JP4481907B2 - Original polylactic acid crimped yarn, method for producing the same, and carpet - Google Patents
Original polylactic acid crimped yarn, method for producing the same, and carpet Download PDFInfo
- Publication number
- JP4481907B2 JP4481907B2 JP2005258632A JP2005258632A JP4481907B2 JP 4481907 B2 JP4481907 B2 JP 4481907B2 JP 2005258632 A JP2005258632 A JP 2005258632A JP 2005258632 A JP2005258632 A JP 2005258632A JP 4481907 B2 JP4481907 B2 JP 4481907B2
- Authority
- JP
- Japan
- Prior art keywords
- yarn
- polylactic acid
- crimped yarn
- temperature
- original
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 229920000747 poly(lactic acid) Polymers 0.000 title claims description 205
- 239000004626 polylactic acid Substances 0.000 title claims description 203
- 238000004519 manufacturing process Methods 0.000 title claims description 31
- 239000012530 fluid Substances 0.000 claims description 45
- 238000002788 crimping Methods 0.000 claims description 35
- 238000010438 heat treatment Methods 0.000 claims description 33
- 239000000835 fiber Substances 0.000 claims description 31
- 238000009998 heat setting Methods 0.000 claims description 31
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 claims description 29
- 239000003086 colorant Substances 0.000 claims description 27
- 238000009987 spinning Methods 0.000 claims description 20
- 239000003795 chemical substances by application Substances 0.000 claims description 19
- 238000001816 cooling Methods 0.000 claims description 17
- 239000004310 lactic acid Substances 0.000 claims description 14
- 235000014655 lactic acid Nutrition 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 14
- 239000003921 oil Substances 0.000 claims description 14
- 239000000470 constituent Substances 0.000 claims description 13
- 238000002425 crystallisation Methods 0.000 claims description 11
- 230000008025 crystallization Effects 0.000 claims description 11
- 230000009477 glass transition Effects 0.000 claims description 8
- 238000012545 processing Methods 0.000 claims description 7
- 239000011248 coating agent Substances 0.000 claims description 3
- 238000000576 coating method Methods 0.000 claims description 3
- 230000001788 irregular Effects 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 25
- JVTAAEKCZFNVCJ-REOHCLBHSA-N L-lactic acid Chemical compound C[C@H](O)C(O)=O JVTAAEKCZFNVCJ-REOHCLBHSA-N 0.000 description 14
- -1 polypropylene Polymers 0.000 description 14
- 238000000034 method Methods 0.000 description 13
- 229920000642 polymer Polymers 0.000 description 11
- 238000005299 abrasion Methods 0.000 description 10
- 239000001023 inorganic pigment Substances 0.000 description 10
- 230000008569 process Effects 0.000 description 9
- 230000002829 reductive effect Effects 0.000 description 9
- 239000006229 carbon black Substances 0.000 description 8
- 239000000178 monomer Substances 0.000 description 8
- 239000012860 organic pigment Substances 0.000 description 8
- 238000004043 dyeing Methods 0.000 description 7
- QPFMBZIOSGYJDE-UHFFFAOYSA-N 1,1,2,2-tetrachloroethane Chemical compound ClC(Cl)C(Cl)Cl QPFMBZIOSGYJDE-UHFFFAOYSA-N 0.000 description 6
- 239000004743 Polypropylene Substances 0.000 description 6
- 239000004744 fabric Substances 0.000 description 6
- 238000000691 measurement method Methods 0.000 description 6
- 239000000049 pigment Substances 0.000 description 6
- 229920001155 polypropylene Polymers 0.000 description 6
- 239000002994 raw material Substances 0.000 description 6
- 239000000463 material Substances 0.000 description 5
- 230000003287 optical effect Effects 0.000 description 5
- 229920000728 polyester Polymers 0.000 description 5
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 4
- 229930182843 D-Lactic acid Natural products 0.000 description 4
- JVTAAEKCZFNVCJ-UWTATZPHSA-N D-lactic acid Chemical compound C[C@@H](O)C(O)=O JVTAAEKCZFNVCJ-UWTATZPHSA-N 0.000 description 4
- 239000004594 Masterbatch (MB) Substances 0.000 description 4
- 239000002216 antistatic agent Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 230000006835 compression Effects 0.000 description 4
- 238000007906 compression Methods 0.000 description 4
- 229940022769 d- lactic acid Drugs 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000011156 evaluation Methods 0.000 description 4
- 239000000155 melt Substances 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 239000004745 nonwoven fabric Substances 0.000 description 4
- 125000002080 perylenyl group Chemical group C1(=CC=C2C=CC=C3C4=CC=CC5=CC=CC(C1=C23)=C45)* 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- 238000004804 winding Methods 0.000 description 4
- 239000004677 Nylon Substances 0.000 description 3
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 239000010941 cobalt Substances 0.000 description 3
- 229910017052 cobalt Inorganic materials 0.000 description 3
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 3
- 238000007872 degassing Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 3
- 239000000975 dye Substances 0.000 description 3
- 239000003995 emulsifying agent Substances 0.000 description 3
- 238000009499 grossing Methods 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 239000011259 mixed solution Substances 0.000 description 3
- 229920001778 nylon Polymers 0.000 description 3
- CSHWQDPOILHKBI-UHFFFAOYSA-N peryrene Natural products C1=CC(C2=CC=CC=3C2=C2C=CC=3)=C3C2=CC=CC3=C1 CSHWQDPOILHKBI-UHFFFAOYSA-N 0.000 description 3
- GUYIZQZWDFCUTA-UHFFFAOYSA-N (pentadecachlorophthalocyaninato(2-))-copper Chemical compound [Cu+2].N1=C([N-]2)C3=C(Cl)C(Cl)=C(Cl)C(Cl)=C3C2=NC(C2=C(Cl)C(Cl)=C(Cl)C(Cl)=C22)=NC2=NC(C2=C(Cl)C(Cl)=C(Cl)C(Cl)=C22)=NC2=NC2=C(C(Cl)=C(C(Cl)=C3)Cl)C3=C1[N-]2 GUYIZQZWDFCUTA-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 229910019142 PO4 Inorganic materials 0.000 description 2
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 239000003963 antioxidant agent Substances 0.000 description 2
- 230000003078 antioxidant effect Effects 0.000 description 2
- 229920006167 biodegradable resin Polymers 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 238000004128 high performance liquid chromatography Methods 0.000 description 2
- PXZQEOJJUGGUIB-UHFFFAOYSA-N isoindolin-1-one Chemical class C1=CC=C2C(=O)NCC2=C1 PXZQEOJJUGGUIB-UHFFFAOYSA-N 0.000 description 2
- 238000002074 melt spinning Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 235000021317 phosphate Nutrition 0.000 description 2
- IEQIEDJGQAUEQZ-UHFFFAOYSA-N phthalocyanine Chemical class N1C(N=C2C3=CC=CC=C3C(N=C3C4=CC=CC=C4C(=N4)N3)=N2)=C(C=CC=C2)C2=C1N=C1C2=CC=CC=C2C4=N1 IEQIEDJGQAUEQZ-UHFFFAOYSA-N 0.000 description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 description 2
- 239000005020 polyethylene terephthalate Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 239000010936 titanium Substances 0.000 description 2
- 229910052719 titanium Inorganic materials 0.000 description 2
- 239000006097 ultraviolet radiation absorber Substances 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 1
- AMZKGJLFYCZDMJ-WRBBJXAJSA-N [2,2-dimethyl-3-[(z)-octadec-9-enoyl]oxypropyl] (z)-octadec-9-enoate Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCC(C)(C)COC(=O)CCCCCCC\C=C/CCCCCCCC AMZKGJLFYCZDMJ-WRBBJXAJSA-N 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000003242 anti bacterial agent Substances 0.000 description 1
- 239000010426 asphalt Substances 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 239000004359 castor oil Substances 0.000 description 1
- 235000019438 castor oil Nutrition 0.000 description 1
- IYRDVAUFQZOLSB-UHFFFAOYSA-N copper iron Chemical compound [Fe].[Cu] IYRDVAUFQZOLSB-UHFFFAOYSA-N 0.000 description 1
- XCJYREBRNVKWGJ-UHFFFAOYSA-N copper(II) phthalocyanine Chemical compound [Cu+2].C12=CC=CC=C2C(N=C2[N-]C(C3=CC=CC=C32)=N2)=NC1=NC([C]1C=CC=CC1=1)=NC=1N=C1[C]3C=CC=CC3=C2[N-]1 XCJYREBRNVKWGJ-UHFFFAOYSA-N 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000002781 deodorant agent Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- KFZAUHNPPZCSCR-UHFFFAOYSA-N iron zinc Chemical compound [Fe].[Zn] KFZAUHNPPZCSCR-UHFFFAOYSA-N 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 230000000670 limiting effect Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000006224 matting agent Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- PJQYNUFEEZFYIS-UHFFFAOYSA-N perylene maroon Chemical compound C=12C3=CC=C(C(N(C)C4=O)=O)C2=C4C=CC=1C1=CC=C2C(=O)N(C)C(=O)C4=CC=C3C1=C42 PJQYNUFEEZFYIS-UHFFFAOYSA-N 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000007573 shrinkage measurement Methods 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 238000009732 tufting Methods 0.000 description 1
- 239000003981 vehicle Substances 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
- 235000014692 zinc oxide Nutrition 0.000 description 1
Images
Landscapes
- Artificial Filaments (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
- Carpets (AREA)
Description
この発明は、嵩高性に優れ、高タフネスで耐摩耗性に優れた原着ポリ乳酸捲縮糸及びその製造方法、並びに該捲縮糸を用いて構成された、十分なボリューム感を有し、風合いや耐摩耗性に優れたカーペットに関する。 This invention is excellent in bulkiness, has high toughness and wear resistance, and has a sufficient volume feeling constituted by using the original polylactic acid crimped yarn having excellent toughness and its production method, and the crimped yarn, It relates to carpets with excellent texture and wear resistance.
ポリ乳酸は、トウモロコシ等の澱粉から得られる乳酸を原料とする生分解性樹脂であり、微生物等により水と二酸化炭素に分解されることから、自然の物質循環サイクルに適合していて地球環境にやさしい素材として注目されている。このような生分解性樹脂であるポリ乳酸繊維を用いて、車両用オプションマット、家庭用ロールカーペットやラグ等を製作することが検討されている。このポリ乳酸を用いた糸で、現行のナイロン捲縮糸、ポリプロピレン捲縮糸、ポリエステル捲縮糸と同様の物性が得られれば、カーペット用途は勿論のこと、他のインテリア用素材として幅広く展開できることが期待されるところである。 Polylactic acid is a biodegradable resin that uses lactic acid obtained from starch such as corn as a raw material, and is decomposed into water and carbon dioxide by microorganisms and the like. It is attracting attention as a gentle material. Production of an option mat for a vehicle, a household roll carpet, a rug, or the like using a polylactic acid fiber that is such a biodegradable resin has been studied. If the same properties as the current nylon crimped polypropylene, polypropylene crimped and polyester crimped yarns can be obtained with this polylactic acid yarn, it can be widely used as a material for interiors as well as carpets. Is expected.
しかしながら、従来のポリ乳酸捲縮糸を使用したカーペットは、嵩高性に劣り、摩耗しやすく、へたり易いという欠点があった。このような欠点を抱えていることから、ごく限られた用途にしか実用化されていないのが実状である。これは、ポリ乳酸捲縮糸の強度や伸度等の糸物性および捲縮特性が、現行のナイロン捲縮糸、ポリプロピレン捲縮糸、ポリエステル捲縮糸と比較して劣っているためである。 However, the carpet using the conventional polylactic acid crimped yarn has the disadvantages that it is inferior in bulkiness, easily worn, and easily sag. Because of these drawbacks, the reality is that it has been put to practical use only for very limited purposes. This is because the properties of the polylactic acid crimped yarn, such as strength and elongation, and crimp properties are inferior to those of current nylon crimped polypropylene, polypropylene crimped yarn, and polyester crimped yarn.
一方、従来、ポリ乳酸捲縮糸及びその製造方法に関し特許文献1〜3が公知である。特許文献1には、先染め用のポリ乳酸捲縮糸として、強度、捲縮伸長率、捲縮潜在化率、加圧熱水処理後の強力保持率が特定範囲にあるものを用いることにより、染色によって生ずる捲縮糸の強度や捲縮特性の低下を改善できることが記載されている。
On the other hand,
また、特許文献2には、単繊維の長軸と短軸の長さの比から求めた単繊維断面の扁平率が3〜8で、該単繊維が単繊維繊度5〜25dtexのポリ乳酸繊維で構成されたポリ乳酸扁平捲縮糸を用いることにより、柔らかで嵩高性があり、清涼感がある独特の風合いを有したカーペットを構成できることが記載されている。
また、特許文献3には、原着ポリ乳酸捲縮糸として、単繊維が変形度1.5〜5.5の異形断面形状を有し、かつ相対粘度、強度、捲縮伸長率、捲縮潜在化率、交絡数、交絡点強度が特定範囲にあるものを用いることにより、カーペットとして嵩高性、耐摩耗性、耐へたり性を改善できることが記載されている。
しかしながら、特許文献1に記載されたポリ乳酸捲縮糸は、先染め用のポリ乳酸捲縮糸に関するものであり、該先染め用のポリ乳酸捲縮糸は、染色による加圧熱水処理により、その強度、伸度、捲縮特性は必ず低下する。特に、黒に代表される濃色の場合には、高温熱水(例えば120〜130℃)にて染色することが不可欠であり、このために物性低下が顕著である。従って、特許文献1に記載のポリ乳酸捲縮糸を用いて濃色系のカーペットを構成した場合には、その嵩高性、耐摩耗性、耐へたり性の改善の程度はまだ不十分であった。
However, the polylactic acid crimped yarn described in
また、特許文献2に記載の技術で得られたポリ乳酸扁平捲縮糸は、糸物性が不十分であり、特に糸強度が不足しており(特許文献2の実施例1では糸強度が1.6、実施例2で1.7、実施例3で1.5、実施例4で1.8、実施例5で1.5cN/dtexである)、このために該ポリ乳酸扁平捲縮糸を用いて構成されたカーペットは、耐摩耗性及び耐へたり性に劣っており、このためにその用途はごく限られたものにならざるを得ない。
In addition, the polylactic acid flat crimped yarn obtained by the technique described in
また、特許文献3に記載された原着ポリ乳酸捲縮糸を用いて構成されたカーペットは、その嵩高性、耐摩耗性、耐へたり性の改善の程度はまだ不十分であり、例えば自動車用オプションマット、自動車用ラインマット、タイルカーペット、家庭用ロールカーペットを構成した場合においてその嵩高性、耐摩耗性、耐へたり性等の耐久性は実用レベルにおいて十分に満足できるものではなかった。なお、特許文献3では、ポリ乳酸繊維の配向・結晶と関係した熱水収縮率等については全く言及されていない。
Further, the carpet constructed using the original polylactic acid crimped yarn described in
この発明は、かかる技術的背景に鑑みてなされたものであって、嵩高性に優れ、高タフネスで耐摩耗性に優れた原着ポリ乳酸捲縮糸及びその製造方法を提供し、また該捲縮糸を用いた、十分なボリューム感を有し、風合いが良好で、嵩高性、耐摩耗性、耐へたり性に優れたカーペットを提供することを目的とする。 The present invention has been made in view of such a technical background, and provides an original polylactic acid crimped yarn excellent in bulkiness, high toughness and wear resistance, and a method for producing the same. An object of the present invention is to provide a carpet having a sufficient volume feeling, good texture, and excellent bulkiness, wear resistance, and sag resistance, using reduced yarn.
