CN111058120B - Method for preparing intelligent fiber through water-phase interface reaction spinning - Google Patents

Method for preparing intelligent fiber through water-phase interface reaction spinning Download PDF

Info

Publication number
CN111058120B
CN111058120B CN201911347195.6A CN201911347195A CN111058120B CN 111058120 B CN111058120 B CN 111058120B CN 201911347195 A CN201911347195 A CN 201911347195A CN 111058120 B CN111058120 B CN 111058120B
Authority
CN
China
Prior art keywords
solution
water
reaction
toluene
fiber
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
CN201911347195.6A
Other languages
Chinese (zh)
Other versions
CN111058120A (en
Inventor
郭静
甘紫文
祁冉冉
管福成
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.)
Dalian Polytechnic University
Original Assignee
Dalian Polytechnic University
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 Dalian Polytechnic University filed Critical Dalian Polytechnic University
Priority to CN201911347195.6A priority Critical patent/CN111058120B/en
Publication of CN111058120A publication Critical patent/CN111058120A/en
Application granted granted Critical
Publication of CN111058120B publication Critical patent/CN111058120B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • D01F6/58Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/70Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyurethanes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/10Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/48Polyethers
    • C08G18/4833Polyethers containing oxyethylene units
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/65Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
    • C08G18/66Compounds of groups C08G18/42, C08G18/48, or C08G18/52
    • C08G18/6666Compounds of group C08G18/48 or C08G18/52
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product
    • Y02P70/62Manufacturing or production processes characterised by the final manufactured product related technologies for production or treatment of textile or flexible materials or products thereof, including footwear

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Artificial Filaments (AREA)

Abstract

本发明涉及功能纤维技术领域,特别是一种水相界面反应纺丝制备智能纤维的方法。本发明提出用水溶液替代传统的扩链剂二胺或二醇作为扩链剂,通过反应纺丝法制备具有温度响应、形状记忆和调温功能的智能纤维材料。与传统技术相比,该方法具有操作简单、节能、环境友好等特点。The invention relates to the technical field of functional fibers, in particular to a method for preparing smart fibers by water-phase interface reaction spinning. The invention proposes to use aqueous solution instead of traditional chain extender diamine or diol as chain extender, and prepare smart fiber material with temperature response, shape memory and temperature regulation functions by reactive spinning method. Compared with the traditional technology, the method has the characteristics of simple operation, energy saving and environmental friendliness.

Description

一种水相界面反应纺丝制备智能纤维的方法A method for preparing smart fibers by water-phase interface reaction spinning

技术领域technical field

本发明涉及功能纤维技术领域,特别是一种水相界面反应纺丝制备智能纤维的方法。The invention relates to the technical field of functional fibers, in particular to a method for preparing smart fibers by water-phase interface reaction spinning.

背景技术Background technique

相聚氨酯纤维具有回弹性优良等优良特性,有纺织“类味精型”纤维的美誉,在织物中只要加入少许氨纶(质量分数2%~25%),就可以改善织物性能,提高织物档次。随着化工、化纤和纺织技术的发展,其应用领域不断拓宽,是典型的形状记忆纤维之一。通常这类纤维通过湿法纺丝或干法纺丝制备,但制备过程需要大量的溶剂,且物料输送能耗大;反应纺丝是先制成聚氨酯预聚体,再加溶剂配制成溶液,然后经纺丝头在凝固浴中扩链固化,凝固浴由二胺或二醇和溶剂组成,二胺或二醇与丝液发生化学反应,加速凝固速度,形成具有三维结构的聚氨酯弹性纤维。由于二胺或二醇的挥发性强,易造成环境污染,使其应用受到限制。Polyurethane fiber has excellent characteristics such as excellent resilience, and has the reputation of textile "MSG-like" fiber. As long as a little spandex (mass fraction 2% to 25%) is added to the fabric, the performance of the fabric can be improved, and the grade of the fabric can be improved. With the development of chemical, chemical fiber and textile technology, its application fields are constantly expanding, and it is one of the typical shape memory fibers. Usually, such fibers are prepared by wet spinning or dry spinning, but the preparation process requires a large amount of solvent, and the material transportation consumes a lot of energy; reaction spinning is to prepare polyurethane prepolymer first, and then add solvent to prepare a solution, Then, it is chain-extended and solidified in a coagulation bath through a spinning head. The coagulation bath is composed of diamine or diol and a solvent. The diamine or diol chemically reacts with the silk liquid to accelerate the coagulation speed and form polyurethane elastic fibers with a three-dimensional structure. Due to the strong volatility of diamine or diol, it is easy to cause environmental pollution, and its application is limited.

