3 μm. Then, a flat-plate-shaped airflow-controlling dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °] was used to spread the fibers to make a net with a weight per unit area of 20 / m 2 , which was applied to the embossing roll and smoothing roll. During the local thermal compression bonding at a thermal compression bonding area ratio of 15%, a polyester long fiber nonwoven fabric is obtained, but as a food filter, sufficient dimensional stability cannot be obtained. The physical properties of the obtained nonwoven 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 fiber after melt spinning at a draw ratio of 345 was set to 50.0 μm, and spinning was performed so that the weight per unit area of the polyester long fiber became 20 g / m 2 . However, the shrinkage of the roller is too large to obtain polyester long fiber nonwoven fabric. The physical properties of the obtained nonwoven 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 Example 3, a net was produced in such a way that the weight per unit area of the polyester long fiber became 40 g / m 2 , except that the polyester long fiber nonwoven fabric was obtained in the same manner as in Example 3, but the transparency of the nonwoven fabric was low , As a food filter can not obtain sufficient transparency. The physical properties of the obtained nonwoven 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。 Except that the titanium content of the resin was set to 3000 ppm, a polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 21. The physical properties of the obtained nonwoven 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。 Except that the IV value of the resin was set to 0.7, in the same manner as in Comparative Example 11, a polyester long-fiber nonwoven fabric was obtained. The physical properties of the obtained nonwoven 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 with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65 and a melting point of 254 ° C is used as the core, and a polyester system with a titanium content of 0 ppm, an intrinsic viscosity (IV) of 0.65 and a melting point of 217 ° C The resin is supplied as a sheath to a commonly used melt spinning device and is melted at 275 ° C. Melt spinning is performed at a spinning speed of 4500 m / min from a spinning head having a spinning hole with a circular cross-section and a flat-shaped controlled air flow is used The dispersing device [the inclination angle of the flat plate with respect to the filament is 4 °] disperses the polyester long fibers with a fiber diameter of 14 μm, and disperses the net weight of 15 g / m 2 between the embossing roller and the smoothing roller to heat The area of the crimping area is 15%, and local thermal crimping is performed to obtain a polyester long fiber nonwoven fabric. The physical properties of the obtained nonwoven fabric are shown in Table 3 below. Furthermore, when heat-sealing the obtained nonwoven fabric, the sealing machine produces serious resin contamination.
[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。 Except that the weight per unit area of each layer was 10 g / m 2 , a polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 21. Table 3 shows the physical properties of the obtained nonwoven fabric.
[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。 Except that the weight per unit area of each layer was 4 g / m 2 , a polyester long-fiber nonwoven fabric was obtained in the same manner as in Example 26. Table 3 shows the physical properties of the obtained nonwoven fabric.
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 excellent in transparency, dimensional stability, powder leakage, and component extractability, so it can be preferably used as a filter for food.
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| JP6836439B2 (en) * | 2017-03-27 | 2021-03-03 | 旭化成株式会社 | Food filter material |
| JP6551918B2 (en) * | 2017-05-20 | 2019-07-31 | 大紀商事株式会社 | Extraction sheet, extraction filter and extraction bag |
| 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 | A kind of air filter material and its use |
| 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 |
| CN118891407A (en) * | 2022-03-15 | 2024-11-01 | 三井化学旭生活材料有限公司 | Nonwoven fabric and use thereof |
| 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 |
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007197028A (en) * | 2006-01-25 | 2007-08-09 | Asahi Kasei Fibers Corp | Bag |
| JP2008054840A (en) * | 2006-08-30 | 2008-03-13 | Asahi Kasei Fibers Corp | FILTER FILTER MATERIAL AND METHOD FOR PRODUCING FOOD-INCLOSED PAG |
| JP2009262991A (en) * | 2008-04-30 | 2009-11-12 | Shizuoka Prefecture | Dripping tea bag |
| TW201125911A (en) * | 2009-09-30 | 2011-08-01 | Adeka Corp | Polyester resin composition, polyester fiber, polyester resin molded article, and process for production of nucleating agent for polyester resin |
Family Cites Families (16)
| 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 |
| JP3939326B2 (en) | 2002-07-01 | 2007-07-04 | 旭化成せんい株式会社 | Non-woven fabric and tea bag |
| JP2007152216A (en) * | 2005-12-05 | 2007-06-21 | Toray Ind Inc | Nonwoven fabric for filter |
| KR101036856B1 (en) * | 2006-01-25 | 2011-05-25 | 아사히 가세이 셍이 가부시키가이샤 | Thermal Adhesive Laminated Nonwoven Fabric |
| 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 |
| TWI618279B (en) * | 2012-04-04 | 2018-03-11 | Asahi Kasei Fibers Corp | Divider material |
| US10811658B2 (en) * | 2012-09-19 | 2020-10-20 | Asahi Kasei Kabushiki Kaisha | Separator and method of preparing the same, and lithium ion secondary battery |
| 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 |
-
2016
- 2016-03-31 GB GB1716072.2A patent/GB2555721B/en active Active
- 2016-03-31 CN CN201680015024.1A patent/CN107429459B/en active Active
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- 2016-03-31 KR KR1020177025786A patent/KR101952528B1/en active Active
-
2020
- 2020-02-05 JP JP2020018048A patent/JP6898482B2/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007197028A (en) * | 2006-01-25 | 2007-08-09 | Asahi Kasei Fibers Corp | Bag |
| JP2008054840A (en) * | 2006-08-30 | 2008-03-13 | Asahi Kasei Fibers Corp | FILTER FILTER MATERIAL AND METHOD FOR PRODUCING FOOD-INCLOSED PAG |
| JP2009262991A (en) * | 2008-04-30 | 2009-11-12 | Shizuoka Prefecture | Dripping tea bag |
| TW201125911A (en) * | 2009-09-30 | 2011-08-01 | Adeka Corp | Polyester resin composition, polyester fiber, polyester resin molded article, and process for production of nucleating agent for polyester resin |
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| GB201716072D0 (en) | 2017-11-15 |
| JPWO2016159266A1 (en) | 2017-11-16 |
| JP6657189B2 (en) | 2020-03-04 |
| CN107429459A (en) | 2017-12-01 |
| JP2020073751A (en) | 2020-05-14 |
| WO2016159266A1 (en) | 2016-10-06 |
| CN107429459B (en) | 2020-04-14 |
| TW201643289A (en) | 2016-12-16 |
| KR20170117525A (en) | 2017-10-23 |
| GB2555721B (en) | 2021-03-03 |
| JP6898482B2 (en) | 2021-07-07 |
| GB2555721A (en) | 2018-05-09 |
| KR101952528B1 (en) | 2019-02-26 |
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