前記目的を達成するために、本発明者は、原着ポリ乳酸捲縮糸の強度等の糸物性の不足及び捲縮特性の不足並びに熱水収縮性能の不適合、これらに起因したカーペットの耐摩耗性不良や嵩高性の不足等の改善について鋭意研究した結果、原着捲縮糸を構成する単繊維の断面形状を特定構成に限定すると共に、相対粘度を特定範囲に限定し、かつ強度、伸度、総繊度、単糸繊度、熱水収縮率及び乾熱捲縮率をそれぞれ特定範囲に限定することによって、前記課題を一挙に解決できることを見出すに至り、この発明を完成したものである。即ち、本発明は以下の手段を提供する。 In order to achieve the above-mentioned object, the present inventor has found that the physical properties such as the strength of the original polylactic acid crimped yarn are insufficient, the crimp property is insufficient, and the hot water shrinkage performance is inadequate. As a result of earnest research on improvements such as inferiority and lack of bulkiness, the cross-sectional shape of the single fiber constituting the original crimped yarn is limited to a specific configuration, the relative viscosity is limited to a specific range, and the strength and elongation are reduced. The inventors have found that the above-mentioned problems can be solved at once by limiting the degree, the total fineness, the single yarn fineness, the hot water shrinkage rate, and the dry heat crimp rate to specific ranges, thereby completing the present invention. That is, the present invention provides the following means.
[1]断面形状が略円形状または円形状の単繊維を有し、相対粘度が2.5〜3.8であるポリ乳酸捲縮糸からなり、
前記ポリ乳酸捲縮糸は、着色剤を0.01〜3質量%含有してなり、
前記ポリ乳酸捲縮糸は、強度が1.75〜3.5cN/dtex、伸度が35〜60%、総繊度が500〜3500dtex、単糸繊度が2.5〜25dtex、熱水収縮率が2〜8%、乾熱捲縮率が5〜25%であることを特徴とする原着ポリ乳酸捲縮糸。
[1] A polylactic acid crimped yarn having a single fiber having a substantially circular or circular cross-section and a relative viscosity of 2.5 to 3.8,
The polylactic acid crimped yarn contains 0.01 to 3% by mass of a colorant,
The polylactic acid crimped yarn has a strength of 1.75 to 3.5 cN / dtex, an elongation of 35 to 60%, a total fineness of 500 to 3500 dtex, a single yarn fineness of 2.5 to 25 dtex, and a hot water shrinkage. An original polylactic acid crimped yarn having a dry heat crimp rate of 2 to 8% and a dry heat crimp rate of 5 to 25%.
[2]前記単繊維の断面形状が異形度1.5未満の略円形状または円形状である前項1に記載の原着ポリ乳酸捲縮糸。
[2] The original polylactic acid crimped yarn according to
[3]前記着色剤として、無機顔料及び有機顔料からなる群より選ばれた少なくとも1種の顔料が用いられている前項1または2に記載の原着ポリ乳酸捲縮糸。
[3] The original polylactic acid crimped yarn according to
[4]前項1〜3のいずれか1項に記載の原着ポリ乳酸捲縮糸を構成繊維の少なくとも一部に用いて構成されたカーペット。
[4] A carpet configured by using the original polylactic acid crimped yarn according to any one of
[5]着色剤及びポリ乳酸を含有し、着色剤含有率が0.01〜3質量%で相対粘度が2.5〜3.8であるポリ乳酸組成物を紡糸して、単繊維の断面形状が異形度1.5未満の略円形状または円形状である紡糸糸を得る紡糸工程と、前記紡糸糸を70〜125℃に設定された延伸ローラにより3〜6倍に延伸する工程と、前記延伸された紡糸糸を100〜150℃に設定された熱セットローラにより熱セットする工程と、前記熱セットされた延伸糸に加熱流体捲縮付与装置を用いて90〜160℃の加熱流体を接触させることによって糸に捲縮を付与する捲縮工程と、前記捲縮工程を経た捲縮糸を該糸のガラス転移温度よりも低い温度まで冷却する工程とを包含することを特徴とする原着ポリ乳酸捲縮糸の製造方法。
[5] Spinning a polylactic acid composition containing a colorant and polylactic acid, having a colorant content of 0.01 to 3% by mass and a relative viscosity of 2.5 to 3.8, A spinning step for obtaining a spun yarn having a substantially circular shape or a circular shape with a profile of less than 1.5, and a step of stretching the
[6]着色剤及びポリ乳酸を含有し、着色剤含有率が0.01〜3質量%で相対粘度が2.5〜3.8であるポリ乳酸組成物を紡糸口金から押出して断面形状が異形度1.5未満の略円形状または円形状のフィラメントを得、該フィラメントを冷風で冷却した後、フィラメントを油剤で被覆することによって紡糸糸を得る紡糸工程と、前記紡糸糸を70〜125℃に設定された延伸ローラにより3〜6倍に延伸する工程と、前記延伸された紡糸糸を100〜150℃に設定された熱セットローラにより熱セットする工程と、前記熱セットされた延伸糸に加熱流体捲縮付与装置を用いて90〜160℃の加熱流体を接触させることによって糸に捲縮を付与する捲縮工程と、前記捲縮工程を経た捲縮糸を該糸のガラス転移温度よりも低い温度まで冷却する工程とを包含することを特徴とする原着ポリ乳酸捲縮糸の製造方法。 [6] A polylactic acid composition containing a colorant and polylactic acid, having a colorant content of 0.01 to 3% by mass and a relative viscosity of 2.5 to 3.8 is extruded from a spinneret and has a cross-sectional shape. A spinning step of obtaining a substantially circular or circular filament having a degree of irregularity of less than 1.5, cooling the filament with cold air, and then coating the filament with an oil agent to obtain a spun yarn; A step of stretching 3 to 6 times by a stretching roller set to ° C., a step of heat setting the stretched spun yarn by a heat setting roller set to 100 to 150 ° C., and the heat-set drawn yarn A crimping step for imparting crimp to the yarn by contacting a heated fluid at 90 to 160 ° C. with a heating fluid crimping device, and the glass transition temperature of the crimped yarn after the crimping step. To lower temperatures Dyed polylactic acid crimped yarn manufacturing method which is characterized in that it comprises the step of retirement.
[7]前記熱セットローラの温度を「S」とし、前記加熱流体捲縮付与装置における加熱流体の温度を「R」としたとき、下記関係式
30℃≧ S−R ≧−10℃
を満足する前項5または6に記載の原着ポリ乳酸捲縮糸の製造方法。
[7] When the temperature of the heat setting roller is “S” and the temperature of the heating fluid in the heating fluid crimping device is “R”, the following relational expression: 30 ° C ≧ SR−10 ° C.
7. The method for producing an original polylactic acid crimped yarn according to
[8]前記延伸された紡糸糸を100℃以上であって且つポリ乳酸の軟化点温度以下の温度に設定された熱セットローラにより熱セットする前項5〜7のいずれか1項に記載の原着ポリ乳酸捲縮糸の製造方法。
[8] The raw material according to any one of
[9]前記熱セットされた延伸糸に加熱流体捲縮付与装置を用いて90℃以上であって且つポリ乳酸の結晶化温度以下の温度の加熱流体を接触させることによって糸に捲縮を付与する前項5〜8のいずれか1項に記載の原着ポリ乳酸捲縮糸の製造方法。
[9] A crimp is applied to the heat-set drawn yarn by contacting the heated fluid at a temperature of 90 ° C. or higher and lower than the crystallization temperature of polylactic acid using a heating fluid crimp applying device. 9. The method for producing an original polylactic acid crimped yarn according to any one of
[10]前記冷却工程を経た捲縮糸に交絡処理装置を用いて交絡処理することを特徴とする前項5〜9のいずれか1項に記載の原着ポリ乳酸捲縮糸の製造方法。 [10] The method for producing an original polylactic acid crimped yarn according to any one of [5] to [9], wherein the crimped yarn subjected to the cooling step is entangled using an entanglement processing device.
[11]前項5〜10のいずれか1項に記載の製造方法で製造された原着ポリ乳酸捲縮糸。 [11] An original polylactic acid crimped yarn produced by the production method according to any one of 5 to 10 above.
[12]前項11に記載の原着ポリ乳酸捲縮糸を構成繊維の少なくとも一部に用いて構成されたカーペット。
[12] A carpet formed by using the original polylactic acid crimped yarn according to
[1]の発明では、原着捲縮糸を構成する単繊維の断面形状を特定構成に限定すると共に、相対粘度を特定範囲に限定し、かつ強度、伸度、総繊度、単糸繊度、熱水収縮率及び乾熱捲縮率をそれぞれ特定範囲に限定しているから、嵩高性に優れ、高タフネスで耐摩耗性に優れた原着ポリ乳酸捲縮糸が提供される。 In the invention of [1], the cross-sectional shape of the single fiber constituting the original crimped yarn is limited to a specific configuration, the relative viscosity is limited to a specific range, and the strength, elongation, total fineness, single yarn fineness, Since the hot water shrinkage rate and the dry heat crimp rate are limited to specific ranges, an original polylactic acid crimped yarn having excellent bulkiness, high toughness and excellent wear resistance is provided.
[2]の発明では、単繊維の断面形状が異形度1.5未満の略円形状または円形状であるから、耐摩耗性をさらに向上させることができる。 In the invention of [2], since the cross-sectional shape of the single fiber is a substantially circular shape or a circular shape having an irregularity of less than 1.5, the wear resistance can be further improved.
[3]の発明では、着色剤として、無機顔料及び有機顔料からなる群より選ばれた少なくとも1種の顔料が用いられているから、染料等の他の着色剤を用いる場合と比べて、耐熱性、耐光性、耐候性を向上させることができる利点がある(即ち染料は熱分解しやすいので耐熱性が十分に得られない)。 In the invention of [3], since at least one pigment selected from the group consisting of inorganic pigments and organic pigments is used as the colorant, the heat resistance is higher than when other colorants such as dyes are used. There is an advantage that the heat resistance, the light resistance and the weather resistance can be improved (that is, since the dye is easily decomposed by heat, sufficient heat resistance cannot be obtained).
[4]の発明のカーペットは、[1]〜[3]のいずれかの構成の原着ポリ乳酸捲縮糸を構成繊維の少なくとも一部に用いて構成されているから、十分なボリューム感を有し、風合いが良好で、嵩高性、耐摩耗性、耐へたり性に優れている。 The carpet according to the invention of [4] is configured by using the original polylactic acid crimped yarn of any one of the constitutions [1] to [3] as at least a part of the constituent fibers. It has a good texture and is excellent in bulkiness, wear resistance and sag resistance.
[5]の発明では、嵩高性に優れ、高タフネスで耐摩耗性に優れた原着ポリ乳酸捲縮糸を製造することができる。また、紡糸原料として原着ポリ乳酸を用いているから、後工程として加熱処理のある染色工程を設けなくて済み、これにより加熱処理による悪影響(機械的強度の低下等)を回避できる利点がある。 In the invention of [5], an original polylactic acid crimped yarn having excellent bulkiness, high toughness and excellent wear resistance can be produced. In addition, since the original polylactic acid is used as a spinning raw material, there is no need to provide a dyeing step with heat treatment as a subsequent step, and this has the advantage of avoiding adverse effects (such as a decrease in mechanical strength) due to heat treatment. .
[6]の発明では、嵩高性に優れ、高タフネスで耐摩耗性に優れた原着ポリ乳酸捲縮糸を製造することができる。また、紡糸原料として原着ポリ乳酸を用いているから、後工程として加熱処理のある染色工程を設けなくて済み、これにより加熱処理による悪影響(機械的強度の低下等)を回避できる利点がある。また、ポリ乳酸組成物を紡糸口金から押出してフィラメントを得、該フィラメントを冷風で冷却した後、フィラメントを油剤で被覆することによって紡糸糸を得るから、生産効率良く紡糸糸を製造できると共に、油剤の被覆により糸に平滑性や帯電防止性を付与することができる。更に、捲縮糸を該糸のガラス転移温度よりも低い温度まで冷却するので、十分な捲縮が付与された原着ポリ乳酸捲縮糸を製造できる。 In the invention of [6], an original polylactic acid crimped yarn having excellent bulkiness, high toughness and excellent wear resistance can be produced. In addition, since the original polylactic acid is used as a spinning raw material, there is no need to provide a dyeing step with heat treatment as a subsequent step, and this has the advantage of avoiding adverse effects (such as a decrease in mechanical strength) due to heat treatment. . In addition, since a polylactic acid composition is extruded from a spinneret to obtain filaments, the filaments are cooled with cold air, and then the filaments are coated with an oil agent to obtain a spun yarn. The coating can impart smoothness and antistatic properties to the yarn. Furthermore, since the crimped yarn is cooled to a temperature lower than the glass transition temperature of the yarn, an original polylactic acid crimped yarn imparted with sufficient crimp can be produced.
[7]の発明では、熱セットローラの温度を「S」とし、前記加熱流体捲縮付与装置における加熱流体の温度を「R」としたとき、下記関係式
30℃≧ S−R ≧−10℃
を満足する条件で製造するので、得られる原着ポリ乳酸捲縮糸の強度及び伸度ともに向上させることができる。
In the invention of [7], when the temperature of the heat setting roller is “S” and the temperature of the heated fluid in the heated fluid crimping device is “R”, the following relational expression: 30 ° C. ≧ SR−10 ℃
Therefore, the strength and elongation of the obtained original polylactic acid crimped yarn can be improved.