发明内容SUMMARY OF THE INVENTION

为解决上述问题,本发明提供一种水相界面反应纺丝制备智能纤维的方法,该纤维制备过程具体如下:In order to solve the above problems, the present invention provides a method for preparing smart fibers by water-phase interface reaction spinning, and the fiber preparation process is as follows:

S1.制备含有聚醚链段的聚氨酯预聚体S1. Preparation of polyurethane prepolymers containing polyether segments

先将二苯基甲烷二异氰酸酯溶于甲苯,在180r/min条件下搅拌,并升温加热至80℃,混合均匀后,滴加少量二月桂酸二丁基锡,混合后得到溶液A;将聚乙二醇溶于甲苯得到溶液B,将溶液B滴加到溶液A,滴完后继续反应1.5-2h;反应结束,产物通过离心法去除杂质,得预聚体;First, diphenylmethane diisocyanate was dissolved in toluene, stirred at 180 r/min, and heated to 80 °C. After mixing uniformly, a small amount of dibutyltin dilaurate was added dropwise, and after mixing, solution A was obtained; The alcohol is dissolved in toluene to obtain solution B, solution B is added dropwise to solution A, and the reaction is continued for 1.5-2 h after the drop is completed; after the reaction is completed, the product is centrifuged to remove impurities to obtain a prepolymer;

S2.配制水基反应介质并注入具有温控装置成型槽S2. Prepare a water-based reaction medium and inject it into a molding tank with a temperature control device

将步骤S1制备的预聚体注入纺丝罐,经计量泵从喷丝孔挤出,挤出液流进入成型槽,与水基介质反应成型并固化4-5min形成纤维,引出纤维,用红外线烘干后卷绕,得到智能响应性纤维。The prepolymer prepared in step S1 is injected into the spinneret, extruded from the spinneret orifice by a metering pump, and the extruded liquid flow enters the forming tank, reacts with the water-based medium and solidifies for 4-5min to form fibers, draws out the fibers, and uses infrared rays to form fibers. After drying, winding is obtained to obtain intelligent responsive fibers.

所述步骤S1中,溶液A由二苯基甲烷二异氰酸酯、甲苯和二月桂酸二丁基锡组成,各原料之间的配比是:二苯基甲烷二异氰酸酯与甲苯的质量配比为1:60-1:90;二月桂酸二丁基锡与二苯基甲烷二异氰酸酯的质量配比为1:25-1:20。In described step S1, solution A is made up of diphenylmethane diisocyanate, toluene and dibutyltin dilaurate, and the ratio between each raw material is: the mass ratio of diphenylmethane diisocyanate and toluene is 1:60. -1:90; the mass ratio of dibutyltin dilaurate to diphenylmethane diisocyanate is 1:25-1:20.

所述步骤S1中,溶液B由聚乙二醇和甲苯组成,聚乙二醇和甲苯质量比为1:7-1:10。In the step S1, the solution B is composed of polyethylene glycol and toluene, and the mass ratio of polyethylene glycol and toluene is 1:7-1:10.

进一步的,所述步骤S1中,溶液A中二苯基甲烷二异氰酸酯与溶液B中聚乙二醇的摩尔比为2:1-2.2:1。溶液B的滴加时间为0.5h,溶液B滴加完毕继续反应时间为1.5-2h。Further, in the step S1, the molar ratio of diphenylmethane diisocyanate in solution A to polyethylene glycol in solution B is 2:1-2.2:1. The dropwise addition time of solution B is 0.5h, and the continuous reaction time is 1.5-2h after the dropwise addition of solution B is completed.

进一步的,所述步骤S1中,聚乙二醇的分子质量为1000-4000。Further, in the step S1, the molecular mass of polyethylene glycol is 1000-4000.

