EP2589689B1 - Spinnlösung zum spinnen einer lyozelle, verfahren zur herstellung einer lyozellenfilamentfaser und verfahren zur herstellung einer lyozellenstapelfaser damit - Google Patents

Spinnlösung zum spinnen einer lyozelle, verfahren zur herstellung einer lyozellenfilamentfaser und verfahren zur herstellung einer lyozellenstapelfaser damit Download PDF

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Publication number
EP2589689B1
EP2589689B1 EP11801135.2A EP11801135A EP2589689B1 EP 2589689 B1 EP2589689 B1 EP 2589689B1 EP 11801135 A EP11801135 A EP 11801135A EP 2589689 B1 EP2589689 B1 EP 2589689B1
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EP
European Patent Office
Prior art keywords
lyocell
filament
fiber
dope
spinning
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EP11801135.2A
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English (en)
French (fr)
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EP2589689A4 (de
EP2589689A2 (de
Inventor
Woo-Chul Kim
Sang-Mok Lee
Jong-Cheol Jeong
Sang-Woo Jin
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Kolon Industries Inc
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Kolon Industries Inc
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Priority claimed from KR1020100062577A external-priority patent/KR101430714B1/ko
Priority claimed from KR1020100094505A external-priority patent/KR101385275B1/ko
Application filed by Kolon Industries Inc filed Critical Kolon Industries Inc
Publication of EP2589689A2 publication Critical patent/EP2589689A2/de
Publication of EP2589689A4 publication Critical patent/EP2589689A4/de
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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
    • D01F2/00—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
    • 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
    • D01D5/26—Formation of staple fibres
    • 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
    • D01D5/22—Formation of filaments, threads, or the like with a crimped or curled structure; with a special structure to simulate wool
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01G—PRELIMINARY TREATMENT OF FIBRES, e.g. FOR SPINNING
    • D01G1/00—Severing continuous filaments or long fibres, e.g. stapling
    • D01G1/02—Severing continuous filaments or long fibres, e.g. stapling to form staple fibres not delivered in strand form
    • D01G1/04—Severing continuous filaments or long fibres, e.g. stapling to form staple fibres not delivered in strand form by cutting
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01H—SPINNING OR TWISTING
    • D01H1/00—Spinning or twisting machines in which the product is wound-up continuously
    • D01H1/14—Details
    • D—TEXTILES; PAPER
    • D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
    • D04H1/04—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres having existing or potential cohesive properties, e.g. natural fibres, prestretched or fibrillated artificial fibres
    • D04H1/06—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres from fleeces or layers composed of fibres having existing or potential cohesive properties, e.g. natural fibres, prestretched or fibrillated artificial fibres by treatment to produce shrinking, swelling, crimping or curling of fibres
    • D04H1/067—Regenerated cellulose series
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
    • Y10T428/2904—Staple length fiber
    • Y10T428/2909—Nonlinear [e.g., crimped, coiled, etc.]

Definitions

  • the present invention relates to a dope for spinning lyocell, a method for manufacturing lyocell filament fiber using the dope, and a method for manufacturing lyocell staple fiber using the dope. More particularly, the present invention relates to dope for spinning lyocell, a method for manufacturing lyocell filament fiber using the dope, and a method for manufacturing lyocell staple fiber using the dope, which may provide lyocell fiber that exhibits a low orientation degree and fibrillation degree, and high elongation, and thus may be applied for fiber for high grade clothing without conducting additional processes.
  • Fiber refers to a natural or artificial linear object that has flexibility and a thin shape, and has large ratio of length to thickness.
  • the fiber may be divided into long fiber, semi-long fiber, and short fiber in terms of the shape, and natural fiber and artificial fiber in terms of the raw material.
  • Fiber has been closely related to human life, and natural fiber such as cotton, linen, wool, and silk has been used as a main ingredient for clothes.
  • natural fiber such as cotton, linen, wool, and silk
  • the application of fiber has been enlarged to industrial use as well as a material for clothes, and to satisfy the rapidly increasing demand of fiber, artificial fiber has been developed as a new fiber material.
  • regenerated fiber has excellent feel and wearability, and has much faster moisture absorption and discharge performance than cotton, and thus it has been used a lot as a material for clothes.
  • rayon fiber has excellent gloss and color formation property, may exhibit equivalent feel to natural fiber, and is recognized as a harmless material to a human body, and thus has been widely used in the past.
  • the rayon fiber is easily shrunken and wrinkled, the manufacturing process is complicated, and a lot of chemicals are used in the process of dissolving wood pulp, and the like, thus causing environmental problems in operation or environmental pollution in the process of waste water treatment and the like.
  • lyocell fiber manufactured from natural pulp and amine oxide hydrate has been introduced.
  • the lyocell fiber has superior fiber properties such as tensile property and feel, and the like, compared to the existing regenerated fiber, does not generate pollutants in the manufacturing process, and the used amine oxide based solvent is recyclable and biodegraded when discarded, and thus it is used as an environmentally friendly fiber in various fields.
  • lyocell fiber has disadvantages in that excessive fibrils are formed on the surface due to high orientation degree and weak binding force between fibrils, and thereby, the fiber surface feel and final product quality are degraded.
  • an additional process such as acid cellulose treatment is required, thus rendering the manufacturing process complicated, increasing manufacturing cost, decreasing fabric weight in the process of fibril removal, or degrading fiber properties.
