WO2008029934A1 - Fibre d'acide polylactique et procédé de fabrication - Google Patents
Fibre d'acide polylactique et procédé de fabrication Download PDFInfo
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- WO2008029934A1 WO2008029934A1 PCT/JP2007/067548 JP2007067548W WO2008029934A1 WO 2008029934 A1 WO2008029934 A1 WO 2008029934A1 JP 2007067548 W JP2007067548 W JP 2007067548W WO 2008029934 A1 WO2008029934 A1 WO 2008029934A1
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- lactic acid
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/88—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds
- D01F6/92—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds of polyesters
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/08—Melt spinning methods
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/08—Melt spinning methods
- D01D5/084—Heating filaments, threads or the like, leaving the spinnerettes
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/10—Other agents for modifying properties
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
- D01F6/62—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters
- D01F6/625—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters derived from hydroxy-carboxylic acids, e.g. lactones
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- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2401/00—Physical properties
- D10B2401/04—Heat-responsive characteristics
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2401/00—Physical properties
- D10B2401/06—Load-responsive characteristics
Definitions
- the present invention relates to a fiber made of polylactic acid and having practical strength, heat resistance, and low heat shrinkage, and a method for producing the same.
- the present invention also relates to a fiber product comprising the fiber.
- biodegradable polymers that are degraded in the natural environment have attracted attention and are being studied around the world.
- the biodegradable polymer polyhydroxy propylate, poly strength prolactone, aliphatic polyester, and polylactic acid are known. These can be melt-molded and are expected to be versatile polymers.
- polylactic acid which is the raw material of lactic acid or lactide, can be produced from natural products, so that it is not only used as a biodegradable polymer but also as a versatile polymer that is friendly to the global environment. is there.
- Polylactic acid is highly transparent and strong, but it is easily hydrolyzed in the presence of water and decomposes without polluting the environment after disposal, so it is expected as a general-purpose polymer with little environmental impact.
- the melting point of polylactic acid is in the range of 1550 to 1700 ° C, and when used as clothing fiber, it is limited to the temperature force S that can be ironed. In addition, when used as an industrial fiber, there are problems such as that it is not suitable for rubber materials and resin-coated cloths that are exposed to high temperatures of about 150,000.
- PLLA poly-L-lactic acid consisting of only L-lactic acid units
- PDLA poly-D-lactic acid consisting of only D-lactic acid units
- Patent Document 1 discloses a stereocomplex polylactic acid fiber obtained by melt spinning a composition containing equimolar amounts of poly L-lactic acid and poly D-lactic acid, but has insufficient heat resistance and is practically used. Not enough to serve.
- Non-Patent Document 2 describes that a stereocomplex polylactic acid fiber is obtained by melt spinning.
- This document describes that a stereocomplex fiber is obtained by heat-treating an undrawn yarn obtained by melt spinning a melt blend of poly L-monolactic acid and poly-D-lactic acid. The molecular orientation of the fiber relaxes and the strength of the resulting fiber remains at 2.3 c NZ d Te x.
- the conventional stereocomplex formation method involves drawing and heat-treating an amorphous undrawn yarn obtained by spinning a blend of poly L monolactic acid and poly D-lactic acid.
- Patent Document 2 proposes a method of forming a stereocomplex at once from a melt of polylactic acid on a spinning line.
- an undrawn crystallized yarn with a spinning rate of 4,00 O mZ and a stereo ratio of 10-35% as measured by wide-angle X-ray diffraction (XRD) is 1.4-2.3. It has been proposed to improve the partial fusion of yarns by double-stretching.
- XRD wide-angle X-ray diffraction
- a spinning speed of about 3,00 O m / min is not sufficient, and a special spinning facility is required for spinning at a spinning speed of 5, 00 O mZ or more.
- the evaluation of heat resistance in this proposal is based on a drastic change such as breaking the fabric by applying an iron at 1700 to the fiber knitting and rough hardening. Not The study on heat resistance is insufficient. Thus, the present situation is that a technique for producing a fiber having a high stereoization ratio and excellent strength and heat shrinkage resistance from an undrawn yarn having a stereoization ratio of 0% has not been completed.