所述步骤S2中,水基反应介质是由二甲基甲酰胺(DMF)、NaHCO3或者乙醇中任一种与水组成的混合物,其中DMF或NaHCO3或乙醇与水的质量混合比为10:90-15:85。In described step S2, water - based reaction medium is by dimethylformamide (DMF), NaHCO or ethanol in any one and the mixture that water forms, wherein DMF or NaHCO or ethanol and the mass mixing ratio of water is 10 . :90-15:85.

因此,所述步骤S2中,从喷丝孔挤出的预聚体与水基介质在10-30℃下反应固化成型,丝条经红外线烘干卷绕,得到智能响应性纤维。Therefore, in the step S2, the prepolymer extruded from the spinneret and the water-based medium are reacted and solidified at 10-30°C, and the filaments are dried and wound by infrared rays to obtain intelligent responsive fibers.

本发明同时请求保护上述方法制备的相变调温功能和温度响应性纤维。The present invention simultaneously claims the phase-change temperature-regulating function and temperature-responsive fibers prepared by the above method.

本发明中选择二苯基甲烷二异氰酸酯为聚氨酯合成用的反应原料,主要作用是与聚乙二醇反应,形成聚氨酯预聚体,在扩链之后构成聚氨酯大分子的硬链段。甲苯在本发明中的作用是:作为反应过程的溶剂和带水剂。二月桂酸二丁基锡在本发明的作用是:作为聚氨酯合成用的催化剂。本发明中聚乙二醇是相变物质,聚乙二醇首先与二苯基甲烷二异氰酸酯反应形成预聚体,再扩链形成软链段。限定聚乙二醇的分子质量在1000-4000可以有效控制相变聚氨酯的相变焓与相变温度。In the present invention, diphenylmethane diisocyanate is selected as the reaction raw material for polyurethane synthesis, and its main function is to react with polyethylene glycol to form a polyurethane prepolymer, which constitutes the hard segment of the polyurethane macromolecule after chain extension. The functions of toluene in the present invention are: as a solvent and a water-carrying agent in the reaction process. The function of dibutyltin dilaurate in the present invention is as a catalyst for polyurethane synthesis. In the present invention, polyethylene glycol is a phase-change substance, and polyethylene glycol first reacts with diphenylmethane diisocyanate to form a prepolymer, and then extends the chain to form a soft segment. Limiting the molecular weight of polyethylene glycol to 1000-4000 can effectively control the phase change enthalpy and phase change temperature of the phase change polyurethane.

有益效果:Beneficial effects:

本发明提出用水溶液替代传统的扩链剂二胺或二醇作为扩链剂,通过反应纺丝法制备具有温度响应、形状记忆和调温功能的智能纤维材料。与传统技术相比,该方法具有操作简单、节能、环境友好等特点。The invention proposes to use aqueous solution instead of traditional chain extender diamine or diol as chain extender, and prepare smart fiber material with temperature response, shape memory and temperature regulation functions by reactive spinning method. Compared with the traditional technology, the method has the characteristics of simple operation, energy saving and environmental friendliness.

附图说明Description of drawings

图1为响应性相变聚氨酯纤维;Figure 1 shows the responsive phase change polyurethane fiber;

图2聚氨酯的红外光谱图。Figure 2 Infrared spectrum of polyurethane.

其中,SSPCPU1-4分别是扩链时使用:10wt%NaHCO3、纯水、10wt%DMF、10wt%乙醇。Among them, SSPCPU1-4 are respectively used in chain extension: 10wt% NaHCO 3 , pure water, 10wt% DMF, 10wt% ethanol.

具体实施方式Detailed ways

下面通过具体实施例详述本发明,但不限制本发明的保护范围。如无特殊说明,本发明所采用的实验方法均为常规方法,所用实验器材、材料、试剂等均可从商业途径获得。The present invention is described in detail below through specific embodiments, but the protection scope of the present invention is not limited. Unless otherwise specified, the experimental methods used in the present invention are all conventional methods, and the experimental equipment, materials, reagents, etc. used can be obtained from commercial channels.

实施例1Example 1

将1.93克二苯基甲烷二异氰酸酯溶于150克甲苯,在180r/min条件下搅拌,并升温加热至80℃,混合均匀后,滴加0.08克二月桂酸二丁基锡,混合后得到溶液A;将7克聚乙二醇2000溶于49克甲苯得到溶液B,用0.5h将溶液B滴加到溶液A,滴完后继续反应2小时;反应结束,将产物在3000r/min下离心滤除杂质,得预聚体;将预聚体从喷丝孔挤出,进入水溶液,反应凝固5分钟,引出纤维,红外线烘干后得到聚氨酯纤维,其相变焓为34.58J/g,相变温度为32.2℃,32℃时具有温度响应。Dissolve 1.93 g of diphenylmethane diisocyanate in 150 g of toluene, stir at 180 r/min, heat the temperature to 80 °C, and after mixing evenly, add 0.08 g of dibutyltin dilaurate dropwise, and mix to obtain solution A; 7 grams of polyethylene glycol 2000 was dissolved in 49 grams of toluene to obtain solution B, and solution B was added dropwise to solution A in 0.5 h, and the reaction was continued for 2 hours after the dripping; after the reaction, the product was centrifugally filtered at 3000 r/min. Impurities are obtained as prepolymers; the prepolymers are extruded from the spinneret holes into the aqueous solution, the reaction solidifies for 5 minutes, the fibers are drawn out, and the polyurethane fibers are obtained after infrared drying. The phase transition enthalpy is 34.58J/g, and the phase transition temperature It is 32.2°C and has a temperature response at 32°C.

实施例2Example 2

将1.93克二苯基甲烷二异氰酸酯溶于150克甲苯,在180r/min条件下搅拌,并升温加热至80℃,混合均匀后,滴加0.06克二月桂酸二丁基锡,混合后得到溶液A;将3.5克聚乙二醇1000溶于35克甲苯得到溶液B,用0.5h将溶液B滴加到溶液A,滴完后继续反应1.5小时;反应结束,将产物在3000r/min下离心滤除杂质,得预聚体;将预聚体从喷丝孔挤出,进入10wt%的碳酸钠水溶液,反应凝固5分钟,引出纤维,红外线烘干后得到聚氨酯纤维,其相变焓为40.1J/g,相变温度为28.2℃,30℃时具有温度响应。Dissolve 1.93 g of diphenylmethane diisocyanate in 150 g of toluene, stir at 180 r/min, heat the temperature to 80 °C, and after mixing evenly, add 0.06 g of dibutyltin dilaurate dropwise, and mix to obtain solution A; Dissolve 3.5 grams of polyethylene glycol 1000 in 35 grams of toluene to obtain solution B, add solution B dropwise to solution A for 0.5 h, and continue to react for 1.5 hours after the dripping; after the reaction is completed, the product is centrifugally filtered at 3000 r/min. Impurities are obtained as prepolymers; the prepolymers are extruded from the spinneret holes into a 10wt% sodium carbonate aqueous solution, and the reaction is solidified for 5 minutes, the fibers are drawn out, and the polyurethane fibers are obtained after infrared drying, and the phase change enthalpy is 40.1J/ g, The phase transition temperature is 28.2 °C, with a temperature response at 30 °C.

实施例3Example 3

将1.76克二苯基甲烷二异氰酸酯溶于105克甲苯,在180r/min条件下搅拌,并升温加热至80℃,混合均匀后,滴加0.08克二月桂酸二丁基锡,混合后得到溶液A;将7克聚乙二醇2000溶于60克甲苯得到溶液B,用0.5h将溶液B滴加到溶液A,滴完后继续反应2小时;反应结束,将产物在3000r/min下离心滤除杂质,得预聚体;将预聚体从喷丝孔挤出,进入10wt%的二甲基甲酰胺水溶液,反应凝固5分钟,引出纤维,红外线烘干后得到聚氨酯纤维,其相变焓为53J/g,相变温度为31℃,30℃时具有温度响应。Dissolve 1.76 g of diphenylmethane diisocyanate in 105 g of toluene, stir at 180 r/min, heat the temperature to 80 °C, and after mixing evenly, add 0.08 g of dibutyltin dilaurate dropwise to obtain solution A after mixing; 7 grams of polyethylene glycol 2000 was dissolved in 60 grams of toluene to obtain solution B, and solution B was added dropwise to solution A in 0.5 h, and the reaction was continued for 2 hours after dripping; after the reaction, the product was centrifugally filtered at 3000 r/min. Impurities are obtained as prepolymers; the prepolymers are extruded from the spinneret holes into a 10 wt% dimethylformamide aqueous solution, and the reaction is solidified for 5 minutes, the fibers are drawn out, and the polyurethane fibers are obtained after infrared drying. The phase change enthalpy is 53J/g, the phase transition temperature is 31℃, and it has a temperature response at 30℃.

实施例4Example 4

将1.93克二苯基甲烷二异氰酸酯溶于150克甲苯,在180r/min条件下搅拌,并升温加热至80℃,混合均匀后,滴加0.06克二月桂酸二丁基锡,混合后得到溶液A;将7克聚乙二醇2000溶于50克甲苯得到溶液B,用0.5h将溶液B滴加到溶液A,滴完后继续反应1.5小时;反应结束,将产物在3000r/min下离心滤除杂质,得预聚体;将预聚体从喷丝孔挤出,进入10wt%的二甲基甲酰胺水溶液,反应凝固5分钟,引出纤维,红外线烘干后得到聚氨酯纤维,其相变焓为53.43J/g,相变温度为31.07℃,31℃时具有温度响应。Dissolve 1.93 g of diphenylmethane diisocyanate in 150 g of toluene, stir at 180 r/min, heat the temperature to 80 °C, and after mixing evenly, add 0.06 g of dibutyltin dilaurate dropwise, and mix to obtain solution A; 7 grams of polyethylene glycol 2000 was dissolved in 50 grams of toluene to obtain solution B, and solution B was added dropwise to solution A in 0.5 h, and the reaction was continued for 1.5 hours after dripping; after the reaction, the product was centrifugally filtered at 3000 r/min. Impurities are obtained as prepolymers; the prepolymers are extruded from the spinneret holes into a 10 wt% dimethylformamide aqueous solution, and the reaction is solidified for 5 minutes, the fibers are drawn out, and the polyurethane fibers are obtained after infrared drying. The phase change enthalpy is 53.43J/g, the phase transition temperature is 31.07℃, and it has a temperature response at 31℃.

实施例5Example 5

将1.93克二苯基甲烷二异氰酸酯溶于150克甲苯,在180r/min条件下搅拌,并升温加热至80℃,混合均匀后,滴加0.06克二月桂酸二丁基锡,混合后得到溶液A;将7克聚乙二醇2000溶于50克甲苯得到溶液B,用0.5h将溶液B滴加到溶液A,滴完后继续反应1.5小时;反应结束,将产物在3000r/min下离心滤除杂质,得预聚体;将预聚体从喷丝孔挤出,进入10wt%的乙醇水溶液,反应凝固3分钟,引出纤维,红外线烘干后得到聚氨酯纤维,其相变焓为48.66J/g,相变温度为27.6℃,29℃时具有温度响应。Dissolve 1.93 g of diphenylmethane diisocyanate in 150 g of toluene, stir at 180 r/min, heat the temperature to 80 °C, and after mixing evenly, add 0.06 g of dibutyltin dilaurate dropwise, and mix to obtain solution A; 7 grams of polyethylene glycol 2000 was dissolved in 50 grams of toluene to obtain solution B, and solution B was added dropwise to solution A in 0.5 h, and the reaction was continued for 1.5 hours after dripping; after the reaction, the product was centrifugally filtered at 3000 r/min. Impurities are obtained as prepolymers; the prepolymers are extruded from the spinneret holes into a 10wt% ethanol aqueous solution, the reaction is solidified for 3 minutes, the fibers are drawn out, and the polyurethane fibers are obtained after infrared drying, and the phase change enthalpy is 48.66J/g , the phase transition temperature is 27.6 °C, and it has a temperature response at 29 °C.

以上所述,仅为本发明创造较佳的具体实施方式,但本发明创造的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明创造披露的技术范围内,根据本发明创造的技术方案及其发明构思加以等同替换或改变,都应涵盖在本发明创造的保护范围之内。The above is only a preferred embodiment of the present invention, but the protection scope of the present invention is not limited to this. The equivalent replacement or modification of the created technical solution and its inventive concept shall be included within the protection scope of the present invention.

Claims (3)

1.一种水相界面反应纺丝制备智能纤维的方法,其特征在于,该纤维制备过程具体如下:1. a method for preparing intelligent fiber by water-phase interface reaction spinning, is characterized in that, this fiber preparation process is specifically as follows: S1.制备含有聚醚链段的聚氨酯预聚体S1. Preparation of polyurethane prepolymers containing polyether segments 先将二苯基甲烷二异氰酸酯溶于甲苯,在180r/min条件下搅拌,并升温加热至80℃,混合均匀后,滴加少量二月桂酸二丁基锡,混合后得到溶液A;将聚乙二醇溶于甲苯得到溶液B,将溶液B滴加到溶液A,滴完后继续反应;反应结束,产物通过离心法去除杂质,得预聚体;聚乙二醇的分子质量为1000-4000;First, diphenylmethane diisocyanate was dissolved in toluene, stirred at 180 r/min, and heated to 80 °C. After mixing uniformly, a small amount of dibutyltin dilaurate was added dropwise, and after mixing, solution A was obtained; The alcohol is dissolved in toluene to obtain solution B, solution B is added dropwise to solution A, and the reaction is continued after the dripping; after the reaction is completed, the product is centrifuged to remove impurities to obtain a prepolymer; the molecular weight of polyethylene glycol is 1000-4000; 溶液A各原料之间的配比是:二苯基甲烷二异氰酸酯与甲苯的质量配比为1:60-1:90;二月桂酸二丁基锡与二苯基甲烷二异氰酸酯的质量配比为1:25-1:20;The ratio between the raw materials of solution A is: the mass ratio of diphenylmethane diisocyanate and toluene is 1:60-1:90; the mass ratio of dibutyltin dilaurate and diphenylmethane diisocyanate is 1 :25-1:20; 溶液B中聚乙二醇和甲苯质量比为1:7-1:10;溶液A中二苯基甲烷二异氰酸酯与溶液B中聚乙二醇的摩尔比为2:1-2.2:1The mass ratio of polyethylene glycol and toluene in solution B is 1:7-1:10; the molar ratio of diphenylmethane diisocyanate in solution A and polyethylene glycol in solution B is 2:1-2.2:1 S2.配制水基反应介质并注入具有温控装置成型槽S2. Prepare a water-based reaction medium and inject it into a molding tank with a temperature control device 将步骤S1制备的预聚体注入纺丝罐,经计量泵从喷丝孔挤出,挤出液流进入成型槽,与水基介质反应成型在10-30℃下反应并固化4-5min形成纤维,引出纤维,用红外线烘干后卷绕,得到智能响应性纤维;The prepolymer prepared in step S1 is injected into the spinning pot, extruded from the spinneret orifice by the metering pump, and the extruded liquid flow enters the molding tank, reacts with the water-based medium, and reacts at 10-30 ° C and solidifies for 4-5min. The fiber is drawn out, dried with infrared rays and then wound to obtain intelligent responsive fiber; 所述水基反应介质是由DMF、NaHCO3或者乙醇中任一种与水组成的混合物,其中DMF或NaHCO3或乙醇与水的质量混合比为10:90-15:85。The water-based reaction medium is a mixture composed of any one of DMF, NaHCO 3 or ethanol and water, wherein the mass mixing ratio of DMF or NaHCO 3 or ethanol and water is 10:90-15:85. 2.根据权利要求1所述的一种水相界面反应纺丝制备智能纤维的方法,其特征在于,溶液B的滴加时间为0.5h,溶液B滴加完毕继续反应时间为1.5-2h。2 . The method for preparing smart fibers by water-phase interface reaction spinning according to claim 1 , wherein the dropwise addition time of solution B is 0.5h, and the continuous reaction time of solution B after dropwise addition is 1.5-2h. 3 . 3.相变调温功能和温度响应性纤维,其特征在于,采用权利要求1所述方法制备。3 . The fiber with phase change temperature regulation function and temperature responsiveness, characterized in that it is prepared by the method of claim 1 .
CN201911347195.6A 2019-12-24 2019-12-24 Method for preparing intelligent fiber through water-phase interface reaction spinning Active CN111058120B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201911347195.6A CN111058120B (en) 2019-12-24 2019-12-24 Method for preparing intelligent fiber through water-phase interface reaction spinning

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201911347195.6A CN111058120B (en) 2019-12-24 2019-12-24 Method for preparing intelligent fiber through water-phase interface reaction spinning

Publications (2)

Publication Number Publication Date
CN111058120A CN111058120A (en) 2020-04-24
CN111058120B true CN111058120B (en) 2022-05-17

Family

ID=70303133

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201911347195.6A Active CN111058120B (en) 2019-12-24 2019-12-24 Method for preparing intelligent fiber through water-phase interface reaction spinning

Country Status (1)

Country Link
CN (1) CN111058120B (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1103565A (en) * 1963-12-20 1968-02-14 Courtaulds Ltd Improvements relating to the production of artificial fibres
CN110230121A (en) * 2019-06-11 2019-09-13 武汉纺织大学 A kind of preparation method of high-ductility polyurethane composite fibre
CN110230117A (en) * 2019-06-11 2019-09-13 武汉纺织大学 A method of improving polyurethane fiber strength and strain

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090093606A1 (en) * 2007-10-09 2009-04-09 The Hong Kong Polytechnic University Shape memory fibers prepared via wet, reaction, dry, melt, and electro spinning
US7976944B2 (en) * 2009-01-02 2011-07-12 The Hong Kong Polytechnic University Temperature-regulating fiber and a method of making the same

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1103565A (en) * 1963-12-20 1968-02-14 Courtaulds Ltd Improvements relating to the production of artificial fibres
CN110230121A (en) * 2019-06-11 2019-09-13 武汉纺织大学 A kind of preparation method of high-ductility polyurethane composite fibre
CN110230117A (en) * 2019-06-11 2019-09-13 武汉纺织大学 A method of improving polyurethane fiber strength and strain

Also Published As

Publication number Publication date
CN111058120A (en) 2020-04-24

Similar Documents

Publication Publication Date Title
CN114481358B (en) Temperature-adjusting fiber and preparation method thereof
CN105019053B (en) One kind can weave phase-change accumulation energy polyster fibre
CN101736619B (en) Cation type reactive polyurethane coloring stabilizer and preparation method thereof
US3635870A (en) Segmented polyurethane elastomers
CN103726127B (en) A kind of black polyurethane urea elastomer adding CNT and preparation method thereof
CN109137113B (en) A kind of phase change temperature regulating viscose fiber with good hygroscopicity and preparation method thereof
CN103952007B (en) A kind of cross-linked modification method of azo dispersion dyes
CN101638471A (en) Method for preparing water-base cation blocked polyisocyanates crosslinking and curing agent
CN102391461A (en) Super-soft polyurethane resin and preparation method and application thereof
CN103450436A (en) Polyurethane resin, and preparation method and application thereof
CN102154727A (en) High-intensity poly(terephthaloyl-p-phenylene diamine) (PPTA) fiber and preparation method thereof
CN101423986A (en) Method for preparing polybenzazole fiber
CN103388188B (en) A kind ofly discarded duds thing is utilized to prepare the method for colored fiber
CN105418887B (en) A kind of anionic polyurethane color fixing agent, preparation method and application for acid dyes
JP2006176772A5 (en)
CN104894684A (en) Woven phase change energy storage polypropylene fiber
CN105838334A (en) Preparing method for heat storing and temperature adjusting phase change microcapsules
CN101545207A (en) Anti-pilling finishing agent for pure cotton knitted fabrics and preparation method thereof
CN111058120B (en) Method for preparing intelligent fiber through water-phase interface reaction spinning
CN105017862B (en) A kind of high performance pigments ink and preparation method thereof
CN110627965B (en) A kind of photochromic waterborne polyurethane coating agent and preparation method thereof
WO2022032852A1 (en) Preparation method of natural dye color masterbatch
CN104178843A (en) A kind of phase change blended fiber and its manufacturing method
CN111074628B (en) In-situ online water chain extension polyurethane phase change temperature regulation functional fabric and preparation method thereof
CN115305722B (en) Photochromic fabric and preparation method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant