JPH0921018A - Biodegradable fiber and nonwoven fabric using the same - Google Patents
Biodegradable fiber and nonwoven fabric using the sameInfo
- Publication number
- JPH0921018A JPH0921018A JP17114295A JP17114295A JPH0921018A JP H0921018 A JPH0921018 A JP H0921018A JP 17114295 A JP17114295 A JP 17114295A JP 17114295 A JP17114295 A JP 17114295A JP H0921018 A JPH0921018 A JP H0921018A
- Authority
- JP
- Japan
- Prior art keywords
- biodegradable fiber
- fiber
- biodegradable
- spinning
- fiber according
- 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.)
- Granted
Links
- 239000000835 fiber Substances 0.000 title claims abstract description 111
- 239000004745 nonwoven fabric Substances 0.000 title claims description 20
- 229920000747 poly(lactic acid) Polymers 0.000 claims abstract description 26
- 239000004626 polylactic acid Substances 0.000 claims abstract description 25
- 229920001577 copolymer Polymers 0.000 claims abstract description 9
- 150000001875 compounds Chemical class 0.000 claims abstract description 6
- 229920005992 thermoplastic resin Polymers 0.000 claims description 26
- 150000003384 small molecules Chemical class 0.000 claims description 23
- 238000002844 melting Methods 0.000 claims description 15
- 230000008018 melting Effects 0.000 claims description 15
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims description 6
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 5
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 abstract description 18
- 239000000463 material Substances 0.000 abstract description 15
- 239000004310 lactic acid Substances 0.000 abstract description 9
- 235000014655 lactic acid Nutrition 0.000 abstract description 9
- 239000012773 agricultural material Substances 0.000 abstract description 6
- JJTUDXZGHPGLLC-UHFFFAOYSA-N lactide Chemical compound CC1OC(=O)C(C)OC1=O JJTUDXZGHPGLLC-UHFFFAOYSA-N 0.000 abstract description 5
- 239000003054 catalyst Substances 0.000 abstract description 4
- 239000004035 construction material Substances 0.000 abstract description 4
- JJTUDXZGHPGLLC-IMJSIDKUSA-N 4511-42-6 Chemical compound C[C@@H]1OC(=O)[C@H](C)OC1=O JJTUDXZGHPGLLC-IMJSIDKUSA-N 0.000 abstract description 3
- 238000007151 ring opening polymerisation reaction Methods 0.000 abstract description 3
- OZZQHCBFUVFZGT-UHFFFAOYSA-N 2-(2-hydroxypropanoyloxy)propanoic acid Chemical compound CC(O)C(=O)OC(C)C(O)=O OZZQHCBFUVFZGT-UHFFFAOYSA-N 0.000 abstract 2
- 238000009987 spinning Methods 0.000 description 45
- 238000000034 method Methods 0.000 description 24
- 238000002074 melt spinning Methods 0.000 description 13
- 230000014759 maintenance of location Effects 0.000 description 7
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 6
- -1 polyethylene Polymers 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- REKYPYSUBKSCAT-UHFFFAOYSA-N 3-hydroxypentanoic acid Chemical compound CCC(O)CC(O)=O REKYPYSUBKSCAT-UHFFFAOYSA-N 0.000 description 4
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 4
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 4
- 150000002334 glycols Chemical class 0.000 description 4
- 230000000704 physical effect Effects 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- 239000002689 soil Substances 0.000 description 4
- AEMRFAOFKBGASW-UHFFFAOYSA-N Glycolic acid Polymers OCC(O)=O AEMRFAOFKBGASW-UHFFFAOYSA-N 0.000 description 3
- 238000003490 calendering Methods 0.000 description 3
- 239000001913 cellulose Substances 0.000 description 3
- 229920002678 cellulose Polymers 0.000 description 3
- 238000002788 crimping Methods 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- LQZZUXJYWNFBMV-UHFFFAOYSA-N dodecan-1-ol Chemical compound CCCCCCCCCCCCO LQZZUXJYWNFBMV-UHFFFAOYSA-N 0.000 description 3
- 238000004049 embossing Methods 0.000 description 3
- 239000012770 industrial material Substances 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 239000000178 monomer Substances 0.000 description 3
- YTJSFYQNRXLOIC-UHFFFAOYSA-N octadecylsilane Chemical compound CCCCCCCCCCCCCCCCCC[SiH3] YTJSFYQNRXLOIC-UHFFFAOYSA-N 0.000 description 3
- 229920001610 polycaprolactone Polymers 0.000 description 3
- 239000004632 polycaprolactone Substances 0.000 description 3
- 229920000728 polyester Polymers 0.000 description 3
- 238000004080 punching Methods 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 238000001226 reprecipitation Methods 0.000 description 3
- UQDJGEHQDNVPGU-UHFFFAOYSA-N serine phosphoethanolamine Chemical compound [NH3+]CCOP([O-])(=O)OCC([NH3+])C([O-])=O UQDJGEHQDNVPGU-UHFFFAOYSA-N 0.000 description 3
- 229920002545 silicone oil Polymers 0.000 description 3
- MNKRTDOUBUSQHX-UHFFFAOYSA-N 2,4-dihydroxy-2-methyl-3-oxopentanoic acid Chemical compound CC(O)C(=O)C(C)(O)C(O)=O MNKRTDOUBUSQHX-UHFFFAOYSA-N 0.000 description 2
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical compound CCCC(O)=O FERIUCNNQQJTOY-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
- 239000002202 Polyethylene glycol Substances 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- 229920003232 aliphatic polyester Polymers 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 229920002988 biodegradable polymer Polymers 0.000 description 2
- 239000004621 biodegradable polymer Substances 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000004811 liquid chromatography Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000004750 melt-blown nonwoven Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- GLDOVTGHNKAZLK-UHFFFAOYSA-N octadecan-1-ol Chemical compound CCCCCCCCCCCCCCCCCCO GLDOVTGHNKAZLK-UHFFFAOYSA-N 0.000 description 2
- 229920000070 poly-3-hydroxybutyrate Polymers 0.000 description 2
- 229920001515 polyalkylene glycol Polymers 0.000 description 2
- 229920001223 polyethylene glycol Polymers 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 238000004007 reversed phase HPLC Methods 0.000 description 2
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 229920001169 thermoplastic Polymers 0.000 description 2
- 239000004416 thermosoftening plastic Substances 0.000 description 2
- 238000004804 winding Methods 0.000 description 2
- KBPLFHHGFOOTCA-UHFFFAOYSA-N 1-Octanol Chemical compound CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 description 1
- BWLBGMIXKSTLSX-UHFFFAOYSA-N 2-hydroxyisobutyric acid Chemical compound CC(C)(O)C(O)=O BWLBGMIXKSTLSX-UHFFFAOYSA-N 0.000 description 1
- JRHWHSJDIILJAT-UHFFFAOYSA-N 2-hydroxypentanoic acid Chemical compound CCCC(O)C(O)=O JRHWHSJDIILJAT-UHFFFAOYSA-N 0.000 description 1
- WHBMMWSBFZVSSR-UHFFFAOYSA-M 3-hydroxybutyrate Chemical compound CC(O)CC([O-])=O WHBMMWSBFZVSSR-UHFFFAOYSA-M 0.000 description 1
- SJZRECIVHVDYJC-UHFFFAOYSA-M 4-hydroxybutyrate Chemical compound OCCCC([O-])=O SJZRECIVHVDYJC-UHFFFAOYSA-M 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 229920002101 Chitin Polymers 0.000 description 1
- 229920001661 Chitosan Polymers 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical class C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 1
- NGEWQZIDQIYUNV-UHFFFAOYSA-N L-valinic acid Natural products CC(C)C(O)C(O)=O NGEWQZIDQIYUNV-UHFFFAOYSA-N 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- 229920001410 Microfiber Polymers 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 229920000954 Polyglycolide Polymers 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- WHBMMWSBFZVSSR-UHFFFAOYSA-N R3HBA Natural products CC(O)CC(O)=O WHBMMWSBFZVSSR-UHFFFAOYSA-N 0.000 description 1
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000008186 active pharmaceutical agent Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 125000003545 alkoxy group Chemical group 0.000 description 1
- 229940061720 alpha hydroxy acid Drugs 0.000 description 1
- 150000001280 alpha hydroxy acids Chemical class 0.000 description 1
- 239000003945 anionic surfactant Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- KDYFGRWQOYBRFD-NUQCWPJISA-N butanedioic acid Chemical compound O[14C](=O)CC[14C](O)=O KDYFGRWQOYBRFD-NUQCWPJISA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 235000001465 calcium Nutrition 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003093 cationic surfactant Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 229920006237 degradable polymer Polymers 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 150000001991 dicarboxylic acids Chemical class 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 239000004205 dimethyl polysiloxane Substances 0.000 description 1
- 235000013870 dimethyl polysiloxane Nutrition 0.000 description 1
- GWTCIAGIKURVBJ-UHFFFAOYSA-L dipotassium;dodecyl phosphate Chemical compound [K+].[K+].CCCCCCCCCCCCOP([O-])([O-])=O GWTCIAGIKURVBJ-UHFFFAOYSA-L 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000003658 microfiber Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- GOQYKNQRPGWPLP-UHFFFAOYSA-N n-heptadecyl alcohol Natural products CCCCCCCCCCCCCCCCCO GOQYKNQRPGWPLP-UHFFFAOYSA-N 0.000 description 1
- 239000002736 nonionic surfactant Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 239000003505 polymerization initiator Substances 0.000 description 1
- 229920001451 polypropylene glycol Polymers 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 235000018102 proteins Nutrition 0.000 description 1
- 150000003242 quaternary ammonium salts Chemical class 0.000 description 1
- 239000004627 regenerated cellulose Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 230000002123 temporal effect Effects 0.000 description 1
- 239000006097 ultraviolet radiation absorber Substances 0.000 description 1
- PAPBSGBWRJIAAV-UHFFFAOYSA-N ε-Caprolactone Chemical compound O=C1CCCCCO1 PAPBSGBWRJIAAV-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Artificial Filaments (AREA)
- Nonwoven Fabrics (AREA)
- Biological Depolymerization Polymers (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、生分解性繊維に関し、
特に室温での経時安定性の良い生分解性繊維に関する。TECHNICAL FIELD The present invention relates to a biodegradable fiber,
In particular, the present invention relates to a biodegradable fiber having good stability over time at room temperature.