[8]の発明では、延伸された紡糸糸を100℃以上であって且つポリ乳酸の軟化点温度以下の温度に設定された熱セットローラにより熱セットするから、ポリ乳酸として適度な結晶化を発現させ得て捲縮糸の強度及び伸度ともに向上させることができる。 In the invention of [8], the drawn spun yarn is heat set by a heat setting roller set at a temperature of 100 ° C. or higher and lower than the softening point temperature of polylactic acid. Both the strength and the elongation of the crimped yarn can be improved.
[9]の発明では、熱セットされた延伸糸に加熱流体捲縮付与装置を用いて90℃以上であって且つポリ乳酸の結晶化温度以下の温度の加熱流体を接触させることによって糸に捲縮を付与するから、配向結晶化したポリ乳酸繊維の捲縮付与時の繊維へのダメージが低減され、これにより、得られる原着ポリ乳酸捲縮糸の強度及び伸度を向上させることができる。 In the invention of [9], the heated set crimped yarn is brought into contact with a heated fluid having a temperature of 90 ° C. or higher and lower than the crystallization temperature of polylactic acid by using a heated fluid crimping device. Since the shrinkage is imparted, damage to the fibers at the time of crimping of the oriented and crystallized polylactic acid fiber is reduced, thereby improving the strength and elongation of the obtained original polylactic acid crimped yarn. .
[10]の発明では、冷却工程を経た捲縮糸に交絡処理装置を用いて交絡処理するから、タフト時の捲縮糸のタフト性を向上させることができる。 In the invention of [10], the crimped yarn that has undergone the cooling process is entangled using the entanglement processing device, so that the tuftability of the crimped yarn during tufting can be improved.
[11]の発明では、嵩高性に優れ、高タフネスで耐摩耗性に優れた原着ポリ乳酸捲縮糸が提供される。 In the invention of [11], an original polylactic acid crimped yarn having excellent bulkiness, high toughness and excellent wear resistance is provided.
[12]の発明では、十分なボリューム感を有し、風合いが良好で、嵩高性、耐摩耗性、耐へたり性に優れたカーペットが提供される。 In the invention of [12], a carpet having sufficient volume feeling, good texture, and excellent in bulkiness, abrasion resistance and sag resistance is provided.
この発明に係る原着ポリ乳酸捲縮糸は、断面形状が略円形状または円形状の単繊維を有するものであり、該捲縮糸は、相対粘度が2.5〜3.8である。また、この発明の原着ポリ乳酸捲縮糸は、着色剤及びポリ乳酸を含有したポリ乳酸組成物からなる。 The original polylactic acid crimped yarn according to the present invention has single fibers having a substantially circular or circular cross section, and the crimped yarn has a relative viscosity of 2.5 to 3.8. The original polylactic acid crimped yarn of the present invention comprises a polylactic acid composition containing a colorant and polylactic acid.
この発明の原着ポリ乳酸捲縮糸の原料として用いられるポリ乳酸組成物を構成するポリ乳酸は、L−乳酸を主成分とする乳酸モノマーを重合してなるポリ乳酸である。前記乳酸モノマー中の90質量%以上がL−乳酸からなる構成を採用するのが好ましい。即ち、前記乳酸モノマー中に10質量%を超えない範囲でD−乳酸を含有していても良い。使用する乳酸モノマーの光学純度(L体の光学純度)が90%以上であれば、そのポリマー(ポリ乳酸)は結晶性となり好ましく、使用する乳酸モノマーの光学純度(L体の光学純度)が97%以上であれば、融点が170℃前後となり、より一層好ましい。また、この発明の効果を阻害しない範囲であれば、乳酸以外の成分を共重合したものを用いても良い。乳酸以外の成分を共重合した場合、ポリマー分子鎖の全繰り返し単位の70質量%以上100質量%未満、好ましくは80質量%以上100質量%未満、より好ましくは90質量%以上100質量%未満を乳酸単位とする。 The polylactic acid constituting the polylactic acid composition used as the raw material of the original polylactic acid crimped yarn of this invention is a polylactic acid obtained by polymerizing a lactic acid monomer containing L-lactic acid as a main component. It is preferable to employ a configuration in which 90% by mass or more of the lactic acid monomer is composed of L-lactic acid. That is, the lactic acid monomer may contain D-lactic acid within a range not exceeding 10% by mass. If the optical purity of the lactic acid monomer used (optical purity of the L isomer) is 90% or more, the polymer (polylactic acid) is preferably crystalline, and the optical purity of the lactic acid monomer used (optical purity of the L isomer) is 97. % Or more, the melting point is around 170 ° C., which is even more preferable. Moreover, as long as the effect of this invention is not inhibited, what copolymerized components other than lactic acid may be used. When components other than lactic acid are copolymerized, 70% by mass or more and less than 100% by mass, preferably 80% by mass or more and less than 100% by mass, more preferably 90% by mass or more and less than 100% by mass, based on all repeating units of the polymer molecular chain. Lactic acid unit.
この発明の原着ポリ乳酸捲縮糸の相対粘度(RV)は2.5〜3.8である必要がある。ここで、前記相対粘度は、20℃、フェノール/テトラクロロエタン=60/40(質量比)の混合溶液で測定した値である。前記相対粘度が2.5未満ではポリ乳酸捲縮糸に十分な強度や伸度を付与することができないし、カーペット用途に適した耐摩耗性を付与することができない。一方、前記相対粘度が3.8を超えると、溶融粘度が高くなり過ぎる結果、紡糸温度を上げる必要が生じ、その結果、得られるポリ乳酸捲縮糸の相対粘度が溶融前のレベルよりもかなり低下し、強度が十分に向上しないし、また製糸し難くなるという問題を生じる。中でも、原着ポリ乳酸捲縮糸の相対粘度は2.8〜3.6であるのが好ましい。 The relative viscosity (RV) of the original polylactic acid crimped yarn of this invention needs to be 2.5 to 3.8. Here, the relative viscosity is a value measured with a mixed solution of 20 ° C. and phenol / tetrachloroethane = 60/40 (mass ratio). When the relative viscosity is less than 2.5, sufficient strength and elongation cannot be imparted to the polylactic acid crimped yarn, and abrasion resistance suitable for carpet use cannot be imparted. On the other hand, if the relative viscosity exceeds 3.8, the melt viscosity becomes too high, so that it is necessary to raise the spinning temperature. As a result, the relative viscosity of the obtained polylactic acid crimped yarn is considerably higher than the level before melting. The strength is lowered and the strength is not sufficiently improved, and it becomes difficult to produce the yarn. Among them, the relative viscosity of the original polylactic acid crimped yarn is preferably 2.8 to 3.6.
また、この発明の原着ポリ乳酸捲縮糸の原料として用いられるポリ乳酸組成物は、着色剤を0.01〜3質量%含有した構成である。このような濃度に設定することにより、捲縮糸に適当な濃度の色を付与することができて意匠性を向上できる。また0.01質量%以上とすることで顔料ムラに起因した色斑の発生を防止できると共に3質量%以下とすることで糸切れ発生を十分に防止することができる。中でも、着色剤の含有率は0.05〜1質量%であるのが好ましい。また、着色剤は、通常用いられる分散剤(オレフィン系化合物等)と併用して用いても良い。 Moreover, the polylactic acid composition used as a raw material of the original polylactic acid crimped yarn of this invention has a constitution containing 0.01 to 3% by mass of a colorant. By setting to such a density | concentration, the color of a suitable density | concentration can be provided to a crimped yarn and the design property can be improved. Further, when the content is 0.01% by mass or more, generation of color spots due to pigment unevenness can be prevented, and when the content is 3% by mass or less, occurrence of yarn breakage can be sufficiently prevented. Especially, it is preferable that the content rate of a coloring agent is 0.05-1 mass%. The colorant may be used in combination with a commonly used dispersant (such as an olefin compound).
なお、この発明の効果を阻害しない範囲であれば、前記ポリ乳酸組成物には、ポリ乳酸以外の他のポリマー(ポリマー粒子を含む)の他、艶消し剤、可塑剤、難燃剤、帯電防止剤、消臭剤、抗菌剤、抗酸化剤、耐熱剤、耐光剤、紫外線吸収剤等の各種添加剤を必要に応じて含有せしめても良い。 As long as the effect of the present invention is not impaired, the polylactic acid composition includes other polymers (including polymer particles) other than polylactic acid, matting agents, plasticizers, flame retardants, and antistatic agents. Various additives such as an agent, a deodorant, an antibacterial agent, an antioxidant, a heat-resistant agent, a light-resistant agent, and an ultraviolet absorber may be included as necessary.
この発明の原着ポリ乳酸捲縮糸は、その構成単繊維の断面形状が略円形状または円形状(即ち丸断面糸)である。このような断面形状にすることによって摩擦等があっても摩耗し難いものとなる、即ち摩擦に強い糸が得られる。中でも、前記単繊維の断面形状が異形度1.5未満(即ち1を超えて1.5未満)の略円形状または円形状であるのが好ましい。異形度が1.5以上であると、ポリ乳酸捲縮糸のカバーリング特性は向上するが、異形度が高いために、ポリ乳酸の硬くて脆い性状が出やすくなり、糸の耐摩耗性が低下するので、好ましくない。なお、前記異形度とは、単糸断面の外接円直径(B)と内接円直径(A)の比B/Aである(図2参照)。 In the original polylactic acid crimped yarn of the present invention, the cross-sectional shape of the constituent single fiber is substantially circular or circular (that is, round cross-sectional yarn). Such a cross-sectional shape makes it difficult to wear even if there is friction or the like, that is, a thread resistant to friction can be obtained. Especially, it is preferable that the cross-sectional shape of the said single fiber is a substantially circular shape or circular shape with a deformity of less than 1.5 (that is, more than 1 and less than 1.5). If the degree of deformity is 1.5 or more, the covering characteristics of the polylactic acid crimped yarn will be improved, but since the degree of deformity is high, the hard and brittle properties of polylactic acid are likely to occur, and the wear resistance of the yarn is reduced. Since it falls, it is not preferable. The irregularity is a ratio B / A between the circumscribed circle diameter (B) and the inscribed circle diameter (A) of the single yarn cross section (see FIG. 2).
更に、この発明の原着ポリ乳酸捲縮糸は、下記(1)〜(6)の特性を満足することを特徴とするものである。
(1)強度:1.75〜3.5cN/dtex
(2)伸度:35〜60%
(3)総繊度:500〜3500dtex
(4)単糸繊度:2.5〜25dtex
(5)熱水収縮率:2〜8%
(6)乾熱捲縮率:5〜25%。
Furthermore, the original polylactic acid crimped yarn of the present invention is characterized by satisfying the following properties (1) to (6).
(1) Strength: 1.75 to 3.5 cN / dtex
(2) Elongation: 35-60%
(3) Total fineness: 500-3500 dtex
(4) Single yarn fineness: 2.5 to 25 dtex
(5) Hot water shrinkage: 2-8%
(6) Dry heat crimp rate: 5 to 25%.
前記原着ポリ乳酸捲縮糸の強度は1.75〜3.5cN/dtexである。前記捲縮糸の強度が1.75cN/dtex未満ではカーペットにした時に捲縮糸の一部がすり切れてしまうことがあり、カーペット用途に適した耐摩耗性を付与することができない。中でも、前記原着ポリ乳酸捲縮糸の強度は2.0〜3.25cN/dtexであるのが好ましく、さらには2.25〜3.25cN/dtexであるのがより好ましい。 The strength of the original polylactic acid crimped yarn is 1.75 to 3.5 cN / dtex. If the strength of the crimped yarn is less than 1.75 cN / dtex, a portion of the crimped yarn may be worn out when it is made into a carpet, and it is impossible to provide abrasion resistance suitable for carpet use. Among these, the strength of the original polylactic acid crimped yarn is preferably 2.0 to 3.25 cN / dtex, and more preferably 2.25 to 3.25 cN / dtex.
前記原着ポリ乳酸捲縮糸の伸度は35〜60%である。前記捲縮糸の伸度が35%未満ではカーペットにした時に捲縮糸の一部がすり切れてしまうことがあり、カーペット用途に適した耐摩耗性を付与することができない。中でも、前記原着ポリ乳酸捲縮糸の伸度は40〜55%であるのが好ましい。 The elongation of the original polylactic acid crimped yarn is 35 to 60%. If the degree of elongation of the crimped yarn is less than 35%, a portion of the crimped yarn may be worn out when it is made into a carpet, and it is impossible to provide wear resistance suitable for carpet use. Among them, the elongation of the original polylactic acid crimped yarn is preferably 40 to 55%.
前記原着ポリ乳酸捲縮糸の強度が2.0〜3.25cN/dtexで、且つ前記原着ポリ乳酸捲縮糸の伸度が40〜55%である場合には、より高タフネスとなるので好ましい。但し、強度を上げていくと通常伸度は低下するものであり、伸度を35%以上とした場合の強度は高々3.5cN/dtexであり、また伸度が60%を超えると強度を1.75cN/dtex以上とすることができない。 When the strength of the original polylactic acid crimped yarn is 2.0 to 3.25 cN / dtex and the elongation of the original polylactic acid crimped yarn is 40 to 55%, higher toughness is obtained. Therefore, it is preferable. However, as the strength is increased, the normal elongation decreases. When the elongation is 35% or more, the strength is 3.5 cN / dtex at the most, and when the elongation exceeds 60%, the strength is decreased. It cannot be 1.75 cN / dtex or more.
また、前記原着ポリ乳酸捲縮糸の総繊度は500〜3500dtexの範囲である。このような範囲であれば、タフテッドカーペット等のカーペット用途に特に適した原着捲縮糸となるが、特にこのような用途への使用に限定されるものではない。中でも、前記原着ポリ乳酸捲縮糸の総繊度は1000〜3000dtexの範囲であるのが好ましい。 The total fineness of the original polylactic acid crimped yarn is in the range of 500 to 3500 dtex. If it is such a range, it will become an original crimped yarn especially suitable for carpet uses, such as a tufted carpet, However, It is not limited to especially the use for such a use. Among these, the total fineness of the original polylactic acid crimped yarn is preferably in the range of 1000 to 3000 dtex.