  • WO 2009/118262 A1 refers to solvent-spun cellulosic mouldings from a solution predominantly containing cellulose in a solvent.
  • KR20090025977 is directed to cellulose filament fibers including a cross-linking unit between cellulose molecules, wherein the cross-linking unit includes an aromatic group selected from a group consisting of aryl, alkylaryl or arylalkyl, heteroaryl and heteroarylalkyl and one selected from the group consisting of hydrogen, halogen, thiol, hydroxy, allyl, alkyl.
  • EP 1 433 881 A2 is directed to a lyocell multi-filament for a tire cord and a method of producing the same.
  • US 2008/0173419 A1 describes a method of making regenerated cellulose microfibers including forming segmented fibers with multiple longitudinally extending segments of slightly different composition.
  • the present invention provides a dope for spinning lyocell that may provide lyocell fiber that exhibits a low orientation degree and fibrillation degree, and high elongation, and thus may be applied for fiber for high grade clothing without conducting additional processes.
  • the present invention also provides a method for manufacturing lyocell filament fiber using the dope for spinning lyocell.
  • the present invention also provides lyocell filament fiber manufactured from the dope for spinning lyocell.
  • the present invention also provides a method for manufacturing lyocell staple fiber that exhibits a low orientation degree and fibrillation degree, and high elongation, and thus may be applied for fiber for high grade clothing without conducting additional processes.
  • the present invention provides dope for spinning lyocell including cotton linter pulp that comprises 99 wt% or more of alpha-cellulose, water, and N-methylmorpholine-N-oxide (NMMO).
  • NMMO N-methylmorpholine-N-oxide
  • the present invention also provides a method for manufacturing lyocell filament fiber including: discharging the spinning dope from a spinner; passing the discharged dope through a coagulation bath to coagulate it into filament; washing the filament that has passed through the coagulation bath; and drying the washed filament.
  • the present invention also provides lyocell filament fiber manufactured from the spinning dope.
  • the present invention also provides a method for manufacturing lyocell staple fiber, including: discharging spinning dope including cotton linter pulp that comprises 99 wt% or more of alpha-cellulose, and an aqueous solution of N-methylmorpholine-N-oxide (NMMO) from a spinner; passing the discharged dope through a coagulation bath to coagulate it into filament; washing the filament that has passed through the coagulation bath; drying the washed filament; crimping the dried filament; and cutting the crimped filament.
  • NMMO N-methylmorpholine-N-oxide
  • dope for spinning lyocell a method for manufacturing lyocell filament fiber, lyocell filament fiber, and a method for manufacturing lyocell staple fiber according to specific embodiments of the invention will be explained in detail.
  • dope for spinning lyocell including cotton linter pulp, water, and N-methylmorpholine-N-oxide (NMMO).
  • NMMO N-methylmorpholine-N-oxide
  • lyocell fiber having a low orientation degree and fibrillation degree may be provided, and completed the invention. If the dope for spinning lyocell is used, the amount of fibrils formed on the surface of lyocell fiber or fibrillation degree becomes very low, and thus surface feel of the fiber and quality of the final product may be improved, and an additional post process may be dispensed with thus simplifying the manufacturing process and reducing manufacturing cost. Further, since lyocell fiber obtained using the dope for spinning lyocell may have a low initial modulus, it may be applied for fiber for high grade clothing such as lining of a suit, underwear, and the like.
  • lint a side having a long fiber length, primarily separated from cotton seed
  • linter a side having a short fiber length, secondarily separated
  • the linter commonly has a fiber length of 3 to 5 mm, and it may be obtained from annual cotton, and thus is favorable for supply and demand of raw material.
  • the cotton linter pulp includes a high content of alpha-cellulose, namely 99 wt% or more of alpha-cellulose, it may exhibit a low fibrillation degree, and since it contains a trace amount of impurities, it may be used for fabric for high grade clothing.
  • the dope for spinning lyocell may include 6 to 16 wt% of cotton linter pulp. If the content of the cotton linter pulp is less than 6 wt%, fiber properties may not be achieved, and if it is greater than 16 wt%, it may be difficult to dissolve in an aqueous solution.
  • the dope for spinning lyocell may include 84 to 94 wt% of an aqueous solution of N-methylmorpholine-N-oxide as a solvent ingredient. If the content of the N-methylmorpholine-N-oxide aqueous solution is less than 84 wt%, solution viscosity may become too high, and if it is greater than 94 wt%, spinning viscosity may become too low, and thus it may be difficult to manufacture uniform fiber in the spinning step.
  • the N-methylmorpholine-N-oxide aqueous solution may include N-methylmorpholine-N-oxide and water in a weight ratio of 91:9 to 83:17. If the weight ratio of the N-methylmorpholine-N-oxide and water is greater than 91:9, cellulose may be decomposed when dissolving cellulose, and if the weight ratio is less than 83:17, dissolving performance of the solvent may be lowered and thus it may be difficult to dissolve cellulose.
  • the dope for spinning lyocell may be prepared by introducing cotton linter pulp in an aqueous solution of N-methylmorpholine-N-oxide including N-methylmorpholine-N-oxide and water in a weight ratio of 90:10 to 50:50 and swelling it, and then removing water so that the weight ratio of N-methylmorpholine-N-oxide and water may become 93:7 to 85:15, and the final content of the pulp may become 6 to 16 wt%, more preferably 10 to 14 wt%.
  • a method for manufacturing lyocell filament fiber including: discharging the spinning dope; passing the discharged dope through a coagulation bath to coagulate it into filament; washing the filament that has passed through the coagulation bath; and drying the washed filament.
  • the inventors confirmed through experiments that if dope for spinning lyocell including cotton linter pulp is applied to a specific manufacturing method, the biggest problem of lyocell fiber in that it has a high orientation degree and excessive fibrils are formed on the surface of fiber may be solved, and environment-friendly lyocell fiber with excellent quality may be provided, and completed the invention.
  • lyocell filament fiber lyocell fiber having a very small amount of fibrils formed on the surface or a low fibrillation degree may be obtained, and thus an additional process need not be conducted to remove fibril, thus simplifying the process and reducing manufacturing cost.
  • lyocell filament fiber that has excellent surface feel and final product quality, and simultaneously has a low initial modulus may be produced, and thus may be applied for a fabric for high grade clothing such as a lining of a suit, underwear, and the like.
  • the spinner functions for passing fibrous filament through an air gap to discharge as a coagulated solution.
  • the step of discharging the spinning dope from the spinner may be conducted at 80 to 130 °C.
  • a step of passing it through an air gap may be further conducted.
  • the air gap functions for supplying air to the dope discharged from the spinner and pre-quenching the liquid dope. Since elongation viscosity of the dope is higher than a common dope, the temperature of the air supplied to smoothly progress the spinning process may be 5 to 30 °C, and preferably 5 to 20 °C.
  • the air volume provided in the air gap may be 10 to 300 m 3 /hr, and preferably 30 to 100 m 3 /hr. If the air volume is too small, yarn cutting may be generated due to non-uniform drawing, and if it is too large, yarn cutting may be generated due to cooling of the spinner.
  • the dope that is discharged from the spinner and selectively passes through the air gap is coagulated in a coagulation bath and made in the form of filament, wherein the temperature of the coagulation bath is 30 °C or less.
  • the coagulation temperature of 30 °C or less is for appropriately maintaining coagulation speed.
  • the coagulation bath may be manufactured with a composition commonly used in the technological field of the invention without specific limitations.
  • the method for manufacturing lyocell filament fiber may include washing the filament that has passed through the coagulation bath, and drying the washed filament.
  • washing solution of 0 to 100 °C may be used, water may be used as the washing solution, and if necessary, other additives may be further included.
  • the step of drying the washed filament may include applying tension of 0.1 to 2 g/d, preferably 0.2 to 0.5 g/d to the filament at 80 to 200 °C, preferably 100 to 150 °C.
  • the drying step may be progressed as a single-step process, or it may be progressed as a multi-step process wherein drying conditions are varied according to each step.
  • specific drying conditions of each step may be optionally selected within the above tension and temperature range, and besides the conditions, commonly used conditions in the technological field of the invention may be used.
  • a common manufacturing apparatus of lyocell multifilament includes a gear pump (11) for supplying a spinning solution at a constant pressure, a spinner (12) for spinning the spinning solution supplied from the extruder in the form of fiber, a first coagulation bath (14) for coagulating non-coagulated fiber (13) discharged from the spinner, and optionally, a second coagulation bath (15).
  • the filament that has passed through the coagulation baths (14, 15) is introduced into a washing apparatus (17) by towing rollers (16), where a solvent and the like included in the spinning dope and the like is removed by water.
  • the filament that has passed through the washing apparatus is dried in a drying apparatus (18), and then wound to obtain final lyocell filament.
  • the spinning apparatus is only one example of an apparatus usable for manufacturing of lyocell filament fiber, and the manufacturing method and apparatus that can be applied in the present invention are not limited thereto.
  • lyocell filament fiber manufactured from the dope for spinning lyocell.
  • the lyocell fiber obtained by applying the dope for spinning lyocell to a specific manufacturing method has a very small amount of fibrils formed on the surface or a low fibrillation degree, for example, a fibrillation degree above grade 1, surface feel of the fiber or quality of the final product is excellent, and the fiber has low initial modulus, and thus it may be easily applied for fabric for high grade clothing such as lining of a suit, underwear, and the like.
  • the lyocell filament fiber may have a fibrillation degree above grade 1.
  • the 'fibrillation degree' means the degree of fibril generation on the surface of the filament, and specifically, it means a value measured from an image obtained by rubbing fiber for a certain time based on a water-immersed fiber to generate fibril, and observing the fibril with optical microscope.
  • the 'fibrillation degree' may be represented by the following General Formula 1, and as the number of generated fibrils is lower, the fiber has a higher grade of fibrillation degree.
  • Fibrillation degree grade number of fibril/unit length of filament 0.1 mm
  • the lyocell filament fiber may have an initial modulus of 150 to 230 g/d. Further, the lyocell filament fiber may have strength of 4 to 8 g/d. The initial modulus and strength may be measured after drying the lyocell filament fiber manufactured from the dope for spinning lyocell in an oven of 105 °C for 2 hours.
  • the lyocell filament fiber has appropriate strength for clothing and the like, and simultaneously exhibits a low initial modulus, and thus it may be easily applied for fabric for high grade clothing such as lining of a suit, underwear, and the like.
  • a method for manufacturing lyocell staple fiber including: discharging spinning dope including cotton linter pulp that comprises 99 wt% or more of alpha-cellulose and an aqueous solution of N-methylmorpholine-N-oxide (NMMO) from a spinner; passing the discharged dope through a coagulation bath to coagulate it into filament; washing the filament that has passed through the coagulation bath; drying the washed filament; crimping the dried filament; and cutting the crimped filament.
  • NMMO N-methylmorpholine-N-oxide
  • lyocell fiber having a low orientation degree and fibrillation degree may be manufactured without conducting an additional process.
  • the dope for spinning lyocell including cotton linter pulp is used, the amount of fibrils formed on the surface of the lyocell fiber or fibrillation degree becomes very low, thus improving surface feel of the fiber and quality of the final product, dispensing with an additional post process such as acid cellulose treatment and the like, thereby simplifying the manufacturing process and reducing manufacturing cost.
  • the lyocell fiber obtained using the dope for spinning lyocell has high strength and elongation, it may be applied for a fabric for high grade clothing such as lining of a suit, underwear, and the like.
  • lyocell staple fiber which is optimized fiber applicable for fabric for high grade clothing among lyocell fiber, may be manufactured by a relatively simplified manufacturing process.
  • lyocell staple fiber that has excellent properties due to a low orientation degree and fibrillation degree, and may be appropriately applied for fabric for high grade clothing, may be easily manufactured while simplifying the process.
  • the spinning dope used in the manufacturing method of lyocell staple fiber is as explained above.
  • lyocell staple fiber In the manufacturing method of lyocell staple fiber, the details of the steps of discharging spinning dope including cotton linter pulp and an aqueous solution of N-methylmorpholine-N-oxide (NMMO) from a spinner, passing the discharged dope through a coagulation bath to coagulate it into filament, washing the filament that has passed through the coagulation bath, and drying the washed filament are as explained in the 'manufacturing method of lyocell filament fiber'.
  • NMMO N-methylmorpholine-N-oxide
  • the filament After drying the filament, the filament is crimped.
  • the crimping step may be progressed in a common crimper applied for manufacturing of various synthetic staple fibers.
  • to manufacture lyocell staple fiber having excellent properties 8 ⁇ 20/inch, preferably 10 ⁇ 16/inch crimps, may be given to the filament.
  • lyocell staple fiber After crimping in this range, lyocell staple fiber is manufactured by a subsequent cutting process, thereby obtaining fiber that exhibits excellent properties such as excellent feel, and may be applied for fabric for high grade clothing.
  • the filament After crimping the filament, the filament is cut to manufacture lyocell staple fiber.
  • the filament may be cut to a length of 20 to 200 mm, preferably 30 to 130 mm, so that it may be preferably used for fabric for high grade clothing.
  • lyocell staple fiber having corresponding length may be manufactured.
  • the lyocell staple fiber may have an optimized form for fabric for high grade clothing and the like.
  • FIG. 2 schematically shows one example of a spinning apparatus that may be used for manufacturing lyocell staple fiber.
  • cotton linter pulp is pulverized and stored in the lyocell staple manufacturing apparatus, and the pulp is dissolved in a concentrated solvent, namely, an aqueous solution of N-methylmorpholine-N-oxide, to form a spinning solution, namely, spinning dope.
  • a concentrated solvent namely, an aqueous solution of N-methylmorpholine-N-oxide
  • the manufacturing apparatus includes a spinner for spinning the spinning solution in the form of fiber, and a coagulation bath for coagulating non-coagulated fiber discharged from the spinner.
  • the filament that has passed through the coagulation bath is introduced into a washing apparatus by towing rollers, where a solvent included in the spinning dope and the like is removed by water. Subsequently, the filament that has passed through the washing apparatus is supplied with an emulsion and dried in a drying apparatus, and then crimpled in a crimper, cut to a specific length, and finally manufactured into lyocell staple fiber.
  • the spinning apparatus of Fig. 2 is only one example used for manufacturing of lyocell staple fiber, and the manufacturing method and apparatus applicable in the present invention are not limited thereto.
  • lyocell staple fiber manufactured by the above method.
  • the staple fiber has a length of 20 to 200 mm, and thus may be appropriately applied for fabric for high grade clothing.
  • the fibrillation degree may be above grade 1.
  • the staple fiber has excellent surface feel and final product quality, high strength, and elongation, and thus it may be preferably applied for fabric for high grade clothing.
  • the 'fibrillation degree' is as defined above.
  • the lyocell staple fiber may have strength of 3 to 8 g/d and elongation at break of 9.5 to 12.0 %.
  • the strength and elongation may be obtained by pre-drying a filament specimen immediately before manufactured into staple fiber at 110 °C for 2 hours below moisture regain, and then standing for 24 hours or more under a KSK 0901 standard state so as to reach a moisture equilibrium state, and measuring with a low speed tension tester (Instron) at a tensile speed of 300 m/min.
  • Instron low speed tension tester
  • the lyocell staple fiber exhibits appropriate elongation for clothing and excellent strength, and thus may be applied for fabric for high grade clothing such as lining of a suit, underwear, and the like.
  • dope for spinning lyocell that may provide lyocell fiber that exhibits a low orientation degree and fibrillation degree, and high elongation, and thus may be applied for fiber for high grade clothing without additional processes, a method for manufacturing lyocell filament fiber using the dope, lyocell filament fiber obtained therefrom, and a method for manufacturing lyocell staple fiber using the dope are provided.
  • Example 1 Manufacture of lyocell filament fiber from cotton linter pulp
  • Cotton linter pulp with a polymerization degree (DP) of 1200 (supplied from Korea Minting and Security Printing Corporation) was introduced into a pulverizer equipped with a 100 mesh filter to prepare pulp powder having a diameter of 1700 ⁇ m or less.
  • the pulp powder was swollen in a 50 wt% NMMO aqueous solution.
  • the NMMO aqueous solution includes 6 wt% of the pulp, and an antioxidant was added in the content of 0.01 wt% to the cotton linter pulp.
  • the swollen pulp slurry was injected into a kneader maintaining an internal temperature of 90 °C and absolute pressure of 50 mmHg with a rotary valve pump at a speed of 16 kg/hour, and completely dissolved while removing extra moisture so that a 50 wt% of NMMO aqueous solution may become a 89 wt% NMMO aqueous solution, and then spinning dope was discharged through a discharge screw.
  • the spinning dope was controlled so that total fineness of the final filament may become 1650 denier, and was spun using a nozzle having 1000 nozzles and a cross-sectional area of 0.47 mm 2 . At this time, a 30 mm air gap was formed between the nozzle and coagulation bath, and in the air gap, 15 °C cooling air was supplied to the discharged dope at air volume of 30 m 3 /hr.
  • the multifilament that passed through the air gap and was coagulated in the coagulation bath was washed with water in a 5-stage washing apparatus, and then non-dried multifilament yarn controlled to a moisture content of 170 % was dried in a 3-stage drying roll to obtain lyocell multifilament yarn.
  • the tension between the 1 st stage and the 2 nd stage of the drying roll was controlled to 0.2 g/d
  • the tension between the 2 nd stage and the 3 rd stage was controlled to 0.5 g/d
  • the temperature of each roll was sequentially controlled to 100 °C, 130 °C, and 150 °C.
  • the number of filaments of the manufactured lyocell filament yarn was 1000, and the mean fineness was 1.5 d.
  • Example 2 Manufacture of lyocell filament fiber from cotton linter pulp
  • Lyocell multifilament yarn was obtained by the same method as Example 1, except using cotton linter pulp of a polymerization degree (DP) of 800.
  • Example 3 Manufacture of staple fiber from cotton linter pulp
  • Cotton linter pulp (supplied from Korea Minting and Security Printing Corporation) of a polymerization degree (DP) of 1200 was introduced into a pulverizer equipped with a 100 mesh filter to prepare pulp powder having a diameter of 1700 ⁇ m or less.
  • the pulp powder was swollen in a 50 wt% NMMO aqueous solution.
  • the NMMO aqueous solution included 6 wt% of the pulp, and an antioxidant was added in the content of 0.01 wt% to the cotton linter pulp.
  • the swollen pulp slurry was injected into a kneader maintaining an internal temperature of 90 °C and absolute pressure of 50 mmHg with a rotary valve pump at a speed of 16 kg/hour, and completely dissolved while removing extra moisture so that a 50 wt% NMMO aqueous solution may become an 89 wt% NMMO aqueous solution, and then spinning dope was discharged through a discharge screw.
  • the spinning dope was controlled so that total fineness of the final filament may become 45,000 denier, and was spun using a nozzle having 30,000 nozzles and a diameter of 0.2 mm. At this time, a 50 mm air gap was formed between the nozzle and the coagulation bath, and in the air gap, 15 °C cooling air was supplied to discharged dope at an air volume of 1500 m 3 /hr.
  • the multifilament that passed through the air gap and was coagulated in the coagulation bath was washed with water in an 8-stage washing apparatus, and then non-dried multifilament yarn controlled to a moisture content of 250 % was dried in a 3-stage drying roll to obtain lyocell multifilament yarn.
  • the tension between the 1 st stage and the 2 nd stage of the drying roll was controlled to 0.2 g/d
  • the tension between the 2 nd stage and the 3 rd stage was controlled to 0.5 g/d
  • the temperature of each roll was sequentially controlled to 130 °C, 150 °C, and 170 °C.
  • the number of filaments of the manufactured lyocell filament yarn was 30,000, and the mean fineness was 1.5 d. 13/inch crimps were given to the dried filament tow in a crimper, and the crimped tow was completely dried at 120 °C in a non-tension drier (lattice drier), and then cut to 38 mm for cotton spinning, to manufacture staple fiber.
  • Example 4 Manufacture of staple fiber from cotton linter pulp
  • Lyocell staple fiber was obtained by the same method as Example 3, except using cotton linter pulp of a polymerization degree (DP) of 800.
  • Comparative Example 1 Manufacture of lyocell filament fiber from softwood pulp sheet
  • Softwood pulp sheet (Buckeye company, V81, DP 1200) was introduced into a pulverizer equipped with a 100 mesh filter to prepare pulp powder having a diameter of 1700 ⁇ m or less.
  • the pulp powder was swollen in a 50 wt% NMMO aqueous solution.
  • the NMMO aqueous solution included 6 wt% of the pulp, and an antioxidant was added in the content of 0.01 wt% to the cotton linter pulp.
  • the swollen pulp slurry was injected into a kneader maintaining an internal temperature of 90 °C and absolute pressure of 50 mmHg with a rotary valve pump at a speed of 16 kg/hour, and completely dissolved while removing extra moisture so that a 50 wt% NMMO aqueous solution may become an 89 wt% of NMMO aqueous solution, and then spinning dope was discharged through a discharge screw.
  • the spinning dope was controlled so that total fineness of the final filament may become 45,000 denier, and was spun using a nozzle having 30,000 nozzles and a diameter of 0.2 mm. At this time, a 50 mm air gap was formed between the nozzle and the coagulation bath, and in the air gap, 15 °C cooling air was supplied to discharged dope at an air volume of 1500 m 3 /hr.
  • the multifilament that passed through the air gap and was coagulated in the coagulation bath was washed with water in an 8-stage washing apparatus, and then non-dried multifilament yarn controlled to a moisture content of 250 % was dried in a 3-stage drying roll to obtain lyocell multifilament yarn.
  • the tension between the 1 st stage and the 2 nd stage of the drying roll was controlled to 0.2 g/d
  • the tension between the 2 nd stage and the 3 rd stage was controlled to 0.5 g/d
  • the temperature of each roll was sequentially controlled to 130 °C, 150 °C, and 170 °C.
  • the number of filaments of the manufactured lyocell filament yarn was 30,000, and the mean fineness was 1.5 d. 13/inch crimps were given to the dried filament tow in a crimper, and the crimped tow was completely dried at 120 °C in a non-tension drier (lattice drier) and then cut to 38 mm for cotton spinning, to manufacture staple fiber.
  • Comparative Example 2 Manufacture of lyocell filament fiber from softwood pulp sheet
  • Lyocell filament fiber was manufactured by the same method as Comparative Example 1, except that softwood pulp sheet (Buckeye company, V-60, DP 800) was introduced into a pulverizer equipped with a 100 mesh filter to prepare pulp powder having a diameter of 1700 ⁇ m or less.
  • softwood pulp sheet Buckeye company, V-60, DP 800
  • Softwood pulp sheet (Buckeye company, V81, DP 1200) was introduced into a pulverizer equipped with a 100 mesh filter to prepare pulp powder having a diameter of 1700 ⁇ m or less.
  • the pulp powder was swollen in a 50 wt% NMMO aqueous solution.
  • the NMMO aqueous solution included 6 wt% of the pulp, and an antioxidant was added in the content of 0.01 wt% to the cotton linter pulp.
  • the swollen pulp slurry was injected into a kneader maintaining an interior temperature of 90 °C and absolute pressure of 50 mmHg with a rotary valve pump at a speed of 16 kg/hour, and completely dissolved while removing extra moisture so that a 50 wt% NMMO aqueous solution may become an 89 wt% of NMMO aqueous solution, and then spinning dope was discharged through a discharge screw.
  • the spinning dope was controlled so that total fineness of the final filament may become 45,000 denier, and was spun using a nozzle having 30,000 nozzles and a diameter of 0.2 mm. At this time, a 50 mm air gap was formed between the nozzle and the coagulation bath, and in the air gap, 15 °C cooling air was supplied to discharged dope at an air volume of 1500 m 3 /hr.
  • the multifilament that passed through the air gap and was coagulated in the coagulation bath was washed with water in an 8-stage washing apparatus, and then the non-dried multifilament yarn controlled to a moisture content of 250 % was dried in a 3-stage drying roll to obtain lyocell multifilament yarn.
  • the tension between the 1 st stage and the 2 nd stage of the drying roll was controlled to 0.2 g/d
  • the tension between the 2 nd stage and the 3 rd stage was controlled to 0.5 g/d
  • the temperature of each roll was sequentially controlled to 130 °C, 150 °C, and 170 °C.
  • the number of filaments of the manufactured lyocell filament yarn was 30,000, and the mean fineness was 1.5 d. 13/inch crimps were given to the dried filament tow in a crimper, and the crimped tow was completely dried at 120 °C in a non-tension drier (lattice drier) and then cut to 38 mm for cotton spinning, to manufacture staple fiber.
  • Staple fiber was manufactured by the same method as Comparative Example 3, except that softwood pulp sheet (Buckeye company, V-60, DP 800) was introduced into a pulverizer equipped with a 100 mesh filter to prepare pulp powder having a diameter of 1700 ⁇ m or less.
  • softwood pulp sheet Buckeye company, V-60, DP 800
  • the filament tow immediately before being finally cut in Examples 3 and 4 and Comparative Examples 3 and 4 was extracted as a specimen.
  • the length of the specimen was controlled to 250 mm.
  • the pulp powder of the examples and comparative examples were immersed in a 17.5 % NaOH solution at 20 °C for 20 minutes, and then non-dissolved material was dried and the weight was measured.
  • the non-dissolved material is alpha cellulose, and the content was calculated according to the following General Formula 2.
  • 0.1g of a filament cut to 5 mm and 1 ml of pure water were introduced into a cylindrical cylinder with a diameter of 10 mm and a length of 30 mm, and the cylinder was sealed and then fibrillation degree of the lyocell filament fiber obtained in the examples and comparative examples was measured using an apparatus for reciprocating 10 times per second.
  • the specific measurement method and conditions are as follows.
  • Fibrillation degree Grade number of fibrils/unit length of filament 0.1 mm _
  • the lyocell staple fiber manufactured in the examples exhibits elongation equal to or better than the conventional fiber of the comparative examples, and simultaneously exhibits better strength and remarkably superior fibrillation degree.
  • the staple fiber of the examples maintains excellent strength and elongation, and simultaneously exhibits excellent feel due to the excellent fibrillation degree and thus it may be preferably applied for a fabric for high grade clothing and the like.

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
  • Artificial Filaments (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)

Claims (11)

  1. Spinnlösung zum Spinnen von Lyocell, umfassend:
    Baumwolllinterzellstoff, der 99 Gew.-% oder mehr alpha-Cellulose enthält; und
    eine wässrige Lösung von N-Methylmorpholin-N-oxid (NMMO).
  2. Spinnlösung zum Spinnen von Lyocell nach Anspruch 1, umfassend:
    6 bis 16 Gew.-% des Baumwolllinterzellstoffs; und
    84 bis 94 Gew.-% der wässrigen Lösung von N-Methylmorpholin-N-oxid.
  3. Spinnlösung zum Spinnen von Lyocell nach Anspruch 1, wobei die wässrigen Lösung von N-Methylmorpholin-N-oxid N-Methylmorpholin-N-oxid und Wasser in einem Gewichtsverhältnis von 91:9 bis 83:17 umfasst.
  4. Verfahren zur Herstellung von Lyocell-Filamentfaser, umfassend:
    Abziehen der Spinnlösung nach irgendeinem der Ansprüche 1 bis 3 von einem Spinner;
    Passieren der abgezogenen Spinnlösung durch ein Koagulationsbad, um diese zu einem Filament zu koagulieren;
    Waschen des Filaments, welches das Koagulationsbad passiert hat; und
    Trocknen des gewaschenen Filaments.
  5. Verfahren zur Herstellung von Lyocell-Filamentfaser nach Anspruch 4, wobei das Abziehen der Spinnlösung von einem Spinner bei 80 bis 130°C durchgeführt wird.
  6. Verfahren zur Herstellung von Lyocell-Filamentfaser nach Anspruch 4, wobei das Trocknen des gewaschenen Filaments das Anlegen einer Spannung von 0,1 bis 1 g/d an das Filament bei 80 bis 200°C umfasst.
  7. Lyocell-Filamentfaser, hergestellt nach irgendeinem der Ansprüche 4 bis 6.
  8. Lyocell-Filamentfaser nach Anspruch 7, wobei die Lyocell-Filamentfaser eine Festigkeit von 4 bis 8 g/d und einen Anfangsmodul von 150 bis 230 g/d aufweist.
  9. Verfahren zur Herstellung von Lyocell-Stapelfaser, umfassend:
    Abziehen einer Spinnlösung, umfassend Baumwolllinterzellstoff, welcher 99 Gew.-% oder mehr alpha-Cellulose und eine wässrige Lösung von N-Methylmorpholin-N-oxid (NMMO) enthält, von einem Spinner;
    Passieren der abgezogenen Spinnlösung durch ein Koagulationsbad, um diese zu einem Filament zu koagulieren;
    Waschen des Filaments, welches das Koagulationsbad passiert hat;
    Trocknen des gewaschenen Filaments;
    Kräuseln des getrockneten Filaments; und
    Schneiden des gekräuselten Filaments.
  10. Verfahren zur Herstellung von Lyocell-Stapelfaser nach Anspruch 9, wobei der Schritt des Kräuselns das Vorsehen von 8-20/Inch Kräuselungen an dem Filament beinhaltet.
  11. Verfahren zur Herstellung von Lyocell-Stapelfaser nach Anspruch 9, wobei der Schritt des Schneidens das Schneiden des Filaments zu einer Länge von 20 bis 200 mm beinhaltet.
EP11801135.2A 2010-06-30 2011-06-29 Spinnlösung zum spinnen einer lyozelle, verfahren zur herstellung einer lyozellenfilamentfaser und verfahren zur herstellung einer lyozellenstapelfaser damit Active EP2589689B1 (de)

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KR1020100094505A KR101385275B1 (ko) 2010-09-29 2010-09-29 라이오셀 스테이플 섬유의 제조 방법 및 이로부터 제조되는 라이오셀 스테이플 섬유
PCT/KR2011/004752 WO2012002729A2 (ko) 2010-06-30 2011-06-29 라이오셀 방사용 도프, 이를 이용한 라이오셀 필라멘트 섬유의 제조방법 및 이를 이용한 라이오셀 스테이플 섬유의 제조 방법

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Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101455002B1 (ko) * 2013-06-28 2014-11-03 코오롱인더스트리 주식회사 담배필터용 라이오셀 소재 및 그 제조방법
JP6370890B2 (ja) 2013-09-26 2018-08-08 コーロン インダストリーズ インク タバコフィルター用リヨセル素材及びその製造方法
AT515180B1 (de) 2013-10-15 2016-06-15 Chemiefaser Lenzing Ag Dreidimensionaler cellulosischer Formkörper, Verfahren zu seiner Herstellung und seine Verwendung
AT515174B1 (de) 2013-10-15 2019-05-15 Chemiefaser Lenzing Ag Cellulosesuspension, Verfahren zu ihrer Herstellung und Verwendung
AT515152B1 (de) * 2013-11-26 2015-12-15 Chemiefaser Lenzing Ag Verfahren zum Vorbehandeln von rückgewonnenen Baumwollfasern zur Verwendung bei der Herstellung von Formkörpern aus regenerierter Cellulose
KR102211219B1 (ko) 2014-06-30 2021-02-03 코오롱인더스트리 주식회사 담배필터용 이형단면 라이오셀 소재 및 그 제조방법
KR102157887B1 (ko) * 2014-09-30 2020-09-18 코오롱인더스트리 주식회사 라이오셀 크림프 섬유
KR102211186B1 (ko) 2014-12-31 2021-02-03 코오롱인더스트리 주식회사 담배필터용 라이오셀 소재 및 그 제조방법
AT517020B1 (de) 2015-02-06 2020-02-15 Chemiefaser Lenzing Ag Recycling von cellulosischen Kunstfasern
EP3385429A1 (de) * 2017-04-03 2018-10-10 Lenzing Aktiengesellschaft Cellulosefaservliesstoff mit faserverbundenen, strahlungsableitenden teilchen
EP3467163A1 (de) * 2017-10-06 2019-04-10 Lenzing Aktiengesellschaft Futterstoff aus lyocell-filamenten
CN108239822A (zh) * 2018-03-14 2018-07-03 天津工业大学 一种Lyocell长丝非织造材料及其制备方法
KR102352034B1 (ko) * 2018-06-29 2022-01-14 코오롱인더스트리 주식회사 라이오셀 섬유를 포함하는 부직 섬유 집합체
EP3674455A1 (de) * 2018-12-28 2020-07-01 Lenzing Aktiengesellschaft Verfahren zur flüssigkeitsentfernung aus cellulosefilamenten, -fäden oder -fasern
CN111155183B (zh) * 2019-12-31 2021-08-31 中国纺织科学研究院有限公司 一种纤维素纤维连续制备方法
CN112064128A (zh) * 2020-09-21 2020-12-11 常隆塑胶科技(苏州)有限公司 一种尼龙导电碳纤维生产装置及其生产工艺
CN112538663A (zh) * 2020-12-04 2021-03-23 上海即索实业有限公司 一种莱赛尔纤维、莱赛尔纤维面膜布及其制作方法
CN113250004A (zh) * 2021-05-31 2021-08-13 山东银鹰股份有限公司 一种莱赛尔纤维用棉浆粕的清洁制浆工艺
CN117448981A (zh) * 2023-12-22 2024-01-26 山东鸿泰鼎新材料科技有限公司 一种含罗布麻活性成分的功能性莱赛尔纤维的制造方法

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1433881A2 (de) * 2002-12-26 2004-06-30 Hyosung Corporation Multifilamentgarn aus Zellulose für Reifencorde und Herstellungsverfahren
US20080173419A1 (en) * 2007-01-19 2008-07-24 Georgia-Pacific Consumer Products Lp Method of making regenerated cellulose microfibers and absorbent products incorporating same
KR20090025977A (ko) * 2007-09-07 2009-03-11 주식회사 코오롱 셀룰로오스계 섬유, 타이어 코오드, 및 방사 유제

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9412500D0 (en) * 1994-06-22 1994-08-10 Courtaulds Fibres Holdings Ltd Fibre manufacture
GB9412501D0 (en) * 1994-06-22 1994-08-10 Courtaulds Fibres Holdings Ltd Manufacture of fibre
AT401393B (de) * 1994-09-05 1996-08-26 Chemiefaser Lenzing Ag Verfahren zur herstellung von cellulosefasern
GB9605504D0 (en) * 1996-03-15 1996-05-15 Courtaulds Plc Manufacture of elongate members
DE69723582T2 (de) * 1996-11-21 2004-05-13 Toyo Boseki K.K. Fasern aus regenerierte zellulose und verfahren zu ihrer herstellung
EP0853146A3 (de) * 1997-01-09 1999-03-24 Akzo Nobel N.V. Verfahren zur Herstellung von cellulosischen Fasern und cellulosische Fasern
CN1061106C (zh) * 1997-12-09 2001-01-24 宜宾丝丽雅集团有限公司 溶剂法纤维素纤维制造方法
DE10043297B4 (de) * 2000-09-02 2005-12-08 Thüringisches Institut für Textil- und Kunststoff-Forschung e.V. Verfahren zur Herstellung von Cellulosefasern und Cellulosefilamentgarnen
CN1184364C (zh) * 2001-09-11 2005-01-12 东华大学 溶剂法生产纤维素纤维的纺丝原液的制备工艺
CN1172035C (zh) * 2002-12-11 2004-10-20 东华大学 溶剂法纤维素纤维的纺丝原液的制备工艺
KR100488604B1 (ko) * 2003-07-25 2005-05-11 주식회사 효성 라이오셀 멀티 필라멘트
US7459015B2 (en) * 2004-04-16 2008-12-02 Birla Research Institute For Applied Sciences Process for the preparation of a cellulose solution for spinning of fibres, filaments or films therefrom
CN101240466B (zh) * 2008-03-14 2010-12-29 宜宾丝丽雅集团有限公司 溶剂法纤维素棉、竹复合纤维及其制备方法
ES2402442T3 (es) * 2008-03-27 2013-05-03 Cordenka Gmbh & Co. Kg Cuerpos celulósicos conformados

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1433881A2 (de) * 2002-12-26 2004-06-30 Hyosung Corporation Multifilamentgarn aus Zellulose für Reifencorde und Herstellungsverfahren
US20080173419A1 (en) * 2007-01-19 2008-07-24 Georgia-Pacific Consumer Products Lp Method of making regenerated cellulose microfibers and absorbent products incorporating same
KR20090025977A (ko) * 2007-09-07 2009-03-11 주식회사 코오롱 셀룰로오스계 섬유, 타이어 코오드, 및 방사 유제

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
AXEL SCZOSTAK: "Cotton Linters: An Alternative Cellulosic Raw Material", MACROMOLECULAR SYMPOSIA., vol. 280, no. 1, 1 June 2009 (2009-06-01), DE, pages 45 - 53, XP055373670, ISSN: 1022-1360, DOI: 10.1002/masy.200950606 *

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