【0002】[0002]
【従来技術・発明が解決しようとする課題】従来、生活
資材、農業資材、漁業資材、土木資材に使用されている
繊維として、ポリエステル、ポリオレフィン、ポリアミ
ド等の合成繊維が挙げられる。これらの繊維は、使用後
自然界に放置されると、分解されにくく、その為にいろ
いろな問題が生じるものであった。例えば、これらの生
活資材、農業資材、土木資材等は、分解されにくい為、
使用後は土中に埋める、焼却する等の処理が必要とな
り、土中に埋めると生分解性が低いため、その土地の利
用方法には制限があった。また、漁業資材においては、
水中に放置されることが多く、海洋を汚す等の問題があ
った。このような問題を解決する為に、土中または水中
で分解される素材を用いることが考えられてきたが、充
分なものは得られていない。2. Description of the Related Art Fibers that have hitherto been used for living materials, agricultural materials, fishery materials, and civil engineering materials include synthetic fibers such as polyester, polyolefin, and polyamide. When these fibers are left in the natural environment after use, they are not easily decomposed, which causes various problems. For example, since these living materials, agricultural materials, civil engineering materials, etc. are difficult to decompose,
After use, it was necessary to bury it in the soil, incinerate it, and so on, and if it was buried in the soil, its biodegradability was low, so there was a limit to how it could be used. In the case of fishery materials,
Often left in the water, there were problems such as polluting the ocean. In order to solve such a problem, it has been considered to use a material that is decomposed in soil or water, but a material that has been sufficiently decomposed has not been obtained.
【0003】従来の生分解性ポリマーとしては、セルロ
ース、セルロース誘導体、キチン、キトサン等の多糖
類、タンパク質、ポリ3−ヒドロキシブチレートや3−
ヒドロキシブチレートと3−ヒドロキシバリレートの共
重合体等の微生物により作られるポリマー、ポリグリコ
リド、ポリラクチド、ポリカプロラクトン等の脂肪族ポ
リエステルが知られている。主に使用されているセルロ
ース系のコットン、再生セルロースは安価であるが、熱
可塑性でないためバインダーを必要とし、該バインダー
繊維としてポリオレフィン、ポリエステル繊維等を用い
るため、生分解されにくいという問題があった。微生物
により作られるポリ3−ヒドロキシブチレート、3−ヒ
ドロキシブチレートと3−ヒドロキシバリレートの共重
合体等は、高価であるため用途が限定され、また強度が
低いという問題があった。ポリカプロラクトンは、比較
的安価な生分解性ポリマーであるが、融点が約60℃と
低く、この温度は自然界において、夏期の流通段階で起
こり得る温度であり、耐熱性という点で問題があった。Examples of conventional biodegradable polymers include cellulose, cellulose derivatives, polysaccharides such as chitin and chitosan, proteins, poly-3-hydroxybutyrate and 3-.
Polymers produced by microorganisms such as copolymers of hydroxybutyrate and 3-hydroxyvalerate, and aliphatic polyesters such as polyglycolide, polylactide and polycaprolactone are known. Cellulose-based cotton and regenerated cellulose, which are mainly used, are inexpensive, but require binders because they are not thermoplastic and use polyolefins, polyester fibers, etc. as the binder fibers, and thus have a problem of being difficult to biodegrade. . Since poly-3-hydroxybutyrate, a copolymer of 3-hydroxybutyrate and 3-hydroxyvalerate, etc. produced by a microorganism are expensive, their applications are limited, and their strength is low. Polycaprolactone is a relatively inexpensive biodegradable polymer, but its melting point is as low as about 60 ° C., which is a temperature that can occur in the distribution stage in summer in nature, and there was a problem in heat resistance. .
【0004】さらには、安価な素材としてポリエチレン
に澱粉を混合した素材が検討されているが、生分解性に
おいて満足いく物でなく、均一な機械特性の繊維を得る
ことができていない。特開平4−108331号公報に
は、グリコール酸及び/又は乳酸を構造単位とする加水
分解性ポリエステル繊維に、その繊維より加水分解性が
低い分解性重合体をコートした釣り糸が開示されている
が、後加工を必要とする問題があった。また、ポリ乳酸
は、比較的安定なポリマーであるが、室温での経時安定
性(強度保持率)に問題があり、特に強度が低下すると
いう問題があった。Further, a material obtained by mixing polyethylene with starch has been studied as an inexpensive material, but it is not satisfactory in terms of biodegradability and fibers having uniform mechanical properties cannot be obtained. JP-A-4-108331 discloses a fishing line in which a hydrolyzable polyester fiber having glycolic acid and / or lactic acid as a structural unit is coated with a degradable polymer having a lower hydrolyzability than the fiber. There was a problem that requires post-processing. Although polylactic acid is a relatively stable polymer, it has a problem in stability over time (strength retention rate) at room temperature, and particularly has a problem that strength is lowered.
【0005】このように従来技術においては、強度及び
実用耐熱性を持ち、室温での経時安定性(強度保持率)
が良く、微生物により速やかで、且つ優れた生分解性を
もつ熱可塑性生分解性繊維がなく、実用性があり且つ比
較的安価な生分解性繊維を得ることができなかった。As described above, the prior art has strength and practical heat resistance and stability at room temperature with time (strength retention rate).
It was not possible to obtain a biodegradable fiber that is practical, and is relatively inexpensive, since it does not have a thermoplastic biodegradable fiber that has good biodegradability, is quick by microorganisms, and has excellent biodegradability.
【0006】本発明の課題は、このような事情に鑑み、
ポリ乳酸系の生分解性繊維において経時安定性(強度保
持率)が改善され、且つ強度をもつような生分解性繊維
を提供することである。[0006] In view of such circumstances, the object of the present invention is to
It is an object of the present invention to provide a biodegradable fiber which has improved stability over time (strength retention rate) and has strength in a polylactic acid-based biodegradable fiber.
【0007】[0007]
【課題を解決するための手段】本発明者らは、上記課題
を解決するために鋭意研究した結果、生分解性繊維に、
ポリ乳酸及び/又はポリ乳酸を主体とする共重合物から
なる熱可塑性樹脂を用いて、低分子量化合物の含量を制
御することで上記問題を解決するに至った。Means for Solving the Problems As a result of intensive research to solve the above problems, the present inventors have found that biodegradable fibers are
The above problem has been solved by controlling the content of low molecular weight compounds using a thermoplastic resin composed of polylactic acid and / or a copolymer mainly composed of polylactic acid.
【0008】即ち、本発明は、(1) ポリ乳酸及び/又は
ポリ乳酸を主体とする共重合物からなる熱可塑性樹脂を
含んでなり、低分子量化合物の含量が1重量%以下であ
ることを特徴とする生分解性繊維、(2) 融点が120〜
200℃の範囲にあるか又は流動開始温度が100〜1
80℃の範囲にある (1)記載の生分解性繊維、(3) 前記
熱可塑性樹脂が、水酸基を持つ化合物によって該熱可塑
性樹脂中のカルボキシル基をエステル化されてなるもの
である (1)または(2) 記載の生分解性繊維、(4) 引張強
度2.5g/d以上、引張破断伸度10%以上である
(1)〜(3) のいずれかに記載の生分解性繊維、(5) 引張
強度2.5g/d以上、引張破断伸度10%以上、結節
強度1.5g/d以上である (1)〜(3) のいずれかに記
載の生分解性繊維、(6) マルチフィラメントの形態であ
る (1)〜(5) のいずれかに記載の生分解性繊維、(7) モ
ノフィラメントの形態である (1)〜(5) のいずれかに記
載の生分解性繊維、(8) 短繊維の形態である (1)〜(7)
のいずれかに記載の生分解性繊維、(9)(8)記載の生分解
性繊維を用いてなる短繊維不織布、(10) (1)〜(3) のい
ずれかに記載の生分解性繊維を用いてなる長繊維不織布
に関する。That is, the present invention comprises (1) a thermoplastic resin comprising polylactic acid and / or a copolymer mainly composed of polylactic acid, wherein the content of the low molecular weight compound is 1% by weight or less. Characteristic biodegradable fiber, (2) Melting point 120 ~
In the range of 200 ° C or the flow starting temperature is 100 to 1
(1) the biodegradable fiber in the range of 80 ° C., (3) the thermoplastic resin in which the carboxyl group in the thermoplastic resin is esterified with a compound having a hydroxyl group (1) Or (2) biodegradable fiber, (4) tensile strength of 2.5 g / d or more, tensile elongation at break of 10% or more
The biodegradable fiber according to any one of (1) to (3), (5) tensile strength 2.5 g / d or more, tensile elongation at break 10% or more, knot strength 1.5 g / d or more (1 ) ~ (3) biodegradable fiber, (6) in the form of multifilament (1) ~ (5) biodegradable fiber, (7) in the form of monofilament There is a biodegradable fiber according to any one of (1) to (5), (8) in the form of short fibers (1) to (7)
Biodegradable fiber according to any one of (1) to (3), (10) (1) to (3) biodegradable non-woven fabric using the biodegradable fiber according to (9) (8) The present invention relates to a long-fiber non-woven fabric using fibers.
【0009】以下、本発明について詳細に説明する。本
発明に用いられる熱可塑性樹脂は、ポリ乳酸及び/又は
ポリ乳酸を主体とする共重合物からなる。ポリ乳酸を製
造するための乳酸としては、D体のみ、L体のみ、D体
とL体の混合物のいずれでもよい。ポリ乳酸を主体とす
る共重合物としては、乳酸(D体のみ、L体のみ、D体
とL体の混合物のいずれでもよい。)と、例えばε−カ
プロラクトン等の環状ラクトン類、α−ヒドロキシ酪
酸、α−ヒドロキシイソ酪酸、α−ヒドロキシ吉草酸等
のα−オキシ酸類、エチレングリコール、1,4−ブタ
ンジオール等のグリコール類、コハク酸、セバシン酸等
のジカルボン酸類から選ばれるモノマーの一種又は二種
以上とを共重合したものが挙げられる。中でも、ポリマ
ーの重合性の点から、環状ラクトン類及びグリコール類
が好ましい。共重合の割合としては特に限定されない
が、乳酸100重量部に対して、共重合させるモノマー
は100重量部以下が好ましく、1〜50重量部がより
好ましい。Hereinafter, the present invention will be described in detail. The thermoplastic resin used in the present invention comprises polylactic acid and / or a copolymer mainly composed of polylactic acid. The lactic acid for producing polylactic acid may be only the D-form, the L-form, or a mixture of the D-form and the L-form. Examples of the copolymer containing polylactic acid as a main component include lactic acid (either D-form, L-form, or a mixture of D- and L-forms), cyclic lactones such as ε-caprolactone, and α-hydroxy. Butyric acid, α-hydroxyisobutyric acid, α-hydroxy acids such as α-hydroxyvaleric acid, ethylene glycol, glycols such as 1,4-butanediol, succinic acid, one of monomers selected from dicarboxylic acids such as sebacic acid, or The thing which copolymerized two or more types is mentioned. Among them, cyclic lactones and glycols are preferable from the viewpoint of polymer polymerizability. The proportion of copolymerization is not particularly limited, but 100 parts by weight or less of the monomer to be copolymerized is preferable, and 1 to 50 parts by weight is more preferable, relative to 100 parts by weight of lactic acid.
【0010】また、上記熱可塑性樹脂が、水酸基を持つ
化合物によって該熱可塑性樹脂中のカルボキシル基をエ
ステル化されてなるものであっても良い。水酸基を持つ
化合物としては、例えばオクチルアルコール、ラウリル
アルコール、ステアリルアルコール等の炭素数が6以上
の高級アルコール類、エチレングリコール、ジエチレン
グリコール、1,4−ブタンジオール等のグリコール類
が挙げられる。水酸基を持つ化合物で熱可塑性樹脂の分
子末端のカルボキシル基をエステル化処理することによ
り、溶融紡糸時の熱安定性および溶融紡糸後の繊維の経
時安定性を改善することができる。中でも、紡糸延伸性
の点から、炭素数6〜18の高級アルコールが好まし
い。Further, the thermoplastic resin may be one in which the carboxyl group in the thermoplastic resin is esterified with a compound having a hydroxyl group. Examples of the compound having a hydroxyl group include higher alcohols having 6 or more carbon atoms such as octyl alcohol, lauryl alcohol and stearyl alcohol, and glycols such as ethylene glycol, diethylene glycol and 1,4-butanediol. By esterifying the carboxyl group at the molecular end of the thermoplastic resin with a compound having a hydroxyl group, the thermal stability during melt spinning and the temporal stability of the fiber after melt spinning can be improved. Among them, higher alcohols having 6 to 18 carbon atoms are preferable from the viewpoint of spinnability.
【0011】熱可塑性樹脂の合成は、自体既知の方法で
行えば良く、例えば、触媒存在下にてL−ラクチドを開
環重合し必要に応じて再沈澱精製し熱可塑性樹脂を得
る。また共重合するモノマー、又はオリゴマーとL−ラ
クチドを触媒存在下にて開環重合し必要に応じ再沈澱精
製し共重合熱可塑性樹脂を得る。The thermoplastic resin may be synthesized by a method known per se. For example, ring-opening polymerization of L-lactide in the presence of a catalyst and reprecipitation purification if necessary to obtain a thermoplastic resin. Further, a monomer or oligomer to be copolymerized and L-lactide are subjected to ring-opening polymerization in the presence of a catalyst and, if necessary, reprecipitation purification is carried out to obtain a copolymerized thermoplastic resin.
【0012】本発明に用いる熱可塑性樹脂は、その粘度
平均分子量が5×103 以上であることが好ましく、よ
り好ましくは1×104 〜1×106 である。5×10
3 未満では繊維として、充分な強度が得られない傾向が
あり、1×106 を越えると、紡糸時高粘度となり製糸
性が劣る傾向がある。The thermoplastic resin used in the present invention preferably has a viscosity average molecular weight of 5 × 10 3 or more, more preferably 1 × 10 4 to 1 × 10 6 . 5 x 10
If it is less than 3 , sufficient fiber strength tends not to be obtained, and if it exceeds 1 × 10 6 , the viscosity tends to be high during spinning and the spinnability tends to be poor.
【0013】ここで粘度平均分子量〔MV〕は、ηsp/
C=7.79×10-4MV0.73〔式中、ηsp/Cは還元
比粘度(dl/g)、MVは粘度平均分子量である〕に
基づいたものである。The viscosity average molecular weight [MV] is η sp /
C = 7.79 × 10 −4 MV 0.73 [wherein, η sp / C is the reduced specific viscosity (dl / g) and MV is the viscosity average molecular weight].
【0014】また、本発明に用いる熱可塑性樹脂は、そ
の還元比粘度が0.5〜19(dl/g)であることが
好ましく、より好ましくは1.0〜6.0(dl/g)
である。熱可塑性樹脂の還元比粘度が0.4(dl/
g)未満であると、引張強度が不足である傾向があり、
20(dl/g)を越えると、紡糸時粘度が高く加工性
が良くない傾向がある。The thermoplastic resin used in the present invention preferably has a reduced specific viscosity of 0.5 to 19 (dl / g), more preferably 1.0 to 6.0 (dl / g).
It is. The reduced specific viscosity of the thermoplastic resin is 0.4 (dl /
If it is less than g), the tensile strength tends to be insufficient,
If it exceeds 20 (dl / g), the viscosity during spinning tends to be high and the processability tends to be poor.
【0015】ここで還元比粘度とは、試料を精秤し、
0.5g/dlとなるようにクロロホルムに溶解し、該
溶液について、25℃でウベローデ型粘度計を用いて測
定したものである。Here, the reduced specific viscosity means that a sample is precisely weighed,
The solution was dissolved in chloroform at 0.5 g / dl, and the solution was measured at 25 ° C. using an Ubbelohde viscometer.
【0016】熱可塑性樹脂の平均分子量は、重合開始
剤、及び重合条件により調整できる。The average molecular weight of the thermoplastic resin can be adjusted by the polymerization initiator and the polymerization conditions.
【0017】本発明の生分解性繊維は、上記熱可塑性樹
脂を通常の溶融紡糸法、例えばスピンドロー法、高速紡
糸法に付すことにより得ることができる。The biodegradable fiber of the present invention can be obtained by subjecting the above-mentioned thermoplastic resin to a usual melt spinning method such as a spin draw method or a high speed spinning method.
【0018】溶融紡糸時の熱可塑性樹脂の温度は、その
融点以上且つ230℃以下であることが望ましい。より
好ましいのは、生分解性繊維の融点以上210℃以下で
ある。230℃を越えると、生分解性繊維中にラクチド
を再生成しやすい傾向があり、熱劣化する傾向がある。The temperature of the thermoplastic resin during melt spinning is preferably above its melting point and below 230 ° C. More preferably, it is not less than the melting point of the biodegradable fiber and not more than 210 ° C. If it exceeds 230 ° C, lactide tends to be regenerated in the biodegradable fiber, and heat deterioration tends to occur.
【0019】溶融紡糸された未延伸糸は、空冷もしく
は、20〜60℃の水浴又は、油浴中で冷却した後、通
常一度巻き取った後、1段又は2段以上の延伸工程で延
伸される。全延伸倍率は、使用目的と要求性能により異
なるが、通常2〜8倍、好ましくは3〜7倍に延伸す
る。The melt-spun unstretched yarn is air-cooled or cooled in a water bath at 20 to 60 ° C. or an oil bath, and usually wound once, and then stretched in one or more stretching steps. It The total stretching ratio varies depending on the purpose of use and the required performance, but is usually 2 to 8 times, preferably 3 to 7 times.
【0020】本発明の生分解性繊維は、好ましくは12
0℃以上、より好ましくは130℃以上の融点を有す
る。かくして、流通における製品の温度安定性、例えば
夏期における80℃程度の保管にも耐えることができ
る。また、紡糸時の熱可塑性樹脂の熱安定性の点から、
好ましくは200℃以下、より好ましくは180℃以下
である。The biodegradable fiber of the present invention is preferably 12
It has a melting point of 0 ° C. or higher, more preferably 130 ° C. or higher. Thus, it is possible to endure the temperature stability of the product in distribution, for example, storage at about 80 ° C. in summer. Also, from the viewpoint of the thermal stability of the thermoplastic resin during spinning,
The temperature is preferably 200 ° C or lower, more preferably 180 ° C or lower.
【0021】本発明において生分解性繊維の融点とは、
島津製作所製DSC−50を用い、10℃/分の速度で
昇温して測定したものである。In the present invention, the melting point of the biodegradable fiber means
It is measured by using a DSC-50 manufactured by Shimadzu Corporation and heating at a rate of 10 ° C./min.
【0022】生分解性繊維の融点は、環状ラクトン類、
グリコール類、ジカルボン酸等を共重合させることによ
り調整できる。また、乳酸のD/L体比を変えることで
も調整できる。The melting point of the biodegradable fiber is as follows:
It can be adjusted by copolymerizing glycols, dicarboxylic acid and the like. It can also be adjusted by changing the D / L ratio of lactic acid.
【0023】生分解性繊維は、DSCで結晶融解ピーク
を示さない場合は、その流動開始温度は好ましくは10
0〜180℃、より好ましくは120〜180℃であ
る。軟化点が100℃未満であれば、耐熱性が低く、用
途を満足しない傾向があり、180℃を越えると、不織
布等の熱加工性が低くなる傾向がある。When the biodegradable fiber does not show a crystal melting peak in DSC, its flow starting temperature is preferably 10.
The temperature is 0 to 180 ° C, more preferably 120 to 180 ° C. If the softening point is less than 100 ° C, the heat resistance tends to be low and the application tends not to be satisfied.
【0024】ここで流動開始温度とは、ヤナコ社製の精
密融点測定機を用い、せん断応力を加え、流動を示した
温度を流動開始温度とする。昇温温度は5℃/分であ
る。Here, the flow starting temperature is defined as the flow starting temperature by using a precision melting point measuring instrument manufactured by Yanaco Co., Ltd. to which shear stress is applied to indicate flow. The temperature rising temperature is 5 ° C./minute.
【0025】生分解性繊維の流動開始温度は、共重合
物、及び共重合比により調整できる。The flow initiation temperature of the biodegradable fiber can be adjusted by the copolymer and the copolymerization ratio.
【0026】また、本発明の生分解性繊維は、その中に
含まれる低分子量化合物の量が1重量%以下である。好
ましくは0.5重量%以下であり、さらに好ましくは
0.3重量%である。生分解性繊維中の低分子量化合物
の含量が1重量%を越えると、室温での経時安定性が悪
くなる。In the biodegradable fiber of the present invention, the amount of the low molecular weight compound contained therein is 1% by weight or less. It is preferably 0.5% by weight or less, and more preferably 0.3% by weight. When the content of the low molecular weight compound in the biodegradable fiber exceeds 1% by weight, the stability with time at room temperature deteriorates.
【0027】本発明において低分子量化合物とは、乳
酸、ラクチド、ラクチル乳酸を示し、低分子量化合物の
含量とは、乳酸、ラクチド、ラクチル乳酸の合計量で表
す。In the present invention, the low molecular weight compound means lactic acid, lactide and lactyl lactic acid, and the content of the low molecular weight compound means the total amount of lactic acid, lactide and lactyl lactic acid.
【0028】ここで低分子量化合物の含量とは、液体ク
ロマトグラフィー法に基づき、オクタデシルシラン(O
DS)カラムを用いて逆相高速液体クロマトグラフィー
にて測定したものである。Here, the content of low molecular weight compound means octadecylsilane (O) based on the liquid chromatography method.
It is measured by reverse phase high performance liquid chromatography using a DS column.
【0029】生分解性繊維中の低分子量化合物の含量
は、熱可塑性樹脂中の低分子量化合物の含量を低下させ
たり、紡糸中の低分子量化合物の生成をおさえることに
より調整できる。すなわち、熱可塑性樹脂中の低分子量
化合物を減圧除去、又は溶媒に溶解し再沈澱精製した
り、紡糸中の解重合をおさえる触媒(重合後は除去する
か、又は失活させることが望ましい)を用いたりするこ
と等である。The content of the low molecular weight compound in the biodegradable fiber can be adjusted by lowering the content of the low molecular weight compound in the thermoplastic resin or suppressing the production of the low molecular weight compound during spinning. That is, a low molecular weight compound in the thermoplastic resin is removed under reduced pressure, or dissolved in a solvent for purification by reprecipitation, or a catalyst for suppressing depolymerization during spinning (preferably removed or deactivated after polymerization). It is used and so on.
【0030】本発明の生分解性繊維は、その引張強度が
2.5g/d以上、引張破断伸度が10%以上であるこ
とが好ましい。The biodegradable fiber of the present invention preferably has a tensile strength of 2.5 g / d or more and a tensile elongation at break of 10% or more.
【0031】本発明の生分解性繊維の引張強度は、前記
のように2.5g/d以上であることが好ましく、より
好ましくは4g/d以上である。引張強度が2.5g/
dに満たないと、土木建築資材用途、漁業資材用途、農
業資材用途、その他産業資材用途、衣料用途として用い
るには、引張強度が不足であって好ましくない。As described above, the tensile strength of the biodegradable fiber of the present invention is preferably 2.5 g / d or more, more preferably 4 g / d or more. Tensile strength is 2.5g /
If it is less than d, the tensile strength is insufficient for use in civil engineering / construction material applications, fishery material applications, agricultural material applications, other industrial material applications, and clothing applications.
【0032】本発明において引張強度とは、JIS L
1013に準じて測定したものである。In the present invention, tensile strength means JIS L
It is measured according to 1013.
【0033】生分解性繊維の引張強度は、紡糸延伸条件
により調整できる。The tensile strength of the biodegradable fiber can be adjusted by spinning and drawing conditions.
【0034】また、本発明の生分解性繊維は、糸物性の
点から、その引張破断伸度が10%以上であることが好
ましく、20〜100%の範囲であることがより好まし
い。The biodegradable fiber of the present invention has a tensile elongation at break of preferably 10% or more, more preferably 20 to 100%, from the viewpoint of yarn physical properties.
【0035】本発明において引張破断伸度とは、JIS
L1013に準じて測定したものである。In the present invention, the tensile elongation at break means JIS.
It is measured according to L1013.
【0036】生分解性繊維の引張破断伸度は、紡糸延伸
条件により調整できる。The tensile elongation at break of the biodegradable fiber can be adjusted by spinning and drawing conditions.
【0037】本発明の生分解性繊維は、引張強度及び引
張破断伸度が上記範囲であることに加えて、その結節強
度が1.5g/d以上であることが好ましく、2.0g
/d以上がより好ましい。結節強度が1.5g/dに満
たないと、土木建築資材用途、漁業資材用途、農業資材
用途、その他産業資材用途、衣料用途として用いる場合
に要求される糸物性を満足できない傾向がある。The biodegradable fiber of the present invention preferably has a knot strength of 1.5 g / d or more, in addition to the tensile strength and the tensile elongation at break in the above-mentioned ranges.
/ D or more is more preferable. If the knot strength is less than 1.5 g / d, there is a tendency that the yarn physical properties required when used for civil engineering / construction material applications, fishery material applications, agricultural material applications, other industrial material applications, and clothing applications cannot be satisfied.
【0038】本発明において結節強度とは、JIS L
1013に基づいて測定したものである。In the present invention, knot strength means JIS L
1013 based on measurement.
【0039】本発明の生分解性繊維は、マルチフィラメ
ント又はモノフィラメント、或いは短繊維又は長繊維不
織布の形態として用いることができる。The biodegradable fiber of the present invention can be used in the form of multifilament or monofilament, or short fiber or long fiber non-woven fabric.
【0040】上記モノフィラメントとは、1本からなる
繊維のことで、前記紡糸法によって得ることができる。The above-mentioned monofilament is a fiber composed of one fiber, and can be obtained by the spinning method.
【0041】上記マルチフィラメントとは、モノフィラ
メントが2〜100本の束となった繊維のことであり、
これらは、モノフィラメントと同様の方法によって得る
ことができる。The multifilament is a fiber in which 2 to 100 monofilaments are bundled,
These can be obtained by the same method as the monofilament.
【0042】また、短繊維とは、繊維長2〜80mm程
度の長さを有する繊維であり、紡績糸、湿式不織布、乾
式不織布等に用いられる。通常、紡績糸に用いる場合、
繊維長は20〜80mm、好ましくは30〜70mm、
湿式不織布に用いる場合は2〜10mm、好ましくは2
〜8mm、乾式不織布に用いる場合は20〜80mm、
好ましくは20〜70mm程度である。本発明の短繊維
は、例えば溶融紡糸し、延伸した後、又は高速紡糸した
後、得られることができる。The short fiber is a fiber having a fiber length of about 2 to 80 mm and is used for spun yarn, wet non-woven fabric, dry non-woven fabric and the like. Normally, when used for spun yarn,
The fiber length is 20 to 80 mm, preferably 30 to 70 mm,
When used in a wet non-woven fabric, it is 2 to 10 mm, preferably 2
~ 8 mm, 20-80 mm when used for dry non-woven fabric,
It is preferably about 20 to 70 mm. The staple fiber of the present invention can be obtained, for example, after melt spinning, drawing, or high speed spinning.
【0043】上記湿式不織布とは、液体中に短繊維を分
散し抄造後、乾燥することにより得られる不織布であ
り、乾式不織布とは、カード、ローラ等で開繊後、ウェ
ッバーによりウェッブとし、必要に応じ部分的、又は全
体に融着させたり、三次元に交絡させた不織布である。The above-mentioned wet non-woven fabric is a non-woven fabric obtained by dispersing short fibers in a liquid, paper-making and drying, and the dry-type non-woven fabric is opened with a card, a roller or the like, and then made into a web with a webber, which is required. It is a non-woven fabric which is partially or wholly fused or entangled three-dimensionally.
【0044】生分解性短繊維には、カード開繊性を良く
するために、捲縮加工を加えることができる。捲縮加工
方法は特に限定されるものではなく、公知の方法を用い
ることができ、例えば押し込みギアー法、スタフィング
ボックス法を使用することができる。The biodegradable short fibers may be crimped in order to improve the card opening property. The crimping method is not particularly limited, and a known method can be used, for example, a pushing gear method or a stuffing box method can be used.
【0045】捲縮数は5〜50コ/25mm、好ましく
は10〜30コ/25mmが好適である。捲縮数が5コ
/25mmより少ないと、開繊時未開繊部分が生じ易い
傾向があり、50コ/25mmを越えると均一な開繊が
得られない傾向がある。ここで捲縮数とは、JIS L
1015に準じて測定したものである。The number of crimps is 5 to 50/25 mm, preferably 10 to 30/25 mm. If the number of crimps is less than 5/25 mm, unopened portions are likely to occur during opening, and if it exceeds 50/25 mm, uniform opening tends not to be obtained. Here, the number of crimps means JIS L
It is measured according to 1015.
【0046】また、捲縮率は5%以上であり、好ましく
は8%以上である。捲縮率が5%未満であると、カード
にかけた時、均一なウェブが得にくく、疎密部分が発生
する傾向がある。ここで捲縮率とは、JIS L101
5に準じて測定したものである。The crimping rate is 5% or more, preferably 8% or more. When the crimping rate is less than 5%, it is difficult to obtain a uniform web when applied to a card, and a sparse and dense portion tends to occur. Here, the crimp ratio means JIS L101.
It was measured according to 5.
【0047】本発明の生分解性繊維を用いてなる短繊維
不織布は、上記短繊維を用い、自体既知の方法で製造す
ればよいが、例えば短繊維をローラーカードによりカー
ディングし、ウェブとし、必要に応じてニードルパンチ
加工、カレンダー加工、エンボス加工等により交絡また
は接着することにより製造できる。また、必要により繊
維方向性をランダムウェバーにより変えることができ
る。The short fiber nonwoven fabric using the biodegradable fiber of the present invention may be produced by a method known per se using the above short fibers. For example, short fibers are carded with a roller card to form a web, If necessary, it can be produced by entanglement or adhesion by needle punching, calendaring, embossing or the like. If necessary, the fiber orientation can be changed by a random webber.
【0048】また、本発明の生分解性繊維を用いてなる
長繊維不織布は、自体既知の方法で製造すればよいが、
例えばスパンボンド法またはメルトブロー法により製造
することができる。スパンボンド法とは、熱可塑性樹脂
を融点以上に加熱溶融し、紡糸口金より紡出し、紡出さ
れた長繊維を冷却固化しながら下部に設置されたエアー
サッカー等の引取り手段により2000m/min以上
の引取り速度により牽引し、その後開繊し定速で移動し
ているエンドレスの捕集面に補集しウェブとし、これを
エンボス加工、カレンダー加工により全体または部分的
に熱圧着する、或いはニードルパンチ加工、水流交絡加
工により交絡する方法である。メルトブロー法とは、熱
可塑性樹脂を融点以上に加熱溶融し一直線に配列された
紡糸孔を有する紡糸口金より吐出し紡糸ノズルの両サイ
ドから高速噴出する高温高圧エアーによってマイクロフ
ァイバー化する。その後定速で移動しているエンドレス
の捕集面に補集しウェブとし、これをエンボス加工、カ
レンダー加工により全体または部分的に熱圧着する、或
いはニードルパンチ加工、水流交絡加工により交絡する
方法である。The long-fiber non-woven fabric using the biodegradable fiber of the present invention may be manufactured by a method known per se.
For example, it can be manufactured by a spun bond method or a melt blow method. The spunbond method is a method in which a thermoplastic resin is heated and melted to a temperature equal to or higher than the melting point, spun from a spinneret, and the spun long fibers are cooled and solidified while being cooled and solidified by an air sucker or the like to be installed at 2000 m / min Tow at the above take-up speed, then open the fiber and collect it on the endless collection surface moving at a constant speed to form a web, which is thermo-compressed wholly or partially by embossing or calendering, or It is a method of entanglement by needle punching and hydroentanglement. In the melt blow method, a thermoplastic resin is heated and melted to a temperature equal to or higher than the melting point, discharged from a spinneret having spinning holes arranged in a straight line, and made into microfibers by high-temperature and high-pressure air jetted at high speed from both sides of a spinning nozzle. After that, it collects on the endless collecting surface moving at a constant speed to form a web, which is thermocompressed wholly or partially by embossing or calendering, or entangled by needle punching or hydroentanglement. is there.
【0049】本発明の生分解性繊維には、帯電防止性、
集束性を考慮して、ラウリルホスフェートカリウム塩等
のアニオン系界面活性剤、四級アンモニウム塩等のカチ
オン系界面活性剤、脂肪族高級アルコールや高級脂肪酸
のエチレンオキサイド付加物等のノニオン系界面活性
剤、ポリエチレングリコール、ポリエチレングリコール
・ポリプロピレングリコールブロック共重合体等のポリ
アルキレングリコール類、ジメチルポリシロキサン、ポ
リエーテル変性シリコーンオイル、高級アルコキシ変性
シリコーンオイル等のシリコーンオイル類を一種又は二
種以上付与することができる。The biodegradable fiber of the present invention has an antistatic property,
Considering the focusing property, anionic surfactants such as lauryl phosphate potassium salt, cationic surfactants such as quaternary ammonium salt, nonionic surfactants such as ethylene oxide adducts of higher aliphatic alcohols and higher fatty acids. One or more kinds of silicone oils such as polyalkylene glycols such as polyethylene glycol and polyethylene glycol / polypropylene glycol block copolymers, dimethylpolysiloxane, polyether modified silicone oil, higher alkoxy modified silicone oil, etc. it can.
【0050】本発明に用いる生分解性繊維には、熱可塑
性樹脂、ポリカプロラクトン等の他の脂肪族ポリエステ
ル、ポリビニルアルコール、ポリアルキレングリコー
ル、ポリアミノ酸等のポリマー、タルク、炭酸カルシウ
ム、硫酸カルシウム、塩化カルシウム等の無機物、デン
プン、タンパク質、食品添加物等を一種又は二種以上、
適量混合することができ、機械特性、生分解特性等を種
々変化させることができる。The biodegradable fibers used in the present invention include thermoplastic resins, other aliphatic polyesters such as polycaprolactone, polymers such as polyvinyl alcohol, polyalkylene glycol and polyamino acid, talc, calcium carbonate, calcium sulfate and chloride. One or more inorganic substances such as calcium, starch, protein, food additives, etc.,
An appropriate amount can be mixed, and various mechanical properties, biodegradation properties, etc. can be changed.
【0051】本発明の生分解性繊維には、上記以外に必
要に応じて酸化防止剤、紫外線吸収剤、可塑剤等の公知
の添加剤が配合されていてもよい。In addition to the above, the biodegradable fiber of the present invention may be mixed with known additives such as an antioxidant, an ultraviolet absorber and a plasticizer, if necessary.
【0052】[0052]
【実施例】以下実施例をあげて、本発明をさらに説明す
る。また、各測定法を以下に説明する。The present invention will be further described with reference to the following examples. Moreover, each measuring method is demonstrated below.
【0053】低分子量化合物の含量は、液体クロマトグ
ラフィー法に基づき、オクタデシルシラン(ODS)カ
ラムを用いて逆相高速液体クロマトグラフィーにて測定
した。The content of low molecular weight compounds was measured by reversed phase high performance liquid chromatography using an octadecylsilane (ODS) column based on the liquid chromatography method.
【0054】還元比粘度は、試料を精秤し、0.5g/
dlとなるようにクロロホルムに溶解し、該溶液につい
て、25℃でウベローデ型粘度計を用いて測定した。The reduced specific viscosity is 0.5 g /
It was dissolved in chloroform so as to have a dl, and the solution was measured at 25 ° C. using an Ubbelohde viscometer.
【0055】引張強度、引張破断伸度および結節強度
は、JIS L1013に基づいて測定した。The tensile strength, tensile breaking elongation and knot strength were measured according to JIS L1013.
【0056】融点は、島津製作所製DSC−50を用
い、10℃/分の速度で昇温して測定した。The melting point was measured by using DSC-50 manufactured by Shimadzu Corp., while raising the temperature at a rate of 10 ° C./min.
【0057】強度保持率は、繊維の初期の引張強度と、
室温25℃、相対湿度60%中に12ヵ月放置した後の
繊維の引張強度を測定し、(式2)により求めた。 強度保持率(%)=(T/T0 )×100 (式2) 〔式中、Tは室温25℃、相対湿度60%中に12ヵ月
放置後の繊維の引張強度(g/d)、T0 は繊維の初期
引張強度(g/d)である〕The strength retention is defined as the initial tensile strength of the fiber,
The tensile strength of the fiber after standing for 12 months in a room temperature of 25 ° C. and a relative humidity of 60% was measured and determined by (Equation 2). Strength retention rate (%) = (T / T 0 ) × 100 (Equation 2) [In the equation, T is the tensile strength (g / d) of the fiber after standing for 12 months at room temperature of 25 ° C. and relative humidity of 60%, T 0 is the initial tensile strength (g / d) of the fiber]
【0058】生分解性については、土壌中に、繊維を埋
没させ、6ヵ月後の分解状態を走査型電子顕微鏡(SE
M:Scanning Electron Microscope)にて評価した。形
状が失われている場合(表面に凹凸が生じる、破断する
等)を生分解性良好とした。Regarding the biodegradability, the fiber was buried in the soil, and the state of degradation after 6 months was examined by a scanning electron microscope (SE).
M: Scanning Electron Microscope). When the shape was lost (irregularities on the surface, breakage, etc.), the biodegradability was considered good.
【0059】実施例1 還元比粘度が1.57である、分子末端のカルボキシル
基をラウリルアルコールでエステル化したポリ乳酸を、
紡糸温度190℃で直径3mmの紡糸孔を20個有する
紡糸ノズルから、紡速300m/minで溶融紡糸し
た。未延伸糸を一旦巻取った後、140℃で4.5倍に
延伸し、単糸繊度2.1d、低分子量化合物含量0.2
重量%の繊維を得た。Example 1 A polylactic acid obtained by esterifying a carboxyl group at the molecular end with lauryl alcohol, having a reduced specific viscosity of 1.57, was prepared.
Melt spinning was performed at a spinning speed of 300 m / min from a spinning nozzle having a spinning temperature of 190 ° C. and 20 spinning holes having a diameter of 3 mm. After unwinding the undrawn yarn, it was drawn 4.5 times at 140 ° C. to obtain a single yarn fineness of 2.1 d and a low molecular weight compound content of 0.2.
A weight percent of fiber was obtained.
【0060】実施例2 還元比粘度が1.54であるポリ乳酸を、紡糸温度20
0℃で直径0.3mmの紡糸孔を20個有する紡糸ノズ
ルから、紡速300m/minで溶融紡糸した。未延伸
糸を一旦巻取った後、140℃で4.5倍に延伸し、単
糸繊度2.2d、低分子量化合物含量0.4重量%の繊
維を得た。Example 2 Polylactic acid having a reduced specific viscosity of 1.54 was prepared at a spinning temperature of 20.
Melt spinning was performed at 0 ° C. from a spinning nozzle having 20 spinning holes with a diameter of 0.3 mm at a spinning speed of 300 m / min. The undrawn yarn was once wound and then drawn 4.5 times at 140 ° C. to obtain a fiber having a single yarn fineness of 2.2 d and a low molecular weight compound content of 0.4% by weight.
【0061】実施例3 還元比粘度が1.55であるポリ乳酸を、紡糸温度19
0℃で直径0.3mmの紡糸孔を20個有する紡糸ノズ
ルから、紡速300m/minで溶融紡糸した。未延伸
糸を一旦巻取った後、140℃で4.5倍に延伸し、単
糸繊度2.2d、低分子量化合物含量0.9重量%の繊
維を得た。Example 3 Polylactic acid having a reduced specific viscosity of 1.55 was added at a spinning temperature of 19
Melt spinning was performed at 0 ° C. from a spinning nozzle having 20 spinning holes with a diameter of 0.3 mm at a spinning speed of 300 m / min. The unstretched yarn was once wound up and then stretched 4.5 times at 140 ° C. to obtain a fiber having a single yarn fineness of 2.2 d and a low molecular weight compound content of 0.9% by weight.
【0062】実施例4 還元比粘度が1.73であるポリ乳酸を、紡糸温度19
0℃で直径1.0mmの紡糸孔を1個有する紡糸ノズル
から溶融紡糸し、水浴中(30℃)で固化させ、紡速2
0m/minで紡糸した。未延伸糸を一旦巻取った後、
140℃で5倍に延伸し、繊度380d、低分子量化合
物含量0.8重量%の繊維を得た。Example 4 Polylactic acid having a reduced specific viscosity of 1.73 was added at a spinning temperature of 19
Melt spinning from a spinning nozzle having one spinning hole with a diameter of 1.0 mm at 0 ° C., solidify in a water bath (30 ° C.), and spin speed 2
It was spun at 0 m / min. After winding the undrawn yarn once,
It was stretched 5 times at 140 ° C. to obtain a fiber having a fineness of 380 d and a low molecular weight compound content of 0.8% by weight.
【0063】比較例1 還元比粘度が1.56であるポリ乳酸を、紡糸温度19
0℃で直径0.3mmの紡糸孔を20個有する紡糸ノズ
ルから、紡速300m/minで溶融紡糸した。未延伸
糸を一旦巻取った後、140℃で4.5倍に延伸し、単
糸繊度2.0d、低分子量化合物含量3.0重量%の繊
維を得た。Comparative Example 1 Polylactic acid having a reduced specific viscosity of 1.56 was spun at a spinning temperature of 19
Melt spinning was performed at 0 ° C. from a spinning nozzle having 20 spinning holes with a diameter of 0.3 mm at a spinning speed of 300 m / min. The undrawn yarn was once wound and then drawn 4.5 times at 140 ° C. to obtain a fiber having a single yarn fineness of 2.0 d and a low molecular weight compound content of 3.0 wt%.
【0064】比較例2 還元比粘度が1.56であるポリ乳酸を、紡糸温度22
0℃で直径0.3mmの紡糸孔を20個有する紡糸ノズ
ルから、紡速300m/minで溶融紡糸した。未延伸
糸を一旦巻取った後、140℃で4.5倍に延伸し、単
糸繊度2.1d、低分子量化合物含量2.2重量%の繊
維を得た。Comparative Example 2 Polylactic acid having a reduced specific viscosity of 1.56 was used at a spinning temperature of 22.
Melt spinning was performed at 0 ° C. from a spinning nozzle having 20 spinning holes with a diameter of 0.3 mm at a spinning speed of 300 m / min. The unstretched yarn was once wound up and then stretched 4.5 times at 140 ° C. to obtain a fiber having a single yarn fineness of 2.1 d and a low molecular weight compound content of 2.2% by weight.
【0065】比較例3 還元比粘度が1.54であるポリ乳酸を、紡糸温度23
0℃で直径0.3mmの紡糸孔を20個有する紡糸ノズ
ルから、紡速300m/minで溶融紡糸した。未延伸
糸を一旦巻取った後、140℃で4.5倍に延伸し、単
糸繊度2.1d、低分子量化合物含量5.1重量%の繊
維を得た。Comparative Example 3 Polylactic acid having a reduced specific viscosity of 1.54 was added at a spinning temperature of 23.
Melt spinning was performed at 0 ° C. from a spinning nozzle having 20 spinning holes with a diameter of 0.3 mm at a spinning speed of 300 m / min. After unwinding the undrawn yarn, it was drawn 4.5 times at 140 ° C. to obtain a fiber having a single yarn fineness of 2.1 d and a low molecular weight compound content of 5.1% by weight.
【0066】比較例4 還元比粘度が1.78であるポリ乳酸を、紡糸温度19
0℃で直径1.0mmの紡糸孔を1個有する紡糸ノズル
から溶融紡糸し、水浴中(30℃)で固化させ、紡速2
0m/minで紡糸した。未延伸糸を一旦巻取った後、
140℃で5倍に延伸し、繊度380d、低分子量化合
物含量3.5重量%の繊維を得た。Comparative Example 4 Polylactic acid having a reduced specific viscosity of 1.78 was added at a spinning temperature of 19
Melt spinning from a spinning nozzle having one spinning hole with a diameter of 1.0 mm at 0 ° C., solidify in a water bath (30 ° C.), and spin speed 2
It was spun at 0 m / min. After winding the undrawn yarn once,
The fiber was stretched 5 times at 140 ° C. to obtain a fiber having a fineness of 380 d and a low molecular weight compound content of 3.5 wt%.
【0067】実施例1〜4、比較例1〜4で得られた繊
維物性値、及び生分解性の評価結果を表1に示す。Table 1 shows the fiber physical property values obtained in Examples 1 to 4 and Comparative Examples 1 to 4 and the evaluation results of biodegradability.
【0068】[0068]
【表1】 [Table 1]
【0069】表1より本発明の生分解性繊維が、優れた
生分解性と良好な物性を有し、室温での強度保持率も良
く、耐熱性にも優れていることが分かった。From Table 1, it was found that the biodegradable fiber of the present invention has excellent biodegradability and good physical properties, has a good strength retention rate at room temperature, and is also excellent in heat resistance.
【0070】実施例5 実施例1で得られた生分解性繊維を、スタフィングボッ
クス法で捲縮加工した後、64mmにカットし、生分解
性短繊維を得た。得られた短繊維をランダムウェッバー
により目付け100g/m2 のウェブとした後、ニード
ルパンチ処理し不織布を得た。Example 5 The biodegradable fiber obtained in Example 1 was crimped by a stuffing box method and then cut into 64 mm to obtain biodegradable short fibers. The obtained short fibers were made into a web having a basis weight of 100 g / m 2 by a random webber and then needle punched to obtain a nonwoven fabric.
【0071】実施例6 還元比粘度が1.51の分子末端カルボキシル基をラウ
リルアルコールでエステル化したポリ乳酸を、スパンボ
ンド法で目付100g/cm2 の不織布を得た。紡糸条
件は、紡糸温度200℃で直径0.3mmの紡糸孔を有
する紡糸ノズルから吐出量=0.8g/min.孔、牽
引速度=3500m/min.であった。スパンボンド
不織布の低分子量化合物の含量は0.5%で、融点は1
73℃であった。Example 6 A polylactic acid obtained by esterifying a terminal carboxyl group of a molecule having a reduced specific viscosity of 1.51 with lauryl alcohol was obtained by a spunbond method to obtain a nonwoven fabric having a basis weight of 100 g / cm 2 . The spinning conditions are as follows: a spinning temperature of 200 ° C., and a discharge amount of 0.8 g / min. Hole, pulling speed = 3500 m / min. Met. The content of low molecular weight compounds in spunbonded non-woven fabric is 0.5% and the melting point is 1
73 ° C.
【0072】実施例7 還元比粘度が1.21のポリ乳酸を、紡糸温度210
℃、空気温度210℃、吐出量=0.8g/min.孔
の条件でメルトブロー法により平均繊維径3.5μm、
目付100g/cm2 のメルトブロー不織布を得た。メ
ルトブロー不織布の低分子量化合物の含量は0.8%
で、融点は172℃であった。Example 7 Polylactic acid having a reduced specific viscosity of 1.21 was added at a spinning temperature of 210.
° C, air temperature 210 ° C, discharge rate = 0.8 g / min. Average fiber diameter of 3.5μm by melt blow method under pore condition,
A melt blown nonwoven fabric having a basis weight of 100 g / cm 2 was obtained. The content of low molecular weight compounds in meltblown nonwoven fabric is 0.8%
And the melting point was 172 ° C.
【0073】実施例5、6、7の不織布の生分解性を評
価したところ生分解性は良好であった。When the biodegradability of the nonwoven fabrics of Examples 5, 6, and 7 was evaluated, the biodegradability was good.
【0074】[0074]
【発明の効果】本発明の生分解性繊維は、ポリ乳酸系の
生分解性繊維であり、しかも経時安定性(強度保持率)
に優れ、且つ強度及び実用耐熱性をもち、実用性があり
且つ比較的安価な生分解性繊維である。また、本発明の
生分解性繊維は、生活資材、農業資材、漁業資材、土木
建築資材、その他産業資材、衣料に好適であり、自然界
において完全生分解性を有する。Industrial Applicability The biodegradable fiber of the present invention is a polylactic acid type biodegradable fiber, and has stability over time (strength retention rate).
It is a biodegradable fiber that has excellent properties, strength, and practical heat resistance, is practical, and is relatively inexpensive. Further, the biodegradable fiber of the present invention is suitable for living materials, agricultural materials, fishery materials, civil engineering and construction materials, other industrial materials, and clothing, and has complete biodegradability in the natural world.
Claims (10)
る共重合物からなる熱可塑性樹脂を含んでなり、低分子
量化合物の含量が1重量%以下であることを特徴とする
生分解性繊維。1. A biodegradable fiber comprising a thermoplastic resin composed of polylactic acid and / or a copolymer mainly composed of polylactic acid, and containing a low molecular weight compound in an amount of 1% by weight or less. .
又は流動開始温度が100〜180℃の範囲にある請求
項1記載の生分解性繊維。2. The biodegradable fiber according to claim 1, which has a melting point in the range of 120 to 200 ° C. or a flow starting temperature in the range of 100 to 180 ° C.
物によって該熱可塑性樹脂中のカルボキシル基をエステ
ル化されてなるものである請求項1または2記載の生分
解性繊維。3. The biodegradable fiber according to claim 1, wherein the thermoplastic resin is obtained by esterifying a carboxyl group in the thermoplastic resin with a compound having a hydroxyl group.
度10%以上である請求項1〜3のいずれかに記載の生
分解性繊維。4. The biodegradable fiber according to claim 1, which has a tensile strength of 2.5 g / d or more and a tensile elongation at break of 10% or more.
度10%以上、結節強度1.5g/d以上である請求項
1〜3記載のいずれかに生分解性繊維。5. The biodegradable fiber according to claim 1, which has a tensile strength of 2.5 g / d or more, a tensile elongation at break of 10% or more, and a knot strength of 1.5 g / d or more.
1〜5のいずれかに記載の生分解性繊維。6. The biodegradable fiber according to claim 1, which is in the form of a multifilament.
〜5のいずれかに記載の生分解性繊維。7. A monofilament form.
6. The biodegradable fiber according to any one of to 5.
れかに記載の生分解性繊維。8. The biodegradable fiber according to claim 1, which is in the form of short fibers.
る短繊維不織布。9. A short fiber non-woven fabric comprising the biodegradable fiber according to claim 8.
解性繊維を用いてなる長繊維不織布。10. A long-fiber nonwoven fabric comprising the biodegradable fiber according to any one of claims 1 to 3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17114295A JP3666059B2 (en) | 1995-07-06 | 1995-07-06 | Biodegradable fiber and non-woven fabric using the same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17114295A JP3666059B2 (en) | 1995-07-06 | 1995-07-06 | Biodegradable fiber and non-woven fabric using the same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0921018A true JPH0921018A (en) | 1997-01-21 |
| JP3666059B2 JP3666059B2 (en) | 2005-06-29 |
Family
ID=15917773
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|---|---|---|---|
| JP17114295A Expired - Lifetime JP3666059B2 (en) | 1995-07-06 | 1995-07-06 | Biodegradable fiber and non-woven fabric using the same |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002038365A (en) * | 2000-07-31 | 2002-02-06 | Toray Ind Inc | Nonwoven fabric for civil engineering and method for producing the same |
| JP2002065079A (en) * | 2000-08-30 | 2002-03-05 | Unitika Ltd | Young tree protection sheet |
| WO2004020708A1 (en) * | 2002-08-30 | 2004-03-11 | Toray Industries, Inc. | Polylactic acid fiber, yarn package, and textile product |
| JP2004189770A (en) * | 2002-12-06 | 2004-07-08 | Uniplas Shiga Kk | Biodegradable resin composition |
| JP2005307428A (en) * | 1999-06-18 | 2005-11-04 | Toray Ind Inc | Polylactic acid monofilament and method for producing the same |
| US7994078B2 (en) | 2002-12-23 | 2011-08-09 | Kimberly-Clark Worldwide, Inc. | High strength nonwoven web from a biodegradable aliphatic polyester |
| JP2014019992A (en) * | 2012-07-23 | 2014-02-03 | Nippon Ester Co Ltd | Short fiber nonwoven fabric of high elongation |
-
1995
- 1995-07-06 JP JP17114295A patent/JP3666059B2/en not_active Expired - Lifetime
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005307428A (en) * | 1999-06-18 | 2005-11-04 | Toray Ind Inc | Polylactic acid monofilament and method for producing the same |
| JP2005307427A (en) * | 1999-06-18 | 2005-11-04 | Toray Ind Inc | Polylactic acid staple fiber and method for producing the same |
| US7989061B2 (en) | 1999-06-18 | 2011-08-02 | Toray Industries, Inc. | Polylactic acid resin, textile products obtained therefrom, and processes for producing textile products |
| JP2002038365A (en) * | 2000-07-31 | 2002-02-06 | Toray Ind Inc | Nonwoven fabric for civil engineering and method for producing the same |
| JP2002065079A (en) * | 2000-08-30 | 2002-03-05 | Unitika Ltd | Young tree protection sheet |
| WO2004020708A1 (en) * | 2002-08-30 | 2004-03-11 | Toray Industries, Inc. | Polylactic acid fiber, yarn package, and textile product |
| US8101688B2 (en) | 2002-08-30 | 2012-01-24 | Toray Industries., Inc. | Polylactic acid fiber yarn package, and textile products |
| JP2004189770A (en) * | 2002-12-06 | 2004-07-08 | Uniplas Shiga Kk | Biodegradable resin composition |
| US7994078B2 (en) | 2002-12-23 | 2011-08-09 | Kimberly-Clark Worldwide, Inc. | High strength nonwoven web from a biodegradable aliphatic polyester |
| JP2014019992A (en) * | 2012-07-23 | 2014-02-03 | Nippon Ester Co Ltd | Short fiber nonwoven fabric of high elongation |
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