また、前記原着ポリ乳酸捲縮糸の単糸繊度は2.5〜25dtexの範囲である。単糸繊度が2.5dtex未満では、捲縮糸を安定に製糸することが困難であり、また該捲縮糸を用いて構成したカーペットは嵩高性が不十分なものとなる。一方、単糸繊度が25dtexを超えると、本発明の原着ポリ乳酸捲縮糸の糸物性を得るのが困難となるし、ポリ乳酸の硬くて脆いという性状が出やすくなって該捲縮糸を用いて構成したカーペットは耐摩耗性が不十分なものとなる。このような傾向は、同じ単糸繊度では、ポリ乳酸繊維の断面形状の異形度が大きくなるのに伴って顕著となる。従って、単繊維の異形度は小さい方が好ましい。中でも、前記原着ポリ乳酸捲縮糸の単糸繊度は4〜20dtexの範囲であるのが好ましく、より好ましくは5〜15dtexの範囲である。なお、単糸繊度2.5〜25dtexの範囲内において、単糸繊度が細くなる程、ポリ乳酸の硬くて脆いという性状がより軽減され得て、原着ポリ乳酸捲縮糸の強度や伸度をより向上させることができると共に、カーペットとした時の耐摩耗性も向上させることができる。 Further, the single yarn fineness of the original polylactic acid crimped yarn is in the range of 2.5 to 25 dtex. When the single yarn fineness is less than 2.5 dtex, it is difficult to stably produce the crimped yarn, and the carpet formed using the crimped yarn has insufficient bulkiness. On the other hand, when the single yarn fineness exceeds 25 dtex, it is difficult to obtain the yarn physical properties of the original polylactic acid crimped yarn of the present invention, and the properties of polylactic acid that are hard and brittle are likely to appear, and the crimped yarn The carpet constructed using the material has insufficient wear resistance. Such a tendency becomes conspicuous as the degree of deformity of the cross-sectional shape of the polylactic acid fiber increases at the same single yarn fineness. Therefore, it is preferable that the single fiber has a smaller degree of deformity. Among these, the single yarn fineness of the original polylactic acid crimped yarn is preferably in the range of 4 to 20 dtex, more preferably in the range of 5 to 15 dtex. In addition, within the range of the single yarn fineness of 2.5 to 25 dtex, as the single yarn fineness decreases, the property that the polylactic acid is hard and brittle can be further reduced, and the strength and elongation of the original polylactic acid crimped yarn can be reduced. Can be further improved, and the wear resistance of the carpet can be improved.
また、前記原着ポリ乳酸捲縮糸の熱水収縮率は2〜8%の範囲である。熱水収縮率が2%未満では、ポリ乳酸捲縮糸の結晶化度が高くなり、ポリ乳酸の硬くて脆いという性状が出やすくなり、強度と伸度がバランス良く発現しないし、カーペットとした時の耐摩耗性が不十分である。一方、熱水収縮率が8%を超えると、原着ポリ乳酸捲縮糸の熱セット処理時に糸収縮が発生するし、またカーペット製造における各工程での管理に困難を生じ易いという問題がある。中でも、前記原着ポリ乳酸捲縮糸の熱水収縮率は3〜6%の範囲であるのが好ましい。 The hot-water shrinkage rate of the original polylactic acid crimped yarn is in the range of 2 to 8%. If the hot water shrinkage is less than 2%, the degree of crystallinity of the polylactic acid crimped yarn becomes high, the polylactic acid tends to be hard and brittle, the strength and elongation are not well-balanced, and the carpet is made. Insufficient wear resistance. On the other hand, if the hot water shrinkage rate exceeds 8%, yarn shrinkage occurs during the heat setting process of the original polylactic acid crimped yarn, and there is a problem in that it is difficult to manage each step in carpet manufacturing. . Especially, it is preferable that the hot water shrinkage rate of the original polylactic acid crimped yarn is in the range of 3 to 6%.
また、前記原着ポリ乳酸捲縮糸の乾熱捲縮率は5〜25%の範囲である。この乾熱捲縮率は、原着ポリ乳酸捲縮糸の嵩高性を示すパラメーターであり、原着ポリ乳酸捲縮糸を100℃の熱風で処理して捲縮を発現させ、その捲縮の程度を示した値である。乾熱捲縮率が5%未満では、捲縮が不十分であり、カーペットとした時の嵩高性が不十分となるし、耐ヘタリ性に劣ったものとなる。一方、乾熱捲縮率が25%を超えるポリ乳酸捲縮糸は、現在の製造技術では得られ難いし、得られたとしても、該捲縮糸を用いて構成したカーペットは、フェルト様になる。中でも、前記原着ポリ乳酸捲縮糸の乾熱捲縮率は8〜20%の範囲であるのが好ましい。 Further, the dry heat crimp rate of the original polylactic acid crimped yarn is in the range of 5 to 25%. This dry heat crimp rate is a parameter indicating the bulkiness of the original polylactic acid crimped yarn, and the original polylactic acid crimped yarn is treated with hot air at 100 ° C. to develop the crimp. It is a value indicating the degree. If the dry heat crimp rate is less than 5%, the crimp is insufficient, the bulkiness of the carpet is insufficient, and the anti-sag property is poor. On the other hand, polylactic acid crimped yarns having a dry heat crimp rate of more than 25% are difficult to obtain with the current production technology. Even if obtained, the carpet formed using the crimped yarn is felt-like. Become. Among these, the dry heat crimp rate of the original polylactic acid crimped yarn is preferably in the range of 8 to 20%.
また、前記着色剤としては、例えば、無機顔料、有機顔料等が挙げられ、捲縮糸に色彩を与え得るものであれば特に限定されない。前記無機顔料としては、例えば、酸化チタン、亜鉛華、チタンイエロー、亜鉛−鉄系ブラウン、チタン・コバルト系グリーン、コバルトグリーン、コバルトブルー、銅−鉄系ブラウン等の酸化物、紺青等のフェロシアン化物、群青等の珪酸塩、炭酸カルシウム等の炭酸塩、マンガンバイオレット等の燐酸塩、カーボンブラック、アルミニウム粉、ブロンズ粉、チタン粉末被覆雲母等が挙げられる。また、前記有機顔料としては、例えば、銅フタロシアニンブルー、銅フタロシアニングリーン、臭素化銅フタロシアニングリーン等のフタロシアニン系、ペリレンスカーレット、ペリレンレア、ペリレンマルーン等のペリレン系、イソインドリノン系等が挙げられる。 Examples of the colorant include inorganic pigments and organic pigments, and are not particularly limited as long as they can give color to the crimped yarn. Examples of the inorganic pigment include oxides such as titanium oxide, zinc white, titanium yellow, zinc-iron brown, titanium / cobalt green, cobalt green, cobalt blue, copper-iron brown, and ferrocyans such as bitumen. Silicates, ultramarine silicates, carbonates such as calcium carbonate, manganese violet phosphates, carbon black, aluminum powder, bronze powder, titanium powder-coated mica, and the like. Examples of the organic pigment include phthalocyanine series such as copper phthalocyanine blue, copper phthalocyanine green, brominated copper phthalocyanine green, perylene series such as perylene scarlet, perylene rare, and perylene maroon, and isoindolinone series.
中でも、無機顔料及び有機顔料からなる群より選ばれた少なくとも1種の顔料を用いるのが好ましい。中でも特に好ましいのは、前記着色剤として、カーボンブラック、酸化物系無機顔料、フェロシアン化物系無機顔料、珪酸塩系無機顔料、炭酸塩系無機顔料、燐酸塩系無機顔料、フタロシアニン系有機顔料、ペリレン系有機顔料及びイソインドリノン系有機顔料からなる群より選ばれた少なくとも1種の顔料を用いる構成である。 Among these, it is preferable to use at least one pigment selected from the group consisting of inorganic pigments and organic pigments. Among them, as the colorant, carbon black, oxide-based inorganic pigment, ferrocyanide-based inorganic pigment, silicate-based inorganic pigment, carbonate-based inorganic pigment, phosphate-based inorganic pigment, phthalocyanine-based organic pigment, In this configuration, at least one pigment selected from the group consisting of perylene organic pigments and isoindolinone organic pigments is used.
次に、上記特徴を備えた原着ポリ乳酸捲縮糸を製造する方法について説明する。 Next, a method for producing an original polylactic acid crimped yarn having the above characteristics will be described.
まず、ポリ乳酸を紡糸して紡糸糸を得る(紡糸工程)。例えば、図1に示すように、ポリ乳酸投入口(10)からポリ乳酸を投入すると共に着色剤投入口(11)から着色剤(顔料等)を投入してベント(13)付き押出機(12)内で溶融混練した後、紡糸ヘッド(14)の先端に取り付けられた紡糸口金(15)から押出してフィラメントを形成する。この時、得られるフィラメントの断面形状が異形度1.5未満の略円形状または円形状になるように紡糸口金(15)の孔の形状を適切に設計する。また、着色剤の混合量は、着色剤含有率が0.01〜3質量%の範囲となるようにする。前記押出機(12)における溶融混練温度は210〜235℃に設定するのが好ましい。前記ポリ乳酸としては、相対粘度が2.8〜3.8であるものを用いる。好ましくは3.0〜3.6であるものを用いる。前記相対粘度は、20℃、フェノール/テトラクロロエタン=60/40(質量比)の混合溶液で測定した値である。相対粘度が2.8〜3.8であるものを用いる理由は、前述したのと同様である。なお、前記着色剤としては、着色剤を予めポリ乳酸に添加したマスターバッチとしたものを使用しても良い。 First, polylactic acid is spun to obtain a spun yarn (spinning step). For example, as shown in FIG. 1, the polylactic acid is charged from the polylactic acid charging port (10) and the colorant (pigment or the like) is charged from the coloring agent charging port (11). ), And then extruded from a spinneret (15) attached to the tip of the spinning head (14) to form a filament. At this time, the shape of the hole of the spinneret (15) is appropriately designed so that the cross-sectional shape of the obtained filament is a substantially circular shape or a circular shape having a degree of irregularity of less than 1.5. Moreover, the mixing amount of the colorant is set so that the colorant content is in the range of 0.01 to 3% by mass. The melt kneading temperature in the extruder (12) is preferably set to 210 to 235 ° C. As the polylactic acid, one having a relative viscosity of 2.8 to 3.8 is used. Those having a viscosity of 3.0 to 3.6 are preferably used. The relative viscosity is a value measured with a mixed solution of 20 ° C. and phenol / tetrachloroethane = 60/40 (mass ratio). The reason for using the one having a relative viscosity of 2.8 to 3.8 is the same as described above. In addition, as the colorant, a masterbatch obtained by adding a colorant to polylactic acid in advance may be used.
ポリ乳酸は、一般には、そのポリマー中の公定水分率が0.4〜0.5質量%(4000〜5000ppm)である。ポリ乳酸を溶融紡糸に用いるためには、ポリ乳酸中の含有水分率が0.01質量%(100ppm)以下であるのが好ましく、0.005質量%(50ppm)以下であるのがより好ましい。従って、例えば、真空熱風乾燥機を使用して100〜130℃で約5時間以上乾燥することによってポリ乳酸中の水分を低減する。なお、前記押出機(12)としてベント付き二軸押出機を用いる場合には、未乾燥ポリ乳酸の使用が十分に可能であり、ポリ乳酸の相対粘度を保持しながら溶融紡糸することができる。 Polylactic acid generally has an official moisture content in the polymer of 0.4 to 0.5% by mass (4000 to 5000 ppm). In order to use polylactic acid for melt spinning, the water content in the polylactic acid is preferably 0.01% by mass (100 ppm) or less, and more preferably 0.005% by mass (50 ppm) or less. Therefore, for example, the moisture in the polylactic acid is reduced by drying at 100 to 130 ° C. for about 5 hours or more using a vacuum hot air dryer. When a biaxial extruder with a vent is used as the extruder (12), undried polylactic acid can be sufficiently used, and melt spinning can be performed while maintaining the relative viscosity of polylactic acid.
なお、前記紡糸口金(15)の孔の形状や寸法は、ポリ乳酸の溶融粘度、紡糸温度、紡糸後の冷却条件等を考慮して、目的とする原着ポリ乳酸捲縮糸が得られるように設計する。 The shape and dimensions of the holes of the spinneret (15) are such that the intended original polylactic acid crimped yarn can be obtained in consideration of the melt viscosity of polylactic acid, the spinning temperature, the cooling conditions after spinning, and the like. To design.
次に、前記紡糸口金(15)から押出されたフィラメントを冷風吹付装置(16)からの冷風によって冷却する(図1参照)。冷風の温度は、10〜30℃であるのが好ましく、より好ましくは15〜25℃である。 Next, the filament extruded from the spinneret (15) is cooled by cold air from the cold air blowing device (16) (see FIG. 1). The temperature of the cold air is preferably 10 to 30 ° C, more preferably 15 to 25 ° C.
しかる後、前記フィラメントに油剤付与装置(17)でもって油剤を付与した後、糸を集束して紡糸糸を得る。前記油剤としては、特に限定されるものではないが、例えば平滑剤を主成分とし、乳化剤、帯電防止剤等を含有するもの等が挙げられる。好ましい油剤組成を例示すると、例えば前記平滑剤としてはネオペンチルグリコールジオレエートが好ましく、前記乳化剤としてはポリオキシエチレンヒマシ油、ポリオキシアルキレンソルビタンエステルが好ましく、前記帯電防止剤としてはポリオキシエチレンアルキルホスフェート塩が好ましい。また、必要に応じ、酸化防止剤、紫外線吸収剤等の添加剤が前記油剤に添加されていても良い。前記油剤における各成分の好適な含有比率は、平滑剤35〜75質量%、乳化剤20〜60質量%、帯電防止剤0.5〜8質量%である。 Thereafter, an oil agent is applied to the filament by an oil agent applying device (17), and then the yarns are converged to obtain a spun yarn. Although it does not specifically limit as said oil agent, For example, what has a smoothing agent as a main component and contains an emulsifier, an antistatic agent, etc. is mentioned. Examples of preferred oil composition include, for example, neopentyl glycol dioleate as the smoothing agent, polyoxyethylene castor oil and polyoxyalkylene sorbitan ester as the emulsifier, and polyoxyethylene alkyl as the antistatic agent. Phosphate salts are preferred. Moreover, additives, such as antioxidant and a ultraviolet absorber, may be added to the said oil agent as needed. The suitable content ratio of each component in the oil agent is 35 to 75% by mass of a smoothing agent, 20 to 60% by mass of an emulsifier, and 0.5 to 8% by mass of an antistatic agent.
前記油剤を付与することによって、原着ポリ乳酸捲縮糸の製造における紡糸・延伸工程における強度や伸度の安定的確保及び捲縮工程における捲縮の発現状態の安定性の確保を図ることができる。また、この原着ポリ乳酸捲縮糸を用いたカーペットの静電気発生の抑制、糸表面の摩擦係数低減を図ることができ、これにより該カーペット表皮の耐摩耗性をさらに向上させることができる。 By applying the oil agent, it is possible to stably secure strength and elongation in the spinning / drawing process in the production of the original polylactic acid crimped yarn and to secure stability of the expression state of the crimp in the crimping process. it can. Further, the generation of static electricity on the carpet using the original polylactic acid crimped yarn can be suppressed, and the friction coefficient of the yarn surface can be reduced, whereby the wear resistance of the carpet skin can be further improved.