- Patent Document 3 discloses that an undrawn yarn melt-spun with a spinning draft ⁇ 50 and take-up speed ⁇ 30 ⁇ is drawn out after being drawn or drawn 2.8 times without winding. And a heat-resistant fiber at 200 ° C. having two peaks of a polylactic acid homocrystal and a stereocomplex crystal at 190 ° C. or higher has been proposed.
- Patent Document 4 proposes that polylactic acid capable of forming a stereocomplex contains a phosphate metal salt as a crystal nucleating agent to improve the heat resistance and impact resistance of a molded product.
- Patent Document 1 Japanese Patent Laid-Open No. 63-241024
- Patent Document 2 Japanese Unexamined Patent Publication No. 2003-293220
- Patent Document 3 Japanese Unexamined Patent Publication No. 2005-23512
- Patent Document 4 Japanese Unexamined Patent Publication No. 2003-192884
- Non-patent document 1 Macro 1 e c u 1 e s, 24, 5651 (19
- Non-Patent Document 2 S en i Ga k ka i P r e r i n t s (19
- the present inventors made a substantially non-crystalline substance when a phosphate ester metal salt (component C) was present. It was found that an undrawn yarn comprising a stereocomplex was obtained. In addition, this undrawn yarn has a low temperature melt caused by poly L-lactic acid and poly D-lactic acid. It was found that no solution peak was observed. Furthermore, the inventors found that partial melting of polylactic acid was not observed even when the drawn yarn was heat-treated at a high temperature, and the present invention was completed.
- the present invention relates to (i) poly L-lactic acid (component A) having a weight average molecular weight of 50,000 to 300,000, (ii) poly D-lactic acid (component B) having a weight average molecular weight of 50,000 to 300,000 and (iii) It consists of a composition containing 0.01-5 parts by weight of phosphate ester metal salt (component C) per 100 parts by weight of the total of component A and component B.
- the fiber has a strength of 2.5-10 cN / dTex. is there.
- the present invention also includes (1) (i) poly-L-lactic acid (A component) having a weight average molecular weight of 50,000 to 300,000, and (ii) poly D-lactic acid having a weight average molecular weight of 50,000 to 300,000 (component B). And (iii) a step of melt spinning a composition containing 0.01 to 5 parts by weight of a phosphoric ester metal salt (component C) per 100 parts by weight of the total of component A and component B to obtain an undrawn yarn,
- FIG. 1 shows an example of the diffraction intensity profile in the equator direction for obtaining the stereo ratio (Sc ratio) in the embodiment.
- the fiber of the present invention is obtained by melt spinning a composition containing poly L-lactic acid (component A), poly D-lactic acid (component B) and a phosphate ester metal salt (component C) to obtain an undrawn yarn.
- component A poly L-lactic acid
- component B poly D-lactic acid
- component C a phosphate ester metal salt
- Poly L monolactic acid mainly consists of L monolactic acid units.
- L-lactic acid unit is a repeating unit derived from L-lactic acid.
- the poly L-lactic acid preferably contains 90 to 100 mol%, more preferably 95 to 100 mol%, and even more preferably 98 to 100 mol% of L-lactic acid units.
- Other repeating units include D-lactic acid units and units other than lactic acid.
- the D-lactic acid unit and the units other than lactic acid are preferably 0 to 10 mol%, more preferably 0 to 5 mol%, and still more preferably 0 to 2 mol%.
- Units other than lactic acid include hydroxycarboxylic acids such as glycolic acid, force prolactone, ptyrolactone, propiolactone, ethylene glycol, 1,3-propanediol, 1,2-propanediol, 1,4-propanediol 1,5-propanediol, hexanediol, octanediol, decandiol, dodecanediol, aliphatic diols having 2 to 30 carbon atoms, succinic acid, maleic acid, adipic acid, 2 to 3 carbon atoms Examples include units derived from one or more monomers selected from 0 aliphatic dicarboxylic acid, terephthalic acid, isophthalic acid, hydroxybenzoic acid, hydroquinone and other aromatic diols, and aromatic dicarboxylic acid.
- hydroxycarboxylic acids such as glycolic acid, force prolactone, ptyrolact
- the poly L monolactic acid preferably has crystallinity.
- the melting point is preferably from 1550 to 190 ° C, more preferably from 1600 to 190 ° C. If these conditions are satisfied, a stereocomplex crystal having a high melting point can be formed and the crystallinity can be increased.
- the poly L-lactic acid has a weight average molecular weight of preferably 50,000 to 300,000, more preferably 10,000 to 250,000.
- Poly D-lactic acid mainly consists of D-lactic acid units.
- the D-lactic acid unit is a repeating unit derived from D-lactic acid.
- the poly-D-lactic acid preferably contains 90 to 100 mol%, more preferably 95 to 100 mol%, and still more preferably 98 to 100 mol% of D-lactic acid units.
- Other repeating units include L-lactic acid units and units other than lactic acid.
- the L-lactic acid unit and the units other than lactic acid are preferably 0 to 10 mol%, more preferably 0 to 5 mol%, and still more preferably 0 to 2 mol%.
- Units other than lactic acid include glycolic acid, force prolactone, ptyrolactone, Hydroxycarboxylic acids such as propiolactone, ethylene glycol, 1,3-propanediol, 1,2-propanediol, 1,4-propanediol, 1,5-propanediol, hexanediol, octanediol, decandi Talent, dodecandiol, aliphatic diols having 2 to 30 carbon atoms, succinic acid, maleic acid, adipic acid, aliphatic dicarboxylic acids having 2 to 30 carbon atoms, terephthalic acid, isofuric acid And units derived from one or more monomers selected from aromatic diols such as hydroxybenzoic acid and hydroquinone, and aromatic dicarponic acid.
- Hydroxycarboxylic acids such as propiolactone, ethylene glycol, 1,3-propanediol
- Poly D-lactic acid preferably has crystallinity.
- the melting point is preferably from 1550 to 190 ° C, more preferably from 1600 to 190 ° C. If these conditions are satisfied, a stereocomplex crystal having a high melting point can be formed and the crystallinity can be increased.
- the poly D-lactic acid has a weight average molecular weight of preferably 50,000 to 300,000, more preferably 10,000 to 250,000.
- Poly L-monolactic acid or poly-D-lactic acid can be produced by direct dehydration condensation of L-monolactic acid or D-lactic acid, or L-monolactic acid or D-lactic acid can be dehydrated and cyclized to form lactide, followed by ring-opening polymerization. It can be manufactured by a method. Catalysts used in these methods include divalent tin compounds such as tin octylate, tin chloride, and tin alkoxides, tetravalent tin compounds such as tin oxide, ptyl tin oxide, ethyl tin oxide, metal tin, zinc compounds, aluminum Examples include compounds, calcium compounds, lanthanide compounds, and the like.
- Poly-monolactic acid and poly-D-lactic acid are preferred because the polymerization catalyst used during the polymerization is removed by washing with a solvent or the catalytic activity is deactivated.
- a catalyst deactivator can be used to inactivate the catalyst activity.
- an organic ligand consisting of a group of chelate ligands having an imino group and capable of coordinating to a metal polymerization catalyst, phosphoric acid, phosphoric acid ester, and organic phosphoric acid compound group represented by the formula (3)
- At least one species selected from The catalyst deactivator is preferably 0.3 to 20 equivalents, more preferably 0.4 to 15 equivalents, even more preferably 1 equivalent of a metal element in the catalyst at the end of the polymerization.
- ⁇ - ⁇ ( 0) m (OH) n (OX 2 ) 2 _ n (3)
- m 0 or 1
- n 1 or 2
- X and X 2 are each independently from 1 to 2 carbon atoms
- the hydrocarbon group include alkyl groups having 1 to 20 carbon atoms such as a methyl group, an ethyl group, a propyl group, and a butyl group.
- Poly L monolactic acid and poly D-lactic acid preferably have a metal ion content of 20 ppm or less from the viewpoint of heat resistance and hydrolysis resistance of the fiber. It is preferable that the content of each metal selected from metal, rare earth, transition metals of the third period, aluminum, germanium, tin and antimony is 20 ppm or less.
- the phosphoric acid ester metal salt (component C) is preferably a compound represented by the following formula (1) or (2).
- One kind of phosphoric acid ester metal salt may be used, or a plurality of kinds may be used in combination.
- R 2 and R 3 each independently represent a hydrogen atom or an alkyl group having 1 to 12 carbon atoms.
- alkyl group having 1 to 12 carbon atoms examples include methyl group, ethyl group, n-propyl group, iso-propyl group, n-butyl group, sec-butyl group, iso-butyl group, tert-butyl group, amyl group, tert-amyl group, hexyl group, heptyl group, octyl group, iso-aged octyl group, tert-octyl group, 2-ethylhexyl group, nonyl group, iso-nonyl group, decyl group, iso-decyl group, tert- Examples include decyl, undecyl, dodecyl, and tert-dodecyl groups.
- p represents 1 or 2.
- Preferred examples of the phosphoric acid ester metal salt represented by the formula (1) include those in which is a hydrogen atom and R 2 and R 3 are both tert-butyl groups.
- R 4 , R 5 and R 6 each independently represent a hydrogen atom or an alkyl group having 1 to 12 carbon atoms.
- alkyl group having 1 to 12 carbon atoms include methyl group, ethyl group, n-propyl group, iso-propyl group, n-butyl group, sec-butyl group, iso-butyl group, tert-butyl group, amyl group, tert-amyl group, hexyl group, heptyl group, octyl group, iso-talyl group, tert-octyl group, 2-ethylhexyl group, nonyl group, iso-nonyl group, decyl group, iso-decyl group Tert-decyl group, undecyl group, dodecyl group, tert-dodecyl group and the like.
- M 2 is an alkali metal atom such as Na, K, Li or Al force such as Mg, Ca Represents alkaline earth metal atoms.
- p represents 1 or 2.
- Preferred examples of the phosphoric acid ester metal salt represented by the formula (2) include those in which R 4 and R 6 are methyl groups and R 5 is a tert-butyl group.
- an ester metal salt of phosphoric acid a trade name, NA-11, manufactured by ADEKA Co., Ltd. can be mentioned.
- the phosphoric acid ester metal salt can be synthesized by a known method.
- the compound represented by the formula (1) or (2) is a compound known as a crystal nucleating agent for polylactic acid.
- Mi and M 2 in the formulas (1) and (2) are an alkali metal atom or an alkaline earth metal atom.
- Mi and M 2 in formula (1) and formula (2) are other metals such as aluminum, the compound itself has low heat resistance, and sublimates are generated during spinning, making spinning difficult. There is.
- the phosphoric acid ester metal salt (component C) preferably has an average primary particle size of 0.01 to 10 m, more preferably 0.05 to 7 / m. It is industrially difficult to make the particle size smaller than 0. O l m, and it is not necessary to make it so small. On the other hand, if it is larger than l O m, the frequency of yarn breakage increases during spinning and drawing.
- the content of the phosphoric acid ester metal salt (component C) is 0.01 to 5 parts by weight per 100 parts by weight of the total of poly L monolactic acid (component A) and poly D —lactic acid (component B), preferably 0. 05 to 5 parts by weight, more preferably 0.05 to 4 parts by weight, and particularly preferably 0.1 to 3 parts by weight.
- component C The content of the phosphoric acid ester metal salt
- component C is 0.01 to 5 parts by weight per 100 parts by weight of the total of poly L monolactic acid (component A) and poly D —lactic acid (component B), preferably 0. 05 to 5 parts by weight, more preferably 0.05 to 4 parts by weight, and particularly preferably 0.1 to 3 parts by weight.
- the amount is less than 0.01 parts by weight, the desired effect is hardly recognized.
- the amount is more than 5 parts by weight, thermal decomposition or fiber breakage may occur during fiber formation.
- the ratio of poly L monolactic acid (component A) to poly D-lactic acid (component B) is A component / B component (weight), preferably 40Z60-60 40, more preferably 45 / 55-55 / 45, More preferably, it is 50/50.
- component A, component B and component C can be mixed with a tumbler, V-type blender, super mixer, nowa mixer, Banbury mixer, kneading roll, single-screw or twin-screw extruder, etc. .
- the composition thus obtained can be melt-mixed and transferred to the spinning device as it is or via a metering pump.
- the temperature for melting and mixing is preferably higher than the melting point of the resulting stereocomplex polylactic acid, and preferably higher than 220 ° C. It can also be supplied to a spinning device after it has been pelletized.
- the pellet length is preferably 1 to 7 mm, the major axis 3 to 5 mm, and the minor axis 1 to 4 mm.
- the pellet shape is preferably uniform.
- the pelletized composition can also be transferred to a spinning device using a conventional melt extruder such as a pressure melt type or a single or twin screw extruder type. In forming a stereocomplex crystal, it is important to sufficiently mix the A component and the B component, and it is particularly preferable to mix them under a shear stress.
- the composition may contain a carpositimide compound. The thermal decomposability and hydrolysis resistance obtained by containing a carpositimide compound are improved.
- carpositimide compounds dicyclohexyl carpositimide, diisopropyl carposimide, diisoptyl carposimide, dioctyl carposimide, octyl decyl carposimide, di-tert-butyl carpositimide, dibenzyl carposimide, diphenyl carposimide , N—octadecyl N′—phenyl carpositimide, N—benzyl—N′—phenyl carposimide, N—benzyl ⁇ / — N′—tolyl carposimide, zeo-tolylcarposimide, ji P—toly Lucalpositimide, Bis (p-aminophenyl) Carposiimide, Bis (p-cyclophenyl) Carposiimide, Bis (o-cyclophenyl) Forced Lupodiimide, Bis (o-ethylphenyl) Calposimide, Bis (p_eth
- polycarposiimide compound examples include calpolite L A-1 and HMV-8 CA, which are sold under the trade name of Carposi Lai, commercially available from Nisshinbo Co., Ltd.
- the composition preferably has a decrease in weight average molecular weight of not more than 20% when melted at 260 ° C. When the molecular weight is drastically reduced at high temperatures, spinning is not only difficult, but also the physical properties of the obtained yarn are lowered, which is not preferable.
- the composition preferably has a moisture content of 100 ppm or less.
- High moisture content promotes hydrolysis of the poly-L-lactic acid component and poly-D-lactic acid component, significantly lowers the molecular weight, making spinning difficult, and lowering the physical properties of the resulting yarn. I don't like it.
- the amount of residual lactide in the composition is preferably 3,000 ppm or less, more preferably 1, O O O ppm or less, and particularly preferably 400 ppm or less. Since lactide in polylactic acid obtained by the lactide method may vaporize during melt spinning and cause yarn unevenness, it is preferable for the purpose of obtaining a good yarn to suppress the lactide amount to 400 ppm or less.
- the composition is melted in an Extruder type or pressure melter type melt extruder. After being melted, it is weighed by a gear pump, filtered in a pack, and then discharged from a nozzle provided on the base as monofilament, multifilament, etc. and spun.
- the shape of the base and the number of bases are not particularly limited, and any of round, irregular, solid, hollow, etc. can be adopted.
- the discharged yarn is immediately cooled and solidified, then converged, oiled, and wound.
- the winding speed is not particularly limited, but is preferably in the range of 300 to 5 m, 0 m / min. From the viewpoint of drawability, a winding speed at which the stereo ratio of the undrawn yarn is 0% is preferable.
- the wound undrawn yarn is then used in the drawing process, but it is not always necessary to separate the spinning process and the drawing process.
- a stretching method may be adopted.
- the fiber of the present invention is obtained by a melt spinning method. From the industrial point of view, solution spinning, such as dry or wet, has high productivity, and the stability of the solution containing poly-L-lactic acid and poly-D-lactic acid is low, so a stable yarn can be obtained. It is hard to be done.
- a low-temperature crystal melt phase (a) of less than 195 is usually used, depending on the components, composition ratio, and stereocomplex formation conditions. It is known that at least two endothermic peaks of the above high-temperature crystal melting phase (b) are exhibited.
- the molten composition used for spinning is substantially amorphous as measured by a wide-angle X-ray diffraction method.
- DSC differential scanning calorimeter
- at least two endothermic peaks of the low-temperature crystal melting phase (a) and the high-temperature crystal melting phase (b) are not shown. It is characterized by showing a single melting peak of the crystal.
- the melting peak temperature is 1 95 or more.
- the spun undrawn yarn is also substantially amorphous as measured by the wide-angle X-ray diffraction method, and exhibits a single melting peak of a stereocomplex crystal in DSC measurement. .
- the undrawn yarn has a substantially single melting peak in differential scanning calorimetry (DSC) measurement, and the melting peak temperature is 1 95 or higher.
- the undrawn yarn is made of amorphous streak. It is presumed that it does not contain poly L-monolactic acid phase and / or poly D-lactic acid phase that can form low-temperature crystalline phase. These characteristics are due to the inclusion of fiber strength s phosphate metal salt (component C), which is a useful property that has never been expected.
- component C fiber strength s phosphate metal salt
- the drawing may be one-stage or multistage drawing of two or more stages.
- the draw ratio is preferably 3 times or more, more preferably 4 to 10 times. However, if the draw ratio is too high, the fiber is devitrified and whitened, resulting in a decrease in fiber strength.
- the preheating for stretching can be performed by heating the roll, using a flat or pin-type contact heating plate, a non-contact type hot plate, or a heating medium bath.
- the stretching temperature is preferably 70 to: L 40 ° C, more preferably 80 to 130 ° C.
- the melting start temperature of the high-temperature crystal melting phase (b) of the drawn yarn is preferably 190 ° C. or higher, more preferably 20 ° C. or higher.
- the stereoification rate (S c rate) obtained from the integrated intensity of the stereocomplex crystal diffraction peak by wide-angle X-ray diffraction measurement of the drawn yarn is at a high level of 90% or more.
- the heat treatment step is a step of heat treating the drawn yarn.
- the heat treatment is performed at 150 to 220, preferably 170 to 220 ° C, more preferably 180 to 200 ° C.
- the heat treatment is preferably performed under tension.
- the heat treatment can be carried out with a hot-mouthed heater, a contact-type heating plate, a non-contact-type hot plate or the like. Heat treatment is continuous with drawing process — _
- the drawn yarn since the drawn yarn does not have a low-temperature crystal melting phase of poly L-lactic acid or poly D-lactic acid, it can be heat-treated at a temperature equal to or higher than the crystal melting point of poly L-lactic acid or poly D-lactic acid. It does not show thermal fusion or fracture of partial melting of single crystals of poly L-lactic acid or poly D-lactic acid, and can be heat-treated at 170 ° C or higher, for example, 190 ° C higher than the melting point of single crystals. As a result, it is possible to obtain a fiber that exhibits a high stereo ratio and is excellent in strength and heat resistance. Since this fiber is excellent in heat resistance, there are few troubles such as heat fusion during production, and it is excellent in heat shrinkage.
- the fiber of the present invention comprises a composition containing an A component, a B component, and a C component, and has a strength of 2.5 to 10 cN / dTe X.
- the A component, B component and C component are as described above.
- the strength of the fiber of the present invention is preferably 2.5 cNZdTex or more, more preferably 3.8 cNZdTex or more, and further preferably 4. OcNZdTex or more.
- fibers having a strength of 4.0 cNZdTex or more are preferred because of their wide practical use range.
- the fiber of the present invention has a heat shrinkage rate at 150 ° C. of preferably 0.1 to 15%, more preferably 0.1 to 7%, still more preferably 0.2 to 6.5%, and even more preferably. 0.3 to 6%, particularly preferably 0.5 to 6%. If the heat shrinkage rate is large, the textile product will shrink and become smaller when it is exposed to high temperatures, such as ironing.
- the stereoification rate of the fiber of the present invention is preferably 90 to 100%, more preferably 95 to 100%, and still more preferably 98 to L00%.
- the fiber of the present invention has a substantially single melting peak in differential scanning calorimetry (DSC) measurement, and has a melting peak temperature of 195 ° C. or higher.
- a wide-angle X-ray diffraction method (XRD) Stereo ratio measured is 90% or more.
- the fiber of the present invention has ironing resistance at 1 ° C. to 0 ° C.
- the fiber of the present invention can be used as a raw yarn for yarn processing such as false twisting, mechanical crimping, and indentation crimping. Further, spun yarns using long fibers, short fibers, and short fibers can also be used. Since the fiber of the present invention has a high stereo ratio and is excellent in strength, heat resistance and shrinkage resistance, it can be made into various fiber products such as woven fabrics, knitted fabrics and non-woven fabrics. That is, this invention includes the textiles containing the fiber of this invention.
- apparel such as shirts, blousons, pants and coats
- apparel materials such as cups and pads
- interior uses such as Ryuichiten, carpets, mats and furniture, belts, nets, ropes, heavy cloths, bags It can also be suitably used for industrial materials such as felts and filters, and vehicle interiors.
- the fiber of the present invention does not have a single crystal phase of poly L-lactic acid or poly D-lactic acid. Therefore, even when ironing a fiber product made of the fiber of the present invention, there is no fear that a part of the fiber is softened and melted or shrunk. Since the textile product of the present invention does not impair the fabric quality, texture and dimensions by ironing, it can be expected to be used in industrial applications that are expected to be used at high temperatures.
- Weight average molecular weight (Mw) The weight average molecular weight of the polymer was determined by GPC (column temperature 40 ° C, black mouth form) in comparison with polystyrene standard samples.
- X-ray source Cu— ⁇ ray (Confocal mirror)
- a 10 cm square cloth was made from the fibers to be tested, ironed for 30 seconds with a pyrone adjusted to a surface temperature of 17 (TC), and the heat resistance was determined from changes in the cloth width, dimensions, and texture. It was done on the basis of.
- TC surface temperature
- FAIL X Single yarn is fused or thermal deformation of the cloth before treatment, changes to a stiff texture.
- Adekastab NA-11 2,2-methylenebisphosphate (4,6-di-tert-butylphenol) sodium salt
- This undrawn yarn had a Sc conversion rate of 0% and had a single crystal melting peak derived from the stereocomplex at 224 ° C with a differential scanning calorimeter (DSC).
- This undrawn yarn was drawn 3.5 times with a preheating of 70 and subsequently heat treated at 180 ° C to obtain 579 dtex / 201 fi 1 fibers.
- the obtained fiber showed a single melting peak of a stereocomplex crystal composed of poly L-lactic acid and poly D-lactic acid in the differential scanning calorimetry (DSC) measurement, and the melting point was 224 ° C.
- the Sc conversion rate in wide-angle X-ray diffraction measurement was 100%
- the fiber strength was 3.3 cN / dTe x
- the elongation was 35%
- 150 and the heat shrinkage rate was 5%.
- Example 2 The same operation as in Example 1 was carried out except that the amount of phosphate metal salt and the heat treatment temperature were changed. At this time, the spinnability and stretchability were good, and there were hardly any problems such as yarn breakage, fluff and fusion. The results are shown in Tables 1 and 2. The obtained fibers showed a single s $ solution peak of the stereocomplex crystal in the DSc measurement, and the melting peak temperatures were all 210 ° C or higher. Comparative Examples 1 and 2
- Example 5 The same operation as in Example 1 was performed except that the phosphoric acid ester metal salt was not used and the heat treatment temperatures were set to 1550 ° C and 180 ° C. The results are shown in Tables 1 and 2.
- Example 5 The same operation as in Example 1 was performed except that the phosphoric acid ester metal salt was not used and the heat treatment temperatures were set to 1550 ° C and 180 ° C. The results are shown in Tables 1 and 2.
- Example 1 when only the average particle diameter of the phosphoric acid ester metal salt was changed to 15 m, the number of fuzz increased slightly during spinning and drawing, but this was not an industrial problem, and there were no other problems. A good drawn yarn could be obtained. The physical properties of the drawn yarn were not different from Example 1. Comparative Example 3
- Example 1 except that 0.5 parts by weight of aluminum 2,2-methylenebis (4,6-di-tert-butylphenylphosphate) hydroxide (ADK STAB NA-2 1) is used as the phosphate metal salt
- ADK STAB NA-2 1 aluminum 2,2-methylenebis (4,6-di-tert-butylphenylphosphate) hydroxide
- the fiber of the present invention is substantially composed only of a stellar complex phase, is excellent in strength and heat resistance, and has a low heat shrinkage rate.
- a composition in which poly L monolactic acid (component A) and poly D-lactic acid (component B) are mixed with a phosphate metal salt (component C) is melt-spun.
- This melted composition is substantially amorphous in the wide-angle X-ray diffraction measurement, and shows a single Si solution peak of the stereocomplex crystal in the DSC measurement. Stable spinning and drawing are possible.
- the obtained undrawn yarn and drawn yarn are also substantially amorphous as measured by the wide-angle X-ray diffraction method, and show substantially a single melting peak of a stereocomplex crystal as measured by DSC measurement.
- DSC measurement As a result, even when heat treatment is performed at a temperature higher than the crystalline melting point of poly L monolactic acid and poly D-lactic acid, poly L monolactic acid and poly D-lactic acid do not partially melt, and have a high stereoization ratio.
- a fiber having excellent heat resistance can be obtained.
- the fiber of the present invention has a high stereo ratio and is excellent in strength, heat resistance and shrinkage resistance, it can be made into various fiber products such as woven fabrics, knitted fabrics and non-woven fabrics.
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- Engineering & Computer Science (AREA)
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- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
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- Manufacturing & Machinery (AREA)
- Artificial Filaments (AREA)
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Description
Claims
Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA2662400A CA2662400C (en) | 2006-09-04 | 2007-09-03 | Polylactic acid fiber and manufacturing method thereof |
EP07806980A EP2060665A4 (en) | 2006-09-04 | 2007-09-03 | POLYLACTIC ACID FIBER AND METHOD OF MANUFACTURE |
BRPI0716443-2A2A BRPI0716443A2 (pt) | 2006-09-04 | 2007-09-03 | fibra, mÉtodo para fabricar uma fibra, e, produto de fibra |
KR1020097004464A KR101397202B1 (ko) | 2006-09-04 | 2007-09-03 | 폴리락트산 섬유 및 그 제조 방법 |
JP2008533218A JP5023065B2 (ja) | 2006-09-04 | 2007-09-03 | ポリ乳酸繊維およびその製造方法 |
US12/439,773 US8299148B2 (en) | 2006-09-04 | 2007-09-03 | Polylactic acid fiber and manufacturing method thereof |
CN2007800328137A CN101528994B (zh) | 2006-09-04 | 2007-09-03 | 聚乳酸纤维及其制造方法 |
AU2007292008A AU2007292008A1 (en) | 2006-09-04 | 2007-09-03 | Polylactic acid fiber and method for producing the same |
MX2009002380A MX2009002380A (es) | 2006-09-04 | 2007-09-03 | Fibra de acido polilactico y metodo para producirla. |
Applications Claiming Priority (2)
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JP2006238928 | 2006-09-04 | ||
JP2006-238928 | 2006-09-04 |
Publications (1)
Publication Number | Publication Date |
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WO2008029934A1 true WO2008029934A1 (fr) | 2008-03-13 |
Family
ID=39157353
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2007/067548 WO2008029934A1 (fr) | 2006-09-04 | 2007-09-03 | Fibre d'acide polylactique et procédé de fabrication |
Country Status (11)
Country | Link |
---|---|
US (1) | US8299148B2 (ja) |
EP (1) | EP2060665A4 (ja) |
JP (1) | JP5023065B2 (ja) |
KR (1) | KR101397202B1 (ja) |
CN (1) | CN101528994B (ja) |
AU (1) | AU2007292008A1 (ja) |
BR (1) | BRPI0716443A2 (ja) |
CA (1) | CA2662400C (ja) |
MX (1) | MX2009002380A (ja) |
TW (1) | TWI444512B (ja) |
WO (1) | WO2008029934A1 (ja) |
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JP2011256471A (ja) * | 2010-06-08 | 2011-12-22 | Teijin Ltd | ポリ乳酸繊維構造体およびそれよりなる衣料 |
JP2012007257A (ja) * | 2010-06-23 | 2012-01-12 | Teijin Ltd | 繊維製品 |
JP2012149359A (ja) * | 2011-01-19 | 2012-08-09 | Teijin Ltd | 低乾熱収縮率のステレオコンプレックスポリ乳酸繊維の製造方法 |
CN102517732A (zh) * | 2011-12-21 | 2012-06-27 | 德州学院 | 一种双粗纱工艺舒适性保温赛络纱纺纱方法 |
WO2015129920A1 (ja) * | 2014-02-27 | 2015-09-03 | 帝人株式会社 | 繊維 |
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TWI444512B (zh) | 2014-07-11 |
MX2009002380A (es) | 2009-03-20 |
CN101528994B (zh) | 2013-12-18 |
CN101528994A (zh) | 2009-09-09 |
EP2060665A4 (en) | 2009-11-11 |
US8299148B2 (en) | 2012-10-30 |
CA2662400C (en) | 2014-03-11 |
CA2662400A1 (en) | 2008-03-13 |
BRPI0716443A2 (pt) | 2013-09-17 |
TW200831725A (en) | 2008-08-01 |
JPWO2008029934A1 (ja) | 2010-01-21 |
KR101397202B1 (ko) | 2014-05-20 |
JP5023065B2 (ja) | 2012-09-12 |
US20100004362A1 (en) | 2010-01-07 |
EP2060665A1 (en) | 2009-05-20 |
KR20090048612A (ko) | 2009-05-14 |
AU2007292008A1 (en) | 2008-03-13 |
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