EP3257975B1 - Method of making a fiber of polyacrylonitrile - cellulose acetate - Google Patents

Method of making a fiber of polyacrylonitrile - cellulose acetate Download PDF

Info

Publication number
EP3257975B1
EP3257975B1 EP16748634.9A EP16748634A EP3257975B1 EP 3257975 B1 EP3257975 B1 EP 3257975B1 EP 16748634 A EP16748634 A EP 16748634A EP 3257975 B1 EP3257975 B1 EP 3257975B1
Authority
EP
European Patent Office
Prior art keywords
polyacrylonitrile
fiber
cellulose acetate
temperature
carrying
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
EP16748634.9A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP3257975A1 (en
EP3257975A4 (en
Inventor
Haiou Zhang
Baozhong SHAO
Lijie YANG
Wei Chen
Dongwen HAO
Hailiang Liu
Penglin HAO
Zhiguo DUAN
Guirong GUO
Dewu Song
Xuefeng Yang
Mingzhe Liu
Hua Bai
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jilin Qifeng Chemical Fiber Co Ltd
Original Assignee
Jilin Qifeng Chemical Fiber Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Jilin Qifeng Chemical Fiber Co Ltd filed Critical Jilin Qifeng Chemical Fiber Co Ltd
Publication of EP3257975A1 publication Critical patent/EP3257975A1/en
Publication of EP3257975A4 publication Critical patent/EP3257975A4/en
Application granted granted Critical
Publication of EP3257975B1 publication Critical patent/EP3257975B1/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/06Wet spinning methods
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/44Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds
    • D01F6/54Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds of polymers of unsaturated nitriles
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F8/00Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof
    • D01F8/02Conjugated, i.e. bi- or multicomponent, artificial filaments or the like; Manufacture thereof from cellulose, cellulose derivatives, or proteins

Definitions

  • the present invention relates to a method of making a fiber of polyacrylonitrile - cellulose acetate.
  • Acrylic fiber is one of the principal varieties of synthetic fiber in the world, which is soft in hand feel, bright in color and luster and relatively good in strength and elasticity and has a good reputation as "artificial wool".
  • the acrylic fiber macromolecule has irregular helical conformation and has no true crystalline structures.
  • the strength of the acrylic fiber is much higher than that of natural fiber and regenerated fiber, the acid resistance of the acrylic fiber is good, and the weather resistance is good.
  • Feedstock polyacrylonitrile (PAN) contains a large number of hydrophobic groups, so that the acrylic fiber is relatively poor in hygroscopicity and generates static electricity extremely easily.
  • the static electricity can cause the fiber to wind or block up a machine element and affect the successful proceeding of a weaving process. Due to the accumulation of electrostatic charges on clothing, wearers easily feel uncomfortable, so that the wearability of acrylic-fiber textiles is lowered, and thus, the further development of the acrylic-fiber textiles is limited.
  • An important method for modifying the antistatic property of the acrylic fiber is to blend an antistatic agent and an acrylic fiber spinning stock solution and then carry out spinning to obtain fiber.
  • a frequently-used blended type antistatic agent is carbon black.
  • CN101805935A discloses a novel antistatic acrylic fiber and a preparation method thereof.
  • the acrylic fiber comprises carbon nano-tubes and carbon black, wherein the weight percent of the carbon nano-tubes is 1-15%, the weight percent of the carbon black is 1-3%, and the weight percent of polyacrylonitrile is 82-98%.
  • the prepared fiber is black, so that the use of the prepared fiber is limited.
  • the antistatic property of the acrylic fiber can also be improved by proper physical and chemical methods, but that causes environmental pollutions of different degrees.
  • a doctoral dissertation, i.e., plasma antistatic treatment of acrylic fiber proposes provides a method for improving the antistatic property of the acrylic fiber through carrying out surface modification on the acrylic fiber by adopting a low-temperature plasma technology.
  • the low-temperature plasma technology is water-saving, energy-saving and pollution-free and has remarkable economic and environmental protection effects.
  • the method is relatively high in requirements and has certain difficulty in actual popularized application.
  • Cellulose acetate fiber is good in hygroscopicity, has a moisture regain of 6%, can be dyed with disperse dyes and has good wearability. Filaments are elegant in luster and soft in hand feel, have good drapability, look exactly like real silk, are suitable for producing underwear, bathrobes, children's wear, lady's garments, indoor decorative fabrics and the like and can also be used for producing cigarette filters. However, the cellulose acetate fiber is low in strength and poor in wearability.
  • copolyacrylonitrile is prepared by an aqueous-phase precipitation polymerization method in a manner of taking acrylonitrile (AN), a potential crosslinker (2-hydroxypropyl acrylate) and vinyl acetate (VAc) as monomers and taking sodium chlorate (NaClO 3 ) as an initiator.
  • AN acrylonitrile
  • VAc vinyl acetate
  • the copolyacrylonitrile fiber which has relatively high water absorption and water retention capacity, is free of irritation and has certain strength, is obtained through preparing copolyacrylonitrile (CPAN) fiber and CPAN/cellulose acetate (CA) blended fiber (CPAN-CA) containing crosslinker through wet spinning by taking N, N-dimethylacetamide (DMAc) as a solvent, preparing copolyacrylonitrile fiber with a crosslinked structure through post-crosslinking and subjecting the fiber to basic hydrolysis.
  • CPAN copolyacrylonitrile
  • CA CPAN/cellulose acetate
  • DMAc N-dimethylacetamide
  • the front crosslinking agent and the initiator are required to be added during the preparation of copolyacrylonitrile
  • the preparation method is complicated, reactions of multiple steps, i.e., aqueous-phase precipitation polymerization, wet spinning, post-crosslinking and basic hydrolysis are required to be adopted, and the condition that hydrolysis is an indispensable step for preparing the polyacrylonitrile hydrophilic fiber is pointed out.
  • the content of cellulose acetate in the prepared blended fiber is 5%
  • the strength of the blended fiber is maximized and is only 1.4cN/dtex, and then, the strength is lowered along with the increase of the cellulose acetate content.
  • the present invention provides a method to produce a polyacrylonitrile-cellulose acetate fiber to overcome the defects that acrylic fiber is poor in hygroscopicity, and likely to cause static electricity; and meanwhile, to overcome the disadvantages that pure cellulose acetate fiber is low in strength and poor in wearability.
  • the method is simple and feasible and is easy to control in process.
  • the fiber of polyacrylonitrile-cellulose acetate provided by the present invention has the advantages of light weight, warm keeping, good weather resistance, good acid/base resistance, good drapability, difficulty in wrinkling, etc.; and not only is a domestic gap filled up, but also a novel fibrous raw material is provided for the textile industry.
  • a preparation method of the fiber of polyacrylonitrile-cellulose acetate comprises the following steps:
  • step 1) the aqueous-phase suspension polymerization reaction is carried out at a temperature of 58 DEG C to 62 DEG C and at a pH value of 2.5 to 3.5.
  • a mass ratio of cellulose acetate to the powdery polyacrylonitrile is arbitrary, preferably (15-35wt%):(65-85wt%), more preferably (15-30wt%):(70-85wt%).
  • a ratio of the sum of the masses of the powdery polyacrylonitrile and cellulose acetate to the mass of the solvent is (20-25.5):(74.5-80);
  • the solvent is selected from dimethylacetamide, dimethyl sulfoxide, dimethylformamide or sodium thiocyanate;
  • the heating means heating up to a temperature of 80 DEG C to 90 DEG C; and the cooling means cooling down to a temperature of 70 DEG C to 80 DEG C.
  • step 3 the spinning is carried out at a temperature of 80 DEG C to 97 DEG C under a pressure of 0.7MPa to 0.9MPa.
  • the coagulating bath is selected from an aqueous solution of dimethylacetamide, dimethyl sulfoxide, dimethylformamide or sodium thiocyanate and has a concentration of 30-55wt% and a temperature of 25 DEG C to 50 DEG C.
  • the temperature adjustment means adjusting a temperature to 80 DEG C to 97 DEG C and the pressure adjustment means adjusting a pressure to 0.7MPa to 0.9MPa.
  • a drafting ratio is 4 to 10; and the setting is carried out under a pressure of 200KPa to 330KPa.
  • hygroscopicity and antistatic properties of the fiber Due to the characteristics of poor water absorption and hygroscopicity, low moisture regain, antistatic properties and the like, the range of application of ordinary polyacrylonitrile fiber is restricted.
  • the hygroscopicity and antistatic properties of the fiber have a certain internal relationship, so that the other properties can be greatly improved through improving the water absorption and hygroscopicity of the polyacrylonitrile fiber.
  • a variety of hygroscopic fibers prepared through blending polyacrylonitrile and cellulose acetate are disclosed in the prior art, and many articles in the prior art indicate that the break strength of the hygroscopic fiber is maximized and is only 1.4cN/dtex when the content of cellulose acetate is 5%.
  • the inventor consciously and surprisedly discovers that, by adopting a relatively high cellulose acetate mass ratio, the strength of the fiber of polyacrylonitrile-cellulose acetate is increased, and the elongation, moisture regain and specific resistance of the polyacrylonitrile-cellulose acetate fiber are better and exceed expected ranges.
  • the polyacrylonitrile-cellulose acetate fiber has good comprehensive performance and has a break strength of 2.3CN/dtex to 3.0CN/dtex, a breaking elongation of 32-40%, a moisture regain of 2-3% and a specific resistance of 9.0 ⁇ 10 8 ⁇ •CM to 4.8 ⁇ 10 9 ⁇ •CM.
  • the determination of break strength and breaking elongation is carried out according to provisions of GB/T 14337; the determination of moisture regain is carried out according to provisions of GB/T 6503; and the determination of specific resistance is carried out according to provisions of GB/T 14342-1993.
  • the fiber of polyacrylonitrile-cellulose acetate is prepared through dissolving polyacrylonitrile and cellulose acetate with a solvent to obtain a colloid and then carrying out wet spinning.
  • blended fiber of polyacrylonitrile and cellulose acetate is generally prepared through carrying out wet spinning, then, carrying out post-crosslinking, and then, carrying out basic hydrolysis, wherein the condition that hydrolysis is an indispensable step for preparing the polyacrylonitrile hydrophilic fiber is pointed out.
  • the fiber of polyacrylonitrile-cellulose acetate provided by the present invention can be obtained through only dissolving polyacrylonitrile and cellulose acetate with a solvent to obtain a colloid and then carrying out wet spinning without crosslinking, post-crosslinking and basic hydrolysis.
  • the process route is simple, so that processing steps are greatly simplified, the working efficiency is increased, and batch production is facilitated; and physical indexes of the produced polyacrylonitrile-cellulose acetate fiber are closer to indexes of the conventional acrylic fiber.
  • polyacrylonitrile is formed from acrylonitrile and vinyl acetate, wherein a mass ratio of acrylonitrile to vinyl acetate is (92-94wt%):(6-8wt%).
  • polyacrylonitrile is generally prepared from acrylonitrile, vinyl acetate and other ingredients such as a front crosslinking agent, an initiator, three single auxiliaries, an oxidant and a reducer.
  • polyacrylonitrile is prepared from acrylonitrile and vinyl acetate which are in a mass ratio of (92-94wt%):(6-8wt%).
  • a ratio of the sum of the masses of polyacrylonitrile and cellulose acetate to the mass of the solvent is (20-25.5):(74.5-80).
  • the object of the present invention is to provide a preparation method of the fiber of polyacrylonitrile-cellulose acetate.
  • the method is simple and feasible and is easy to control in process.
  • the preparation method of the polyacrylonitrile-cellulose acetate fiber comprises the following steps:
  • copolyacrylonitrile is prepared by an aqueous-phase precipitation polymerization method, taking acrylonitrile (AN), a potential crosslinker (2-hydroxypropyl acrylate) and vinyl acetate (VAc) as monomers and taking sodium chlorate (NaClO 3 ) as an initiator.
  • AN acrylonitrile
  • VAc vinyl acetate
  • Copolyacrylonitrile (CPAN) fiber and CPAN/cellulose acetate (CA) blended fiber (CPAN-CA) with crosslinker is obtained through wet spinning by taking N, N-dimethylacetamide (DMAc) as a solvent, and then the copolyacrylonitrile-base fiber with a crosslinked structure is prepared by post-crosslinking, and is subjected to basic hydrolysis to obtain copolyacrylonitrile-base fiber, which has relatively high water absorption and water retention capacity and certain strength.
  • a front crosslinking agent and the initiator are required to be added during the preparation of copolyacrylonitrile, the preparation method is complicated, and reactions of multiple steps, i.e., aqueous-phase precipitation polymerization, wet spinning, post-crosslinking and basic hydrolysis are required to be adopted.
  • the condition that hydrolysis is an indispensable step for preparing the polyacrylonitrile hydrophilic fiber is emphasized. Obviously, in the prior art, it is generally believed that hydrolysis is an
  • the fiber of polyacrylonitrile-cellulose acetate can be obtained by only adopting two monomers, i.e., acrylonitrile and vinyl acetate, carrying out aqueous-phase suspension polymerization to obtain polyacrylonitrile and then subjecting polyacrylonitrile and cellulose acetate to wet spinning without crosslinking, post-crosslinking and basic hydrolysis.
  • the process route is simple, so that processing steps are greatly simplified, the working efficiency is increased, and batch production is facilitated; and physical indexes of the produced fiber of polyacrylonitrile-cellulose acetate are closer to indexes of the conventional acrylic fiber.
  • step 1) the aqueous-phase suspension polymerization reaction is carried out at a temperature of 58 DEG C to 62 DEG C and at a pH value of 2.5 to 3.5.
  • a mass ratio of cellulose acetate to the powdery polyacrylonitrile is arbitrary, preferably (15-35wt%):(65-85wt%), more preferably (15-30wt%):(70-85wt%).
  • a ratio of the sum of the masses of the powdery polyacrylonitrile and cellulose acetate to the mass of the solvent is (20-25.5):(74.5-80);
  • the solvent is selected from dimethylacetamide, dimethyl sulfoxide, dimethylformamide or sodium thiocyanate;
  • the heating means heating up to a temperature of 80 DEG C to 90 DEG C; and the cooling means cooling down to a temperature of 70 DEG C to 80 DEG C.
  • step 3 the spinning is carried out at a temperature of 80 DEG C to 97 DEG C under a pressure of 0.7MPa to 0.9MPa.
  • the coagulating bath is selected from an aqueous solution of dimethylacetamide, dimethyl sulfoxide, dimethylformamide or sodium thiocyanate and has a concentration of 30-55wt% and a temperature of 25 DEG C to 50 DEG C.
  • the temperature adjustment means adjusting a temperature to 80 DEG C to 97 DEG C and the pressure adjustment means adjusting a pressure to 0.7MPa to 0.9MPa.
  • a drafting ratio is 4 to 10; and the setting is carried out under a pressure of 200KPa to 330KPa.
  • the preparation method provided by the present invention is simple and feasible in process, and the prepared polyacrylonitrile-cellulose acetate fiber is good in comprehensive performance and has a break strength of 2.3CN/dtex to 3.0CN/dtex, a breaking elongation of 32-40%, a moisture regain of 2-3% and a specific resistance of 9.0 ⁇ 10 8 ⁇ •CM to 4.8 ⁇ 10 9 ⁇ •CM.
  • the fiber of polyacrylonitrile-cellulose acetate and the preparation method thereof have the following advantages:
  • Polyacrylonitrile was prepared by the means of an intermittent aqueous-phase precipitation polymerization method. Specifically, white powdery polyacrylonitrile was prepared by controlling a temperature in a four-mouthed flask to 45+/-2 DEG C through a constant-temperature circulating water bath, then adding acrylonitrile (AN), vinyl acetate (VAc) and a potential crosslinker (HQ) into the flask according to a certain ratio under nitrogen protection, adjusting a pH value to about 2, and adding an initiator, i.e., NaClO 3 -Na 2 SO 3 to initiate a polymerization reaction, controlling polymerization time to 1.5 hours, adding NaOH to terminate the reaction, and then carrying out filtering and baking.
  • AN acrylonitrile
  • VAc vinyl acetate
  • HQ potential crosslinker
  • the blended fiber was obtained as the following step: blending the prepared white powdery polyacrylonitrile and cellulose acetate separately according to mass ratios of 85/15, 80/20, 75/25, 70/30 and 65/35, preparing a DMAc spinning solution according to a concentration of 20%, putting the spinning solution into a spinning kettle, carrying out uniform stirring and mixing at a certain rate of revolution to obtain a brown and transparent uniform solution, carrying out vacuumized deaeration at a temperature of 60 DEG C, spinning nascent fiber by a wet spinning process in a manner of taking a 40% DMAc aqueous solution as a coagulating bath, and carried out coagulating shaping, drafting, relaxing and drying to obtain the blended fiber.
  • Blended fiber with a crosslinked network structure was obtained through naturally airing the above-mentioned prepared fiber, and subjecting the aired fiber to crosslinking for appropriate time in a baking oven with a temperature of 180 DEG C to allow functional groups inside fiber macromolecules to be subjected to a dehydrated crosslinking reaction.
  • Blended fiber with hydrophilicity was obtained through putting blended staple fiber into alkali liquor tanks of different concentrations and different temperatures, controlling hydrolysis time, taking out the hydrolyzed fiber, neutralizing residual alkali liquor on the surface of the fiber with hydrochloric acid, sufficiently washing the fiber with distilled water, and carrying out natural air-drying.
  • Test samples the fiber of polyacrylonitrile-cellulose acetate provided by the present invention was prepared through blending polyacrylonitrile and cellulose acetate separately according to mass ratios of 85/15, 80/20, 75/25, 70/30 and 65/35 according to the method provided by the embodiment 1 of the present invention.
  • Control samples the blended fiber in the prior art was prepared through blending polyacrylonitrile and cellulose acetate separately according to mass ratios of 85/15, 80/20, 75/25, 70/30 and 65/35 according to the method provided by the comparative example.
  • test example main technical indexes of the fiber of polyacrylonitrile-cellulose acetate prepared by the method provided by the present invention and main technical indexes of the conventional acrylic fiber and cellulose acetate fiber were tested separately, and results were separately shown in a table 2 and a table 3 as follows. Determination provisions were the same as those in the test example 1.
  • Table 2 Main technical indexes of the polyacrylonitrile-cellulose acetate fiber prepared by the method provided by the present invention and main technical indexes of the conventional acrylic fiber Specifica tions (dtex) Variety (glazed) Size (dtex) Break strength (CN/dtex) Breaking elongation (%) Moisture regain (%) Specific resistance ( ⁇ • CM) 1.33 polyacrylonitril e-cellulose acetate fiber 1.4 2.5 34 2.63 9.27 ⁇ 10 8 1.33 conventional acrylic fiber 1.31 2.69 35 0.81 2.75 ⁇ 10 12 1.67 polyacrylonitril e-cellulose acetate fiber 1.78 2.68 36 2.1 4.73 ⁇ 10 9 1.67 conventional acrylic fiber 1.70 2.71 38 0.93 9.13 ⁇ 10 11
  • Table 3 Main technical indexes of the fiber of polyacrylonitrile-cellulose acetate prepared by the method provided by the present invention and main technical indexes of the conventional cellulose acetate fiber Specifications (dtex) Variety (glazed) Break strength (CN/dtex) Breaking elongation (%)
  • the fiber of polyacrylonitrile-cellulose acetate was prepared from polyacrylonitrile and cellulose acetate in different proportioning ratios according to the method provided by the embodiment 1, the moisture regain and specific resistance of the fiber of polyacrylonitrile-cellulose acetate were investigated, and results were shown in a table 4. Determination provisions were the same as those in the test example 1.
  • a mass ratio of cellulose acetate to polyacrylonitrile is preferably (15-35wt%):(65-85wt%), more preferably (15-30wt%):(70-85wt%).

Landscapes

  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Artificial Filaments (AREA)
EP16748634.9A 2015-02-13 2016-01-29 Method of making a fiber of polyacrylonitrile - cellulose acetate Active EP3257975B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201510079823.2A CN105002592B (zh) 2015-02-13 2015-02-13 一种醋腈纤维及其制备方法
PCT/CN2016/072777 WO2016127833A1 (zh) 2015-02-13 2016-01-29 一种醋腈纤维及其制备方法

Publications (3)

Publication Number Publication Date
EP3257975A1 EP3257975A1 (en) 2017-12-20
EP3257975A4 EP3257975A4 (en) 2017-12-20
EP3257975B1 true EP3257975B1 (en) 2019-04-03

Family

ID=54375442

Family Applications (1)

Application Number Title Priority Date Filing Date
EP16748634.9A Active EP3257975B1 (en) 2015-02-13 2016-01-29 Method of making a fiber of polyacrylonitrile - cellulose acetate

Country Status (4)

Country Link
EP (1) EP3257975B1 (zh)
CN (1) CN105002592B (zh)
TR (1) TR201909285T4 (zh)
WO (1) WO2016127833A1 (zh)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105002592B (zh) * 2015-02-13 2017-10-17 吉林奇峰化纤股份有限公司 一种醋腈纤维及其制备方法
CN107385591A (zh) * 2016-05-17 2017-11-24 句容市润龙纺织品有限公司 一种醋青纤维纱及其加工工艺
CN107541808B (zh) * 2016-06-29 2020-08-04 吉林富博纤维研究院有限公司 一种采用湿法纺丝工艺制备醋腈长丝的方法
CN106012076B (zh) * 2016-07-15 2018-06-19 吉林富博纤维研究院有限公司 一种醋酸纤维的湿法纺丝制备方法
CN107245770A (zh) * 2017-02-16 2017-10-13 王和军 一种可中和酸碱的新型纤维
CN110016728B (zh) * 2018-01-08 2022-04-22 吉林吉盟腈纶有限公司 一种聚丙烯腈石墨烯纤维的制备方法
CN110295437A (zh) * 2018-03-23 2019-10-01 上海水星家用纺织品股份有限公司 一种应用醋青纤维的家纺用面料
CN109371718B (zh) * 2018-10-29 2020-11-06 绍兴文理学院 一种小蘖碱对醋青纤维的染色方法
CN111220657A (zh) * 2020-03-27 2020-06-02 中简科技股份有限公司 一种聚丙烯腈碳纤维pH测试方法
CN112080830A (zh) * 2020-08-20 2020-12-15 江苏瑞康安全装备有限公司 一种色丁布用弹性好手感柔软蓬松的腈纶丝
CN113373528A (zh) * 2021-06-09 2021-09-10 温州市名达服饰有限公司 一种保暖西裤及其保暖层

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH432721A (fr) * 1964-01-25 1967-03-31 Rhodiaceta Procédé de préparation de mélanges filables de matières à poids moléculaire élevé
JPH0299609A (ja) * 1988-10-03 1990-04-11 Mitsubishi Rayon Co Ltd 新規なアクリル系合成繊維の製造方法
JP3851192B2 (ja) * 2001-07-11 2006-11-29 三菱レイヨン株式会社 アクリル系複合繊維の製造方法
CN100491608C (zh) * 2007-06-12 2009-05-27 天津工业大学 亲水性共聚丙烯腈纤维的制备方法
CN100535210C (zh) * 2007-07-31 2009-09-02 浙江杭州湾腈纶有限公司 一种建筑用腈纶制备方法
CN103498208B (zh) * 2013-09-26 2016-03-30 吉林奇峰化纤股份有限公司 蓄热纤维及其制备方法
CN103882547B (zh) * 2014-02-27 2016-07-06 宁波中新腈纶有限公司 一种扁平腈纶纤维及其生产方法
CN105002592B (zh) * 2015-02-13 2017-10-17 吉林奇峰化纤股份有限公司 一种醋腈纤维及其制备方法

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

Also Published As

Publication number Publication date
WO2016127833A1 (zh) 2016-08-18
TR201909285T4 (tr) 2019-07-22
EP3257975A1 (en) 2017-12-20
CN105002592A (zh) 2015-10-28
CN105002592B (zh) 2017-10-17
EP3257975A4 (en) 2017-12-20

Similar Documents

Publication Publication Date Title
EP3257975B1 (en) Method of making a fiber of polyacrylonitrile - cellulose acetate
CN103710782A (zh) 一种高吸湿易染仿棉聚酯短纤维及其制备方法
CN110747649B (zh) 一种亲水增深有机硅柔软剂、制备方法及织物
CN107313128A (zh) 一种pbt纤维制造工艺
CN107475794B (zh) 一种硅氮系阻燃高湿模量粘胶纤维及其制备方法
CN102409427B (zh) 一种具有抗紫外线、抗静电、抗起球复合功能的聚酯纤维的制备方法
CN105367673A (zh) 一种氧化交联改性淀粉及其制备方法
CN112853535B (zh) 一种假发用复合纤维材料及其制备方法
CN112127000B (zh) 一种远红外腈纶纤维及其制备方法
CN106283224B (zh) 一种湿法大有光腈纶的制备方法
CN102409429A (zh) 一种高舒适复合功能聚酯纤维的制备方法
CN102443876A (zh) 一种具有抗紫外线、抗老化、吸湿速干复合功能的聚酯纤维的制备方法
CN103882546A (zh) 一种高收缩超细腈纶纤维及其制备方法
CN111691001A (zh) 一种离子液体增塑聚酰胺56工业丝的制备方法
CN111607889A (zh) 一种抑菌防霉面料
CN113136633B (zh) 一种长效抑菌阻燃双效莱赛尔纤维及其制备方法
CN111379048B (zh) 一种双组分复合仿毛弹性纤维的制备方法
CN101362821B (zh) 一种ptt聚酯切片及抗静电ptt聚酯纤维的制备方法
CN111424335A (zh) 一种防掉毛抗起球羊毛衫的制备方法
CN107419351A (zh) 一种腈纶纤维的制备工艺
CN108929446A (zh) 石墨烯复合母粒、改性纤维、超细纤维革及其制备方法用途
CN111235659A (zh) 具有蓄热保温功能的莱赛尔纤维及其制备方法
CN108330563B (zh) 一种腈纶纤维及其制备方法
CN115182064B (zh) 植物抗菌腈纶及其生产方法
CN114164516A (zh) 高耐光照色牢度的有色涤纶高收缩全拉伸丝的生产方法

Legal Events

Date Code Title Description
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE

PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE

17P Request for examination filed

Effective date: 20170912

A4 Supplementary search report drawn up and despatched

Effective date: 20171103

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

DAV Request for validation of the european patent (deleted)
DAX Request for extension of the european patent (deleted)
GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: GRANT OF PATENT IS INTENDED

INTG Intention to grant announced

Effective date: 20190108

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE PATENT HAS BEEN GRANTED

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

Ref country code: AT

Ref legal event code: REF

Ref document number: 1115860

Country of ref document: AT

Kind code of ref document: T

Effective date: 20190415

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 602016011985

Country of ref document: DE

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

REG Reference to a national code

Ref country code: NL

Ref legal event code: MP

Effective date: 20190403

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG4D

REG Reference to a national code

Ref country code: AT

Ref legal event code: MK05

Ref document number: 1115860

Country of ref document: AT

Kind code of ref document: T

Effective date: 20190403

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

Ref country code: HR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

Ref country code: NO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190703

Ref country code: ES

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190803

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

Ref country code: PL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190703

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190704

Ref country code: RS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190803

Ref country code: AT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 602016011985

Country of ref document: DE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

Ref country code: SM

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

26N No opposition filed

Effective date: 20200106

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20200129

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20200131

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200129

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200131

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200129

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200131

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200131

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200131

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20200129

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20190403

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: TR

Payment date: 20230124

Year of fee payment: 8

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20240125

Year of fee payment: 9