次いで、前記紡糸糸を所定の速度で回転する引き取りローラ(1)で捲回して引き取る。前記引き取りローラ(1)の引き取り速度は400〜1000m/分であるのが好ましい。引き取り速度が400m/分未満では紡糸時の糸条張力が低くなり過ぎるので好ましくない。一方、引き取り速度が1000m/分を超えると、延伸速度及び捲縮加工が高速となることから、現行の実用プロセスでは製造が困難である。 Next, the spun yarn is wound by a take-up roller (1) that rotates at a predetermined speed. The take-up speed of the take-up roller (1) is preferably 400 to 1000 m / min. If the take-up speed is less than 400 m / min, the yarn tension at the time of spinning becomes too low, which is not preferable. On the other hand, if the take-up speed exceeds 1000 m / min, the drawing speed and crimping process become high, and thus it is difficult to manufacture with the current practical process.
次いで、前記引き取りローラ(1)で引き取られた紡糸糸を、ローラ群(2)(3)(4)を用いて1段または2段以上の多段で熱延伸する。即ち、まず、前記引き取られた紡糸糸を予熱ローラ(2)に導き、この予熱ローラ(2)で紡糸糸の予熱を行う。この時、予熱ローラ(2)の温度を55〜95℃の範囲に設定するのが好ましい。このような温度範囲に設定した場合には均一な予備加熱を実現することができる。中でも、前記予熱ローラ(2)の温度は55〜70℃の範囲に設定するのがより好ましい。 Next, the spun yarn taken up by the take-up roller (1) is hot-drawn in one or more stages using the roller groups (2), (3), and (4). That is, first, the drawn spun yarn is guided to the preheating roller (2), and the preheated roller (2) preheats the spun yarn. At this time, it is preferable to set the temperature of the preheating roller (2) in the range of 55 to 95 ° C. When the temperature is set in such a range, uniform preheating can be realized. Especially, it is more preferable to set the temperature of the preheating roller (2) in the range of 55 to 70 ° C.
しかる後、前記紡糸糸を予熱ローラ(2)から延伸ローラ(3)に導く。この時、延伸ローラ(3)の温度を70〜125℃の範囲に設定する。70℃未満では延伸ムラが生じやすいし、十分に延伸することが困難で糸切れを生じやすい。一方125℃を超えると工程途中で糸に弛みを生じる。前記延伸ローラ(3)の温度は85〜125℃の範囲に設定するのが好ましく、特に好適なのは95〜120℃である。なお、上記温度範囲内において、延伸ローラ(3)の温度は予熱ローラ(2)の温度よりも高い温度に設定する。 Thereafter, the spun yarn is guided from the preheating roller (2) to the drawing roller (3). At this time, the temperature of the stretching roller (3) is set in the range of 70 to 125 ° C. If it is less than 70 ° C., stretching unevenness is likely to occur, and it is difficult to sufficiently stretch, and yarn breakage is likely to occur. On the other hand, when the temperature exceeds 125 ° C., the yarn is slackened during the process. The temperature of the stretching roller (3) is preferably set in the range of 85 to 125 ° C, particularly preferably 95 to 120 ° C. In addition, within the said temperature range, the temperature of the extending | stretching roller (3) is set to a temperature higher than the temperature of the preheating roller (2).
また、延伸倍率は3〜6倍とする。3倍未満では十分な強度が得られなくなるし、6倍を超えると毛羽が顕著に発生するものとなる。中でも、前記延伸倍率は3.5〜5.0倍とするのが好ましい。 Moreover, a draw ratio shall be 3-6 times. If it is less than 3 times, sufficient strength can not be obtained, and if it exceeds 6 times, fluff is remarkably generated. Especially, it is preferable that the said draw ratio shall be 3.5-5.0 times.
前記延伸ローラ(3)の温度を70〜125℃の範囲に設定し、かつ延伸倍率を3〜6倍に設定することにより、本発明の原着ポリ乳酸捲縮糸の高強度・高伸度及び高捲縮特性を得ることが可能となり、これにより捲縮糸をカーペットの構成糸として使用した時のカーペットとしての優れた嵩高性、耐摩耗性を実現できる。 By setting the temperature of the drawing roller (3) in the range of 70 to 125 ° C. and setting the draw ratio to 3 to 6, the high strength and high elongation of the original polylactic acid crimped yarn of the present invention In addition, it is possible to obtain a high crimp property, which makes it possible to realize excellent bulkiness and wear resistance as a carpet when the crimped yarn is used as a constituent yarn of the carpet.
しかる後、前記紡糸糸を延伸ローラ(3)から熱セットローラ(4)に導き、ここで熱セットする。この時、熱セットローラ(4)の温度を100〜150℃の範囲に設定する。このような温度範囲に設定することにより、ポリ乳酸繊維として適度な結晶化を発現させ得て捲縮糸の強度及び伸度ともに向上させることができる。中でも、前記熱セットローラ(4)の温度は105〜140℃の範囲に設定するのが好ましく、さらに好適なのは110〜130℃であり、最も好適なのは110〜125℃である。また、前記熱セットローラ(4)の温度は、100〜150℃の範囲内で、前記延伸ローラ(3)の温度よりも高い温度に設定するのが好ましい。 Thereafter, the spun yarn is guided from the drawing roller (3) to the heat setting roller (4), where it is heat set. At this time, the temperature of the heat setting roller (4) is set in the range of 100 to 150 ° C. By setting to such a temperature range, moderate crystallization can be expressed as a polylactic acid fiber, and both the strength and elongation of the crimped yarn can be improved. Among them, the temperature of the heat setting roller (4) is preferably set in the range of 105 to 140 ° C, more preferably 110 to 130 ° C, and most preferably 110 to 125 ° C. Moreover, it is preferable to set the temperature of the said heat setting roller (4) to the temperature higher than the temperature of the said extending | stretching roller (3) within the range of 100-150 degreeC.
特に、本発明の原着ポリ乳酸捲縮糸の高強度・高伸度及び高捲縮特性を得るためには、前記熱セットローラ(4)の温度をポリ乳酸の軟化点温度(Ts)以下の温度に設定するのが好ましい。即ち、前記熱セットローラ(4)の温度は、100℃以上であって且つポリ乳酸の軟化点温度(Ts)以下の温度に設定するのが好ましい。ポリ乳酸の軟化点温度は130℃程度であるから、換言すれば、前記熱セットローラ(4)の温度は、100〜130℃に設定するのが好ましい。中でも、前記熱セットローラ(4)の温度は、110〜130℃に設定するのがより好ましく、110〜125℃が特に好ましい。 In particular, in order to obtain the high strength, high elongation and high crimp characteristics of the original polylactic acid crimped yarn of the present invention, the temperature of the heat setting roller (4) is lower than the softening point temperature (Ts) of polylactic acid. Preferably, the temperature is set to That is, the temperature of the heat setting roller (4) is preferably set to a temperature not lower than 100 ° C. and not higher than the softening point temperature (Ts) of polylactic acid. Since the softening point temperature of polylactic acid is about 130 ° C., in other words, the temperature of the heat setting roller (4) is preferably set to 100 to 130 ° C. Among them, the temperature of the heat setting roller (4) is more preferably set to 110 to 130 ° C, and particularly preferably 110 to 125 ° C.
次に、前記熱セットが行われた延伸糸を加熱流体捲縮付与装置(5)に導き、該捲縮付与装置(5)によって糸に捲縮を与え嵩高性を付与する(捲縮工程)。前記加熱流体捲縮付与装置(5)は、糸に加熱流体を接触させることによって糸に捲縮を付与せしめる装置であり、前記加熱流体の温度は90〜160℃の範囲に設定する。90℃未満では十分な捲縮を付与できないし、160℃を超えると単糸を融着させることがある。 Next, the drawn yarn subjected to the heat setting is led to a heated fluid crimping device (5), and the crimp is imparted to the yarn by the crimping device (5) to impart bulkiness (crimping step). . The heated fluid crimp imparting device (5) is a device that imparts crimp to the yarn by bringing the heated fluid into contact with the yarn, and the temperature of the heated fluid is set in the range of 90 to 160 ° C. If it is less than 90 ° C., sufficient crimp cannot be imparted, and if it exceeds 160 ° C., the single yarn may be fused.
本実施形態では、前記加熱流体捲縮付与装置(5)は、加熱高圧流体を糸条に噴射して単糸をランダムに交絡させ、3次元クリンプを形成させる加熱流体噴射ノズル装置と、捲縮糸に対して加熱流体の下に圧縮熱処理を行う圧縮熱処理装置とを備えている。圧縮熱処理装置は、金属製板を一定の間隔で積層配置した環状の装置であり、加熱加圧流体は金属製板間より外部へ吸引される。この圧縮熱処理装置内で、糸条は折り畳まれ、積層されながら、一定時間滞留して熱処理される。 In the present embodiment, the heated fluid crimping device (5) includes a heated fluid ejection nozzle device that ejects a heated high-pressure fluid onto the yarn to randomly entangle the single yarn to form a three-dimensional crimp; A compression heat treatment apparatus that performs a compression heat treatment on the yarn under a heating fluid. The compression heat treatment apparatus is an annular apparatus in which metal plates are stacked and arranged at regular intervals, and the heated and pressurized fluid is sucked to the outside from between the metal plates. In this compression heat treatment apparatus, the yarn is folded and laminated, and stays for a certain time and is heat-treated.
前記加熱流体捲縮付与装置(5)で使用する加熱流体としては、例えば過熱蒸気、加熱空気等が挙げられる。中でも、加熱空気を使用するのが好ましい。また、前記加熱空気の温度は90〜160℃の範囲に設定されるが、中でも、100〜140℃の範囲であるのが好ましく、105〜125℃の範囲であるのが特に好ましい。なお、前記加熱流体の温度は、90〜160℃の範囲内で、加熱流体の圧力、流量、捲縮処理対象のポリ乳酸糸の繊度、捲縮処理速度等に応じて適切な条件を選択すれば良い。 Examples of the heating fluid used in the heating fluid crimping device (5) include superheated steam and heated air. Among these, it is preferable to use heated air. Further, the temperature of the heated air is set in a range of 90 to 160 ° C., among which a range of 100 to 140 ° C. is preferable, and a range of 105 to 125 ° C. is particularly preferable. Note that the temperature of the heating fluid is within a range of 90 to 160 ° C., and an appropriate condition is selected according to the pressure and flow rate of the heating fluid, the fineness of the polylactic acid yarn to be crimped, the crimping speed, and the like. It ’s fine.
更に、本発明の原着ポリ乳酸捲縮糸の高強度・高伸度及び高捲縮特性を得るためには、前記加熱流体の温度は、ポリ乳酸の結晶化温度(Tc)以下の温度に設定するのが好ましい。このように加熱流体の温度を、90℃以上であって且つポリ乳酸の結晶化温度(Tc)以下の温度に設定すれば、配向結晶化したポリ乳酸繊維の捲縮付与時の繊維へのダメージが低減され、所望の捲縮特性が確実に得られるものとなる。なお、ポリ乳酸の結晶化温度は115〜120℃程度であるから、換言すれば、前記加熱流体の温度は90〜120℃に設定するのが好ましい。中でも、前記加熱流体の温度は90〜115℃に設定するのが特に好ましい。 Furthermore, in order to obtain the high strength, high elongation and high crimp characteristics of the original polylactic acid crimped yarn of the present invention, the temperature of the heating fluid is set to a temperature below the crystallization temperature (Tc) of polylactic acid. It is preferable to set. Thus, if the temperature of the heating fluid is set to a temperature of 90 ° C. or more and not more than the crystallization temperature (Tc) of polylactic acid, damage to the fibers at the time of crimping of the oriented and crystallized polylactic acid fibers is caused. As a result, the desired crimp characteristics can be reliably obtained. In addition, since the crystallization temperature of polylactic acid is about 115-120 degreeC, in other words, it is preferable to set the temperature of the said heating fluid to 90-120 degreeC. In particular, the temperature of the heating fluid is particularly preferably set to 90 to 115 ° C.
また、前記熱セットローラ(4)の温度を「S」とし、前記加熱流体捲縮付与装置(5)における加熱流体の温度を「R」としたとき、下記関係式
30℃≧ S−R ≧−10℃
を満足することが特に好ましい。このような条件を満足する場合には、得られる原着ポリ乳酸捲縮糸の強度及び伸度ともに向上させることができる。中でも、下記関係式
20℃≧ S−R ≧−10℃
を満足することがより好ましく、特に好ましいのは15℃≧S−R≧−10℃の関係を満足する構成である。
Further, when the temperature of the heat setting roller (4) is “S” and the temperature of the heating fluid in the heating fluid crimping device (5) is “R”, the following relational expression: 30 ° C. ≧ SR− ≧ -10 ° C
It is particularly preferable to satisfy When such conditions are satisfied, both the strength and elongation of the original polylactic acid crimped yarn obtained can be improved. Above all, the following
Is more preferable, and a configuration satisfying the relationship of 15 ° C. ≧ S−R ≧ −10 ° C. is particularly preferable.
次に、前記加熱流体捲縮付与装置(5)で捲縮が付与された捲縮糸(6)を冷却ドラム(20)で冷却する。本実施形態では、この冷却ドラム(20)上に噴出された捲縮糸(6)は、冷却ドラム(20)表面に穿設された孔で吸引冷却されながら移送される。この冷却により、前記捲縮糸(6)を該糸のガラス転移温度(Tg)(57〜60℃)よりも低い温度まで冷却するのが望ましい。これにより、時間が経過しても捲縮が緩まない十分な捲縮が付与された原着ポリ乳酸捲縮糸を製造することができる。中でも、前記捲縮糸(6)を冷却ドラム(20)で30〜55℃まで冷却するのが好ましい。 Next, the crimped yarn (6) that has been crimped by the heated fluid crimping device (5) is cooled by a cooling drum (20). In the present embodiment, the crimped yarn (6) ejected onto the cooling drum (20) is transferred while being cooled by suction through holes formed in the surface of the cooling drum (20). It is desirable to cool the crimped yarn (6) to a temperature lower than the glass transition temperature (Tg) (57 to 60 ° C.) of the yarn by this cooling. As a result, it is possible to produce an original polylactic acid crimped yarn to which sufficient crimp is applied so that the crimp does not loosen over time. Especially, it is preferable to cool the said crimped yarn (6) to 30-55 degreeC with a cooling drum (20).
しかる後、前記捲縮糸を交絡処理装置(21)のノズルを通過させて交絡処理する。交絡ノズルから走行捲縮糸条に対して略直角方向から0.2〜0.5MPaの高圧空気を噴射させて交絡処理するのが良い。 Thereafter, the crimped yarn is entangled by passing through the nozzle of the entanglement processing device (21). It is preferable to perform the entanglement process by injecting high pressure air of 0.2 to 0.5 MPa from a direction substantially perpendicular to the running crimped yarn from the entanglement nozzle.
次いで、交絡処理後の捲縮糸をワインダー(22)に巻き取る。この時の巻き取り張力は、0.10cN/dtex以下とするのが好ましい。中でも、巻き取り張力は0.02〜0.07cN/dtexの範囲であるのがより好ましく、さらには0.03〜0.05cN/dtexの範囲が特に好ましい。 Next, the crimped yarn after the entanglement process is wound around a winder (22). The winding tension at this time is preferably 0.10 cN / dtex or less. Among these, the winding tension is more preferably in the range of 0.02 to 0.07 cN / dtex, and further preferably in the range of 0.03 to 0.05 cN / dtex.
上記のようにして得られた原着ポリ乳酸捲縮糸は、嵩高性に優れ、高タフネスで耐摩耗性に優れているから、例えばカーペットの構成糸として好適に用いられる。例えば、得られた原着ポリ乳酸捲縮糸は、基布にタフトされてカーペットに構成される。前記基布としては、特に限定されるものではないが、例えばポリエステル不織布、ポリプロピレン不織布の他、ポリ乳酸繊維からなる不織布等が挙げられる。中でも、前記基布としてはポリ乳酸繊維からなる不織布を用いるのが好ましく、この場合には、使用後廃棄された際にタフトカーペットの全体が微生物等により分解されるので地球環境保護に十分に貢献することができる。 Since the original polylactic acid crimped yarn obtained as described above is excellent in bulkiness, high toughness and excellent in abrasion resistance, it is suitably used as a constituent yarn for carpets, for example. For example, the obtained original polylactic acid crimped yarn is tufted into a base fabric to form a carpet. Although it does not specifically limit as said base fabric, For example, the nonwoven fabric etc. which consist of a polylactic acid fiber other than a polyester nonwoven fabric and a polypropylene nonwoven fabric etc. are mentioned. Among them, it is preferable to use a non-woven fabric made of polylactic acid fibers as the base fabric. In this case, the entire tuft carpet is decomposed by microorganisms and the like when discarded after use, thus contributing to the protection of the global environment. can do.
なお、この発明に係る原着ポリ乳酸捲縮糸は、上記例示した製造方法で製造されたものに特に限定されるものではない。 The original polylactic acid crimped yarn according to the present invention is not particularly limited to those produced by the production method exemplified above.
この発明の原着ポリ乳酸捲縮糸は、撚糸、無撚糸いずれの状態で用いても良く、また例えば無撚糸を他の無撚糸とエアーエンタングル設備で混繊して混繊糸形態で用いることもできる。また、この発明の原着ポリ乳酸捲縮糸は、他のナイロン捲縮糸、ポリプロピレン捲縮糸、ポリエステル捲縮糸等と合撚して合撚糸となし、これをカーペットの構成糸として用いることもできる。環境対応のリサイクルを十分に考慮すると、カーペットの他の構成素材(原着ポリ乳酸捲縮糸以外の素材)としては、PET(ポリエチレンテレフタレート)等のポリエステルを用いるのが好ましい。 The original polylactic acid crimped yarn of the present invention may be used in either a twisted or untwisted state. For example, the untwisted yarn may be mixed with other untwisted yarns using an air entanglement equipment and used in the form of mixed yarn. You can also. The original polylactic acid crimped yarn of the present invention is twisted with other nylon crimped yarns, polypropylene crimped yarns, polyester crimped yarns, etc. to form a twisted yarn, which is used as a constituent yarn of the carpet. You can also. Considering environmentally friendly recycling, it is preferable to use polyester such as PET (polyethylene terephthalate) as the other constituent material of the carpet (a material other than the original polylactic acid crimped yarn).
また、この発明の原着ポリ乳酸捲縮糸を2または3本用い、上撚り、下撚りを施して撚り捲縮糸(撚り数は150〜250回/mが好ましい)とした後、100〜125℃の熱風処理又は90〜115℃の真空蒸気熱処理を行うことによって、撚り止めを行うと共に捲縮糸の嵩高性、耐摩耗性及び耐へたり性をさらに向上せしめた捲縮糸を得て、該捲縮糸をタフトして高級カーペットを構成することもできる。 In addition, two or three of the original polylactic acid crimped yarns of the present invention were used, and an upper twist and a lower twist were applied to obtain a twisted crimped yarn (the number of twists is preferably 150 to 250 times / m), and then 100 to By performing hot air treatment at 125 ° C. or vacuum steam heat treatment at 90 to 115 ° C., a crimped yarn is obtained that is twisted and further improved in bulkiness, wear resistance and sag resistance of the crimped yarn. The crimped yarn can be tufted to constitute a high-grade carpet.
この発明の原着ポリ乳酸捲縮糸及びこの発明の製造方法で得られた原着ポリ乳酸捲縮糸は、例えばカーペットの構成糸として好適に用いられる。しかして、この発明の原着ポリ乳酸捲縮糸を用いて構成したカーペット及びこの発明の製造方法で得られた原着ポリ乳酸捲縮糸を用いて構成したカーペットは、十分な嵩高性及び十分なボリューム感を有したものとなると共に耐摩耗性及び耐ヘタリ性にも優れたものとなる。 The original polylactic acid crimped yarn of the present invention and the original polylactic acid crimped yarn obtained by the production method of the present invention are suitably used as, for example, a constituent yarn of a carpet. Thus, the carpet constituted by using the original polylactic acid crimped yarn of the present invention and the carpet constituted by using the original polylactic acid crimped yarn obtained by the production method of the present invention have sufficient bulkiness and sufficient As well as having a good volume feeling, it also has excellent wear resistance and sag resistance.
ここで用いられた用語及び説明は、この発明に係る実施形態を説明するために用いられたものであって、この発明はこれに限定されるものではない。この発明は請求の範囲内であれば、その精神を逸脱するものでない限りいかなる設計的変更をも許容するものである。 The terms and explanations used here are used to describe the embodiments of the present invention, and the present invention is not limited to these. Within the scope of the claims, the present invention allows any design changes without departing from the spirit thereof.
次に、この発明の具体的実施例について説明するが、本発明はこれら実施例のものに特に限定されるものではない。 Next, specific examples of the present invention will be described, but the present invention is not particularly limited to these examples.
<実施例1>
図1に示す構成からなる製造装置を用いてポリ乳酸捲縮糸を製造した。即ち、まずポリ乳酸投入口(10)からポリ乳酸チップ(L−乳酸98質量%とD−乳酸2質量%からなる乳酸モノマーの重合体、重量平均分子量140000、相対粘度3.2、ガラス転移温度Tg:57℃、融点Tm:170℃、軟化点温度Ts:130℃、結晶化温度Tc:115℃)100質量部を投入する一方、着色剤投入口(11)からカーボンブラックのマスターバッチ(前記ポリ乳酸75質量%、カーボンブラック25質量%の組成)4質量部を投入してベント(13)付き2軸押出機(12)内で脱気しながら230℃で溶融混練した後、2軸押出機(12)の先端に取り付けられた紡糸口金(15)の64個の円形断面(丸断面)のノズルから紡糸ビーム温度225℃で押出して3口金分をまとめて紡糸した。
<Example 1>
A polylactic acid crimped yarn was produced using a production apparatus having the structure shown in FIG. That is, first, a polylactic acid chip (a polymer of lactic acid monomer composed of 98% by mass of L-lactic acid and 2% by mass of D-lactic acid, a weight average molecular weight of 140000, a relative viscosity of 3.2, a glass transition temperature from a polylactic acid charging port (10). Tg: 57 ° C., melting point Tm: 170 ° C., softening point temperature Ts: 130 ° C., crystallization temperature Tc: 115 ° C.) 100 parts by mass, while carbon black masterbatch (from the colorant inlet (11)) (Composition of 75% by mass of polylactic acid and 25% by mass of carbon black) 4 parts by mass were melt-kneaded at 230 ° C. while degassing in a biaxial extruder (12) with a vent (13), and then biaxial extrusion The spinneret (15) attached to the tip of the machine (12) was extruded from 64 nozzles having a circular cross section (round cross section) at a spinning beam temperature of 225 ° C., and the three bases were spun together.
次に、紡糸された糸条を冷風吹付装置(16)からの冷風(20℃70%RH)によって冷却・固化し、丸断面フィラメント192本からなるマルチフィラメント糸を得た。次いで、前記糸条に油剤付与装置(17)でもって油剤を付与し、糸を集束し、速度462m/分の速度で回転する非加熱の引き取りローラ(1)に捲回して引き取った後、速度462m/分・温度70℃に設定された予熱ローラ(2)で糸の予熱を行った。 Next, the spun yarn was cooled and solidified by cold air (20 ° C., 70% RH) from a cold air spraying device (16) to obtain a multifilament yarn comprising 192 round cross-section filaments. Next, an oil agent is applied to the yarn with an oil agent applicator (17), the yarn is focused, wound on an unheated take-up roller (1) rotating at a speed of 462 m / min, and then taken up. The yarn was preheated with a preheating roller (2) set at 462 m / min and a temperature of 70 ° C.
しかる後、前記紡糸糸を速度489m/分・温度105℃に設定された延伸ローラ(3)に捲回し、速度2200m/分・温度120℃に設定された熱セットローラ(4)との間で延伸を行った。延伸倍率は4.5倍であった。熱セットローラ(4)の温度は、ポリ乳酸の軟化点温度Tsよりも低い120℃とした。 Thereafter, the spun yarn is wound around a drawing roller (3) set at a speed of 489 m / min and a temperature of 105 ° C., and between the heat setting roller (4) set at a speed of 2200 m / min and a temperature of 120 ° C. Stretching was performed. The draw ratio was 4.5 times. The temperature of the heat setting roller (4) was 120 ° C. lower than the softening point temperature Ts of polylactic acid.
次に、熱セットが行われた延伸糸を加熱流体捲縮付与装置(5)内に導き、110℃、0.6MPaの加熱加圧空気を接触させて糸に捲縮を付与した後、この捲縮糸を冷却ドラム(20)で30℃まで冷却した。前記加熱加圧空気の温度は、ポリ乳酸の結晶化温度Tcよりも低い110℃とした。次いで、捲縮糸に交絡処理装置(21)で30個/mの交絡処理を行い、0.05cN/dtexの巻き取り張力で速度1910m/分のワインダー(22)に巻き取って、原着ポリ乳酸捲縮糸を得た。 Next, the drawn yarn subjected to heat setting is introduced into the heated fluid crimping device (5), and heated and pressurized air at 110 ° C. and 0.6 MPa is brought into contact with the yarn to crimp this yarn. The crimped yarn was cooled to 30 ° C. with a cooling drum (20). The temperature of the heated and pressurized air was 110 ° C., which is lower than the crystallization temperature Tc of polylactic acid. Next, the crimped yarn is subjected to an entanglement treatment of 30 pcs / m with an entanglement processing device (21), wound on a winder (22) with a winding tension of 0.05 cN / dtex and a speed of 1910 m / min. A lactic acid crimped yarn was obtained.
得られた原着ポリ乳酸捲縮糸は、総繊度1448dtex/192フィラメント(単糸繊度7.5dtex)の丸断面糸で、相対粘度が3.0、強度が3.12cN/dtex、伸度が46.6%、熱水収縮率が4.5%、乾熱捲縮率が11.2%であった。 The obtained original polylactic acid crimped yarn is a round cross-section yarn having a total fineness of 1448 dtex / 192 filament (single yarn fineness 7.5 dtex), a relative viscosity of 3.0, a strength of 3.12 cN / dtex, and an elongation of The shrinkage percentage was 46.6%, the hot water shrinkage ratio was 4.5%, and the dry heat crimp percentage was 11.2%.
得られた原着ポリ乳酸捲縮糸を2本用い、撚り数180回/mで下撚りと上撚りを施し合撚糸とした後、115℃の熱風処理で撚り止めを行い、カーペット用のパイル糸とした。このパイル糸を用いて、ゲージ:1/10(2.54cm/10針)、ステッチ:48本/10cm、パイル長さ:10mm、パイル部目付:1500g/m2の規格でカットパイルを備えたタフテッドカーペットを得た。 Using two of the original polylactic acid crimped yarns obtained, after twisting and twisting at a twist rate of 180 times / m to make a combined twisted yarn, it was twisted by hot air treatment at 115 ° C., and piled for carpet It was a thread. Using this pile yarn, a cut pile was provided according to the standards of gauge: 1/10 (2.54 cm / 10 needle), stitch: 48 pieces / 10 cm, pile length: 10 mm, pile unit weight: 1500 g / m 2 . I got a tufted carpet.
<実施例2>
図1に示す構成からなる製造装置を用いてポリ乳酸捲縮糸を製造した。即ち、まずポリ乳酸投入口(10)からポリ乳酸チップ(L−乳酸98質量%とD−乳酸2質量%からなる乳酸モノマーの重合体、重量平均分子量140000、相対粘度3.2、ガラス転移温度Tg:57℃、融点Tm:170℃、軟化点温度Ts:130℃、結晶化温度Tc:115℃)100質量部を投入する一方、着色剤投入口(11)からカーボンブラックのマスターバッチ(前記ポリ乳酸75質量%、カーボンブラック25質量%の組成)4質量部を投入してベント(13)付き2軸押出機(12)内で脱気しながら230℃で溶融混練した後、2軸押出機(12)の先端に取り付けられた紡糸口金(15)の64個の円形断面(丸断面)のノズルから紡糸ビーム温度225℃で押出して3口金分をまとめて紡糸した。
<Example 2>
A polylactic acid crimped yarn was produced using a production apparatus having the structure shown in FIG. That is, first, a polylactic acid chip (a polymer of lactic acid monomer composed of 98% by mass of L-lactic acid and 2% by mass of D-lactic acid, a weight average molecular weight of 140000, a relative viscosity of 3.2, a glass transition temperature from a polylactic acid charging port (10). Tg: 57 ° C., melting point Tm: 170 ° C., softening point temperature Ts: 130 ° C., crystallization temperature Tc: 115 ° C.) 100 parts by mass, while carbon black masterbatch (from the colorant inlet (11)) (Composition of 75% by mass of polylactic acid and 25% by mass of carbon black) 4 parts by mass were melt-kneaded at 230 ° C. while degassing in a biaxial extruder (12) with a vent (13), and then biaxial extrusion The spinneret (15) attached to the tip of the machine (12) was extruded from 64 nozzles having a circular cross section (round cross section) at a spinning beam temperature of 225 ° C., and the three bases were spun together.
次に、紡糸された糸条を冷風吹付装置(16)からの冷風(20℃70%RH)によって冷却・固化し、丸断面フィラメント192本からなるマルチフィラメント糸を得た。次いで、前記糸条に油剤付与装置(17)でもって油剤を付与し、糸を集束し、速度510m/分の速度で回転する非加熱の引き取りローラ(1)に捲回して引き取った後、速度516m/分・温度95℃に設定された予熱ローラ(2)で糸の予熱を行った。 Next, the spun yarn was cooled and solidified by cold air (20 ° C., 70% RH) from a cold air spraying device (16) to obtain a multifilament yarn comprising 192 round cross-section filaments. Subsequently, an oil agent is applied to the yarn with an oil agent applying device (17), the yarn is focused, wound on an unheated take-up roller (1) rotating at a speed of 510 m / min, and then taken up. The yarn was preheated with a preheating roller (2) set at 516 m / min and temperature 95 ° C.
しかる後、前記紡糸糸を速度524m/分・温度110℃に設定された延伸ローラ(3)に捲回し、速度2200m/分・温度125℃に設定された熱セットローラ(4)との間で延伸を行った。延伸倍率は4.3倍であった。熱セットローラ(4)の温度は、ポリ乳酸の軟化点温度Tsよりも低い125℃とした。 Thereafter, the spun yarn is wound around a drawing roller (3) set at a speed of 524 m / min and a temperature of 110 ° C., and between the heat setting roller (4) set at a speed of 2200 m / min and a temperature of 125 ° C. Stretching was performed. The draw ratio was 4.3 times. The temperature of the heat setting roller (4) was set to 125 ° C. lower than the softening point temperature Ts of polylactic acid.
次に、熱セットが行われた延伸糸を加熱流体捲縮付与装置(5)内に導き、115℃、0.6MPaの加熱加圧空気を接触させて糸に捲縮を付与した後、この捲縮糸を冷却ドラム(20)で30℃まで冷却した。前記加熱加圧空気の温度は、ポリ乳酸の結晶化温度Tcと同じ115℃とした。次いで、捲縮糸に交絡処理装置(21)で25個/mの交絡処理を行い、0.05cN/dtexの巻き取り張力で速度1636m/分のワインダー(22)に巻き取って、原着ポリ乳酸捲縮糸を得た。 Next, the drawn yarn subjected to heat setting is introduced into the heated fluid crimping device (5), and heated and pressurized air at 115 ° C. and 0.6 MPa is contacted to impart crimp to the yarn. The crimped yarn was cooled to 30 ° C. with a cooling drum (20). The temperature of the heated and pressurized air was 115 ° C. which is the same as the crystallization temperature Tc of polylactic acid. Next, the crimped yarn is subjected to an entanglement treatment of 25 pcs / m with an entanglement processing device (21), wound on a winder (22) with a winding tension of 0.05 cN / dtex and a speed of 1636 m / min. A lactic acid crimped yarn was obtained.
得られた原着ポリ乳酸捲縮糸は、総繊度3200dtex/192フィラメント(単糸繊度16.7dtex)の丸断面糸で、相対粘度が3.0、強度が1.84cN/dtex、伸度が53.1%、熱水収縮率が3.8%、乾熱捲縮率が12.3%であった。 The obtained original polylactic acid crimped yarn is a round cross-section yarn having a total fineness of 3200 dtex / 192 filament (single yarn fineness of 16.7 dtex), a relative viscosity of 3.0, a strength of 1.84 cN / dtex, and an elongation of It was 53.1%, the hot water shrinkage was 3.8%, and the dry heat crimp was 12.3%.
得られた原着ポリ乳酸捲縮糸を用い、撚り数180回/mで撚りを施した後、95℃の真空蒸気で熱処理して撚り止めを行い、カーペット用のパイル糸とした。このパイル糸を用いて、ゲージ:1/10(2.54cm/10針)、ステッチ:44本/10cm、パイル長さ:10mm、パイル部目付:1500g/m2の規格でカットパイルを備えたタフテッドカーペットを得た。 The obtained original polylactic acid crimped yarn was twisted at a twist number of 180 times / m, and then heat-treated with vacuum steam at 95 ° C. to be twisted to obtain a pile yarn for carpet. Using this pile yarn, a cut pile was prepared according to the standards of gauge: 1/10 (2.54 cm / 10 needle), stitch: 44 pieces / 10 cm, pile length: 10 mm, pile unit weight: 1500 g / m 2 . I got a tufted carpet.
<実施例3>
単繊維の断面形状が異形度1.4の略円形状である糸を用いた以外は、実施例1と同様にして原着ポリ乳酸捲縮糸を製造した。得られた原着ポリ乳酸捲縮糸の特性は表1に示したとおりである。また、得られた原着ポリ乳酸捲縮糸を用いて、実施例1と同様にしてタフテッドカーペットを得た。
<Example 3>
An original polylactic acid crimped yarn was produced in the same manner as in Example 1 except that a yarn having a cross-sectional shape of a single fiber and a substantially circular shape with a degree of profile of 1.4 was used. The properties of the obtained original polylactic acid crimped yarn are as shown in Table 1. In addition, a tufted carpet was obtained in the same manner as in Example 1 by using the obtained original polylactic acid crimped yarn.
<実施例4>
単糸繊度が4.1dtexである糸を用いた以外は、実施例1と同様にして原着ポリ乳酸捲縮糸を製造した。得られた原着ポリ乳酸捲縮糸の特性は表1に示したとおりである。また、得られた原着ポリ乳酸捲縮糸を用いて、実施例1と同様にしてタフテッドカーペットを得た。
<Example 4>
An original polylactic acid crimped yarn was produced in the same manner as in Example 1 except that a yarn having a single yarn fineness of 4.1 dtex was used. The properties of the obtained original polylactic acid crimped yarn are as shown in Table 1. In addition, a tufted carpet was obtained in the same manner as in Example 1 by using the obtained original polylactic acid crimped yarn.
<参考例、比較例2>
表1に示す条件で製造するものとした以外は、実施例1と同様にして原着ポリ乳酸捲縮糸を製造した。得られた原着ポリ乳酸捲縮糸の特性は表1に示したとおりである。また、得られた原着ポリ乳酸捲縮糸を用いて、実施例1と同様にしてタフテッドカーペットを得た。
< Reference Example , Comparative Example 2>
An original polylactic acid crimped yarn was produced in the same manner as in Example 1 except that it was produced under the conditions shown in Table 1. The properties of the obtained original polylactic acid crimped yarn are as shown in Table 1. In addition, a tufted carpet was obtained in the same manner as in Example 1 by using the obtained original polylactic acid crimped yarn.
<比較例1>
紡糸口金(15)として、32個の略Y字形状断面のノズルを備えた紡糸口金を用いた以外は、実施例1と同様にして原着ポリ乳酸捲縮糸を製造した。
<Comparative Example 1>
An original polylactic acid crimped yarn was produced in the same manner as in Example 1 except that a spinneret provided with 32 nozzles having a substantially Y-shaped cross section was used as the spinneret (15).
得られた原着ポリ乳酸捲縮糸は、総繊度1100dtex/96フィラメント(単糸繊度11.5dtex)の異形度2.2の異形断面糸で、相対粘度が3.0、強度が1.54cN/dtex、伸度が32.0%、熱水収縮率が4.1%、乾熱捲縮率が12.3%であった。 The obtained original polylactic acid crimped yarn is a modified cross-sectional yarn having a total fineness of 1100 dtex / 96 filaments (single yarn fineness of 11.5 dtex) and a modified degree of 2.2, having a relative viscosity of 3.0 and a strength of 1.54 cN. / Dtex, elongation was 32.0%, hot water shrinkage was 4.1%, and dry heat crimp was 12.3%.
得られた原着ポリ乳酸捲縮糸を3本合撚して合撚糸とした後、115℃の熱風処理で撚り止めを行い、カーペット用のパイル糸とした。このパイル糸を用いて、ゲージ:1/10(2.54cm/10針)、ステッチ:44本/10cm、パイル長さ:10mm、パイル部目付:1500g/m2の規格でカットパイルを備えたタフテッドカーペットを得た。 Three of the obtained original polylactic acid crimped yarns were twisted into a twisted yarn, which was then twisted by hot air treatment at 115 ° C. to obtain a pile yarn for carpet. Using this pile yarn, a cut pile was prepared according to the standards of gauge: 1/10 (2.54 cm / 10 needle), stitch: 44 pieces / 10 cm, pile length: 10 mm, pile unit weight: 1500 g / m 2 . I got a tufted carpet.
<比較例3>
図1に示す構成からなる製造装置におけるポリ乳酸投入口(10)からポリ乳酸チップ(L−乳酸98質量%とD−乳酸2質量%からなる乳酸モノマーの重合体、重量平均分子量220000、相対粘度4.0)100質量部を投入する一方、着色剤投入口(11)からカーボンブラックのマスターバッチ(前記ポリ乳酸75質量%、カーボンブラック25質量%の組成)4質量部を投入してベント(13)付き2軸押出機(12)内で脱気しながら230℃で溶融混練した。2軸押出機(12)の出口でのポリ乳酸の溶融粘度が高すぎるために、ポリマー管温度225℃の紡糸ヘッド(14)までのポリマー管内での圧力損失が大きく、紡糸ヘッド(14)出口でポリ乳酸の吐出量ムラが顕著に発生した。そこで、2軸押出機(12)の温度を235℃に、ポリマー管温度を250℃に設定した。これによりポリ乳酸の吐出量は安定したが、紡糸ヘッド(14)出口でポリ乳酸が黄変し、しかも熱分解と思われる発煙も発生し、良好状態に紡糸することができなかった。
<Comparative Example 3>
A polylactic acid chip (polymer of lactic acid monomer comprising 98% by mass of L-lactic acid and 2% by mass of D-lactic acid, weight average molecular weight 220,000, relative viscosity from the polylactic acid inlet (10) in the production apparatus having the structure shown in FIG. 4.0) While charging 100 parts by mass, 4 parts by mass of carbon black masterbatch (composition of 75% by mass of polylactic acid and 25% by mass of carbon black) was introduced from the colorant inlet (11) and vented ( 13) The mixture was melt-kneaded at 230 ° C. while degassing in a twin screw extruder (12). Since the melt viscosity of polylactic acid at the outlet of the twin-screw extruder (12) is too high, the pressure loss in the polymer tube up to the spinning head (14) with a polymer tube temperature of 225 ° C is large, and the outlet of the spinning head (14) As a result, uneven discharge of polylactic acid occurred remarkably. Therefore, the temperature of the twin screw extruder (12) was set to 235 ° C, and the polymer tube temperature was set to 250 ° C. As a result, the discharge amount of polylactic acid was stabilized, but the polylactic acid was yellowed at the outlet of the spinning head (14), and smoke generation that was thought to be thermal decomposition was also generated, so that spinning could not be performed in a good state.
なお、各原着ポリ乳酸捲縮糸の特性は下記測定法に基づいて測定した。また、得られたタフテッドカーペットの嵩高性及び耐摩耗性は下記評価法に基づいて評価した。これらの結果を表1に示す。 In addition, the characteristic of each original polylactic acid crimped yarn was measured based on the following measuring method. Moreover, the bulkiness and abrasion resistance of the obtained tufted carpet were evaluated based on the following evaluation methods. These results are shown in Table 1.
<相対粘度測定法>
フェノール/テトラクロロエタン=60/40(質量比)の混合溶液に試料を1g/dLの濃度となるよう溶解せしめ、20℃でウベローデ粘度管を用いて相対粘度を測定した。
<Relative viscosity measurement method>
The sample was dissolved in a mixed solution of phenol / tetrachloroethane = 60/40 (mass ratio) to a concentration of 1 g / dL, and the relative viscosity was measured at 20 ° C. using an Ubbelohde viscosity tube.
<重量平均分子量測定法>
試料を10mg/mLの濃度になるようクロロホルムに溶解せしめ、クロロホルムを溶媒として、東ソー製HLC8120GPCによりGPC分析を行い、重量平均分子量Mwを測定した。検出器はRI(赤外分光器)を用い、分子量の標準物質としてはポリスチレンを使用した。
<Weight average molecular weight measurement method>
The sample was dissolved in chloroform so as to have a concentration of 10 mg / mL, and GPC analysis was performed by using HLC8120GPC manufactured by Tosoh, using chloroform as a solvent, and the weight average molecular weight Mw was measured. RI (infrared spectrometer) was used as a detector, and polystyrene was used as a standard substance for molecular weight.
<L−乳酸の比率測定法>
ポリ乳酸を加水分解し、メタノール性水酸化ナトリウム溶液(濃度1.0N)を溶媒として高速液体クロマトグラフィー(HPLC:島津製作所LC10AD型)を使用してL−乳酸の比率を求めた。
<L-lactic acid ratio measurement method>
Polylactic acid was hydrolyzed, and the ratio of L-lactic acid was determined using high performance liquid chromatography (HPLC: Shimadzu Corporation LC10AD type) using methanolic sodium hydroxide solution (concentration: 1.0 N) as a solvent.
<異形度評価法>
単糸を切断後、光学顕微鏡を用いて単糸の外接円直径(B)と内接円直径(A)を測定して、B/Aの値を異形度とした(図2参照)。
<Variation degree evaluation method>
After cutting the single yarn, the circumscribed circle diameter (B) and the inscribed circle diameter (A) of the single yarn were measured using an optical microscope, and the value of B / A was defined as the degree of irregularity (see FIG. 2).
<強伸度測定法>
USTER社製TENSORAPID3の引張試験機を用い、試料長25cm、引張速度30cm/分の条件で強力(cN)と伸度(%)を測定した。強度(cN/dtex)は、強力(cN)を総繊度で除した値である。
<Strong elongation measurement method>
Strength (cN) and elongation (%) were measured under the conditions of a sample length of 25 cm and a tensile speed of 30 cm / min using a tensile tester of TENSORAPID3 manufactured by USTER. The strength (cN / dtex) is a value obtained by dividing the strength (cN) by the total fineness.
<繊度測定法>
JIS L1013に準拠して測定した。
<Fineness measurement method>
Measurement was performed in accordance with JIS L1013.
<熱水収縮率測定法>
熱水収縮率(%)は、JIS L1013のカセ収縮率(A法)に準拠して測定した。まず、ボビンパッケージからカセ取りした原着ポリ乳酸捲縮糸を試料とする。この試料糸に総繊度dtex×0.882mN(90mg/dtex)の張力を与える荷重をかけ10秒経過した後に、試料長さ(Ls1)を測定する。無荷重状態にて98℃の熱水に30分間浸漬した後、一昼夜自然乾燥させる。この乾燥後の捲縮糸を熱水処理後の原着ポリ乳酸捲縮糸とする。この熱水処理後の原着ポリ乳酸捲縮糸に、総繊度dtex×0.882mN(90mg/dtex)の張力を与える荷重をかけ10秒経過した後に、試料長さ(Ls2)を測定する。
熱水収縮率(%)={(Ls1−Ls2)/Ls1}×100
上記式より熱水収縮率(%)を求める。
<Hot water shrinkage measurement method>
The hot water shrinkage rate (%) was measured according to the casserole shrinkage rate (Method A) of JIS L1013. First, an original polylactic acid crimped yarn cut from a bobbin package is used as a sample. A load giving a tension of total fineness dtex × 0.882 mN (90 mg / dtex) is applied to the sample yarn, and after 10 seconds, the sample length (Ls1) is measured. After being immersed in hot water at 98 ° C. for 30 minutes in an unloaded state, it is naturally dried overnight. This dried crimped yarn is used as an original polylactic acid crimped yarn after hot water treatment. A load giving a total fineness of dtex × 0.882 mN (90 mg / dtex) is applied to the original polylactic acid crimped yarn after the hot water treatment, and after 10 seconds, the sample length (Ls2) is measured.
Hot water shrinkage (%) = {(Ls1-Ls2) / Ls1} × 100
The hot water shrinkage (%) is obtained from the above formula.
<乾熱捲縮率測定法>
ボビンパッケージからカセ取りした原着ポリ乳酸捲縮糸を、無荷重状態で100℃の熱風で10分間処理した後、10分間自然放置する。この糸を乾熱処理後の原着ポリ乳酸捲縮糸とする。この乾熱処理後の原着ポリ乳酸捲縮糸に、総繊度dtex×0.882mN(90mg/dtex)の張力を与える定荷重をかけ10秒経過した後に、試料長さ(Lc1)を測定する。次いで、前記乾熱処理後の原着ポリ乳酸捲縮糸に、総繊度dtex×0.0176mN(1.8mg/dtex)の張力を与える定荷重をかけ10秒経過した後に、試料長さ(Lc2)を測定する。
乾熱捲縮率(%)={(Lc1−Lc2)/Lc1}×100
上記式より乾熱捲縮率(%)を求める。
<Dry heat crimp rate measurement method>
The original polylactic acid crimped yarn cut from the bobbin package is treated with hot air at 100 ° C. for 10 minutes under no load, and then allowed to stand for 10 minutes. This yarn is the original polylactic acid crimped yarn after dry heat treatment. A constant load giving a tension of total fineness dtex × 0.882 mN (90 mg / dtex) is applied to the original polylactic acid crimped yarn after the dry heat treatment, and after 10 seconds, the sample length (Lc1) is measured. Next, after applying a constant load that gives a tension of total fineness dtex × 0.0176 mN (1.8 mg / dtex) to the original polylactic acid crimped yarn after the dry heat treatment, the sample length (Lc2) Measure.
Dry heat crimp rate (%) = {(Lc1-Lc2) / Lc1} × 100
The dry heat crimp rate (%) is obtained from the above formula.
<嵩高性評価>
カーペットを真上から見た時に、パイル表皮の隙間から基布が見える状態を目視で評価し、基布が見えにくいものを「◎」、基布がある程度見えるものを「○」、基布がよく見えるものを「×」とした。
<Bulkness evaluation>
When the carpet is viewed from directly above, the condition where the base fabric can be seen through the gaps in the pile skin is visually evaluated. “◎” indicates that the base fabric is difficult to see, “○” indicates that the base fabric is visible to some extent, Those that looked good were marked with “x”.
<耐摩耗性評価>
カーペットの耐摩耗性は、JIS L1096.17.3に規定のテーバー型摩耗試験機を用いて評価した。即ち、H−18摩耗輪を使用し、この摩耗輪に9.8Nの荷重をかけ試験台を1000回回転させて試験片を摩耗させ、その摩耗状態を目視により評価した。摩耗の非常に少ないものを「◎」、摩耗の少ないものを「○」、摩耗がある程度あるものを「△」、摩耗が多いものを「×」とした。
<Abrasion resistance evaluation>
The abrasion resistance of the carpet was evaluated using a Taber type abrasion tester specified in JIS L1096.17.3. That is, an H-18 wear wheel was used, a load of 9.8 N was applied to the wear wheel, the test stand was rotated 1000 times to wear the test piece, and the wear state was visually evaluated. Those with very little wear were marked with “◎”, those with little wear were marked with “◯”, those with some wear were “△”, and those with much wear were marked with “X”.
表1から明らかなように、この発明の原着ポリ乳酸捲縮糸を用いて構成された実施例1〜4のカーペットは、十分な嵩高性が得られると共に耐摩耗性に優れていた。これに対し、比較例1、2のカーペットは耐摩耗性に劣っていた。 As can be seen from Table 1, the carpets of Examples 1 to 4 constructed using the original polylactic acid crimped yarn of the present invention had sufficient bulkiness and excellent wear resistance. On the other hand, the carpets of Comparative Examples 1 and 2 were inferior in wear resistance.
この発明の原着ポリ乳酸捲縮糸及びこの発明の製造方法で得られた原着ポリ乳酸捲縮糸は、例えばカーペットの構成糸として好適に用いられる。例えば、ロールカーペット、ピースカーペット、タイルカーペット、自動車用ラインカーペット、自動車用オプションマット、家庭用ラグ・マット等の構成糸として好適に用いられる。この発明の原着ポリ乳酸捲縮糸でカーペットのパイルを構成する場合、そのパイル形態は特に限定されず、ループパイル、カットパイル、カットアンドループパイル等どのようなパイル形状も採用できる。また、タフテッドカーペットのみならず、織物カーペット、編物カーペット、刺繍カーペット、接着カーペット等の構成糸としても使用できる。本発明の原着ポリ乳酸捲縮糸を用いて構成されたカーペットは、使用後廃棄された場合には微生物等により分解されるので地球環境保全に貢献することができる。 The original polylactic acid crimped yarn of the present invention and the original polylactic acid crimped yarn obtained by the production method of the present invention are suitably used as, for example, a constituent yarn of a carpet. For example, it is suitably used as a constituent yarn for roll carpets, piece carpets, tile carpets, automotive line carpets, automotive option mats, household rugs and mats, and the like. When the carpet pile is constituted by the original polylactic acid crimped yarn of the present invention, the pile form is not particularly limited, and any pile shape such as loop pile, cut pile, cut and loop pile can be adopted. Moreover, it can be used not only as a tufted carpet but also as a constituent yarn of a woven carpet, a knitted carpet, an embroidery carpet, an adhesive carpet and the like. The carpet constituted by using the original polylactic acid crimped yarn of the present invention is decomposed by microorganisms or the like when discarded after use, and can contribute to the preservation of the global environment.
2…予熱ローラ
3…延伸ローラ
4…熱セットローラ
5…加熱流体捲縮付与装置
6…捲縮糸
20…冷却ドラム
21…交絡処理装置
DESCRIPTION OF
Claims (8)
前記紡糸糸を70〜125℃に設定された延伸ローラにより3〜6倍に延伸する工程と、
前記延伸された紡糸糸を100〜150℃に設定された熱セットローラにより熱セットする工程と、
前記熱セットされた延伸糸に加熱流体捲縮付与装置を用いて105〜125℃の加熱流体を接触させることによって糸に捲縮を付与する捲縮工程と、
前記捲縮工程を経た捲縮糸を該糸のガラス転移温度よりも低い温度まで冷却する工程とを包含することを特徴とする原着ポリ乳酸捲縮糸の製造方法。 A polylactic acid composition containing a colorant and polylactic acid, having a colorant content of 0.01 to 3% by mass and a relative viscosity of 2.5 to 3.8 is spun, and the cross-sectional shape of the single fiber is irregular. A spinning step for obtaining a spun yarn having a substantially circular shape or a circular shape having a degree of less than 1.5;
Stretching the spun yarn 3-6 times with a stretching roller set at 70-125 ° C;
Heat-setting the drawn spun yarn with a heat-setting roller set at 100 to 150 ° C .;
A crimping step of imparting crimp to the yarn by bringing the heated fluid crimping device into contact with a heated fluid at 105 to 125 ° C. using a heated fluid crimping device;
And a step of cooling the crimped yarn having undergone the crimping step to a temperature lower than the glass transition temperature of the yarn.
前記紡糸糸を70〜125℃に設定された延伸ローラにより3〜6倍に延伸する工程と、
前記延伸された紡糸糸を100〜150℃に設定された熱セットローラにより熱セットする工程と、
前記熱セットされた延伸糸に加熱流体捲縮付与装置を用いて105〜125℃℃の加熱流体を接触させることによって糸に捲縮を付与する捲縮工程と、
前記捲縮工程を経た捲縮糸を該糸のガラス転移温度よりも低い温度まで冷却する工程とを包含することを特徴とする原着ポリ乳酸捲縮糸の製造方法。 A polylactic acid composition containing a colorant and polylactic acid, having a colorant content of 0.01 to 3% by mass and a relative viscosity of 2.5 to 3.8 is extruded from a spinneret and has a cross-sectional shape of 1 A spinning step of obtaining a spun yarn by obtaining a substantially circular or circular filament of less than .5, cooling the filament with cold air, and then coating the filament with an oil agent;
Stretching the spun yarn 3-6 times with a stretching roller set at 70-125 ° C;
Heat-setting the drawn spun yarn with a heat-setting roller set at 100 to 150 ° C .;
A crimping step for imparting crimps to the yarn by bringing the heated fluid crimping device into contact with a heated fluid at 105 to 125 ° C using a heated fluid crimping device;
And a step of cooling the crimped yarn having undergone the crimping step to a temperature lower than the glass transition temperature of the yarn.
30℃≧ S−R ≧−10℃
を満足する請求項1または2に記載の原着ポリ乳酸捲縮糸の製造方法。 When the temperature of the heat setting roller is “S” and the temperature of the heating fluid in the heating fluid crimping device is “R”, the following relational expression 30 ° C. ≧ SR−−10 ° C.
The method for producing an original polylactic acid crimped yarn according to claim 1 or 2 , wherein:
A carpet constituted by using the original polylactic acid crimped yarn according to claim 7 as at least a part of constituent fibers.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2005258632A JP4481907B2 (en) | 2005-09-07 | 2005-09-07 | Original polylactic acid crimped yarn, method for producing the same, and carpet |
PCT/JP2006/317533 WO2007029688A1 (en) | 2005-09-07 | 2006-09-05 | Spun-dyed, crimped polylactic acid fiber, method for manufacture thereof, and carpet |
EP06797439A EP1956120A4 (en) | 2005-09-07 | 2006-09-05 | Spun-dyed, crimped polylactic acid fiber, method for manufacture thereof, and carpet |
US11/991,460 US20090208695A1 (en) | 2005-09-07 | 2006-09-05 | Spun-dyed, crimped polylactic acid fiber, method for manufacture thereof, and carpet |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2005258632A JP4481907B2 (en) | 2005-09-07 | 2005-09-07 | Original polylactic acid crimped yarn, method for producing the same, and carpet |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2007070757A JP2007070757A (en) | 2007-03-22 |
JP4481907B2 true JP4481907B2 (en) | 2010-06-16 |
Family
ID=37932463
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2005258632A Active JP4481907B2 (en) | 2005-09-07 | 2005-09-07 | Original polylactic acid crimped yarn, method for producing the same, and carpet |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP4481907B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007029688A1 (en) * | 2005-09-07 | 2007-03-15 | Suminoe Textile Co., Ltd. | Spun-dyed, crimped polylactic acid fiber, method for manufacture thereof, and carpet |
JP2012251417A (en) * | 2011-05-09 | 2012-12-20 | Japan Carpet Co Ltd | Tile carpet |
-
2005
- 2005-09-07 JP JP2005258632A patent/JP4481907B2/en active Active
Also Published As
Publication number | Publication date |
---|---|
JP2007070757A (en) | 2007-03-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2007029688A1 (en) | Spun-dyed, crimped polylactic acid fiber, method for manufacture thereof, and carpet | |
KR102213562B1 (en) | Process for the preparation of a fiber, a fiber and a yarn made from such a fiber | |
EP0745711B1 (en) | Process for preparing poly (trimethylene terephthalate) yarns | |
JP5105619B2 (en) | Original polyethylene terephthalate false twisted yarn, method for producing the same, and carpet using the same | |
CA2252138C (en) | Process for making poly(trimethylene terephthalate) yarn | |
US20100215895A1 (en) | Process of producing ultra fine microdenier filaments and fabrics made thereof | |
US20030054718A1 (en) | Poly(lactic acid) fiber | |
TWI746672B (en) | Polymer blend fiber and fiber structure containing it | |
JP4789261B2 (en) | Breathable tile carpet with improved vegetation | |
JP2006336125A (en) | Bulky sheath-core conjugated filaments and method for producing the same | |
JP4481907B2 (en) | Original polylactic acid crimped yarn, method for producing the same, and carpet | |
TW202129105A (en) | Carpet made from self-bulking ptt-containing bicomponent fibers | |
JP4571095B2 (en) | Original polylactic acid false twisted yarn, method for producing the same, and carpet | |
TWI437142B (en) | Core-sheath conjugate type partially oriented fiber of polyester, cheese package, and false twisting yarn | |
JP4783105B2 (en) | carpet | |
JP2023533501A (en) | Method of making bicomponent fibers and articles containing same | |
JP5964437B2 (en) | Poly (trimethylene arylate) fiber, method for making the same, and fabric made therefrom | |
JP4804092B2 (en) | carpet | |
JP2002227036A (en) | Aliphatic polyester yarn for carpet and carpet | |
JPH10501031A (en) | Matted nylon filament with vertical stripes of polymethylpentene | |
JP5264599B2 (en) | carpet | |
JP4254368B2 (en) | Production method of polylactic acid crimped yarn and carpet | |
JP2005060850A (en) | Spun-dyed polylactic acid crimped yarn and carpet using the same | |
JP2018071023A (en) | Spun-dyed crimped yarn and carpet | |
JP2014526621A (en) | Poly (trimethylene arylate) fiber, method for making the same, and fabric made therefrom |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20071219 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20091215 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20100118 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20100223 |
|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20100318 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130326 Year of fee payment: 3 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 4481907 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130326 Year of fee payment: 3 |
|
RD02 | Notification of acceptance of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: R3D02 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130326 Year of fee payment: 3 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20140326 Year of fee payment: 4 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |