CN103526335B - A kind of preparation method of fluorine-containing PBT-PBT core-skin composite fiber - Google Patents
A kind of preparation method of fluorine-containing PBT-PBT core-skin composite fiber Download PDFInfo
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- 229910052731 fluorine Inorganic materials 0.000 title claims abstract description 100
- 239000011737 fluorine Substances 0.000 title claims abstract description 96
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- 239000000835 fiber Substances 0.000 title claims abstract description 64
- 239000002131 composite material Substances 0.000 title claims abstract description 62
- 238000002360 preparation method Methods 0.000 title claims abstract description 37
- 238000005886 esterification reaction Methods 0.000 claims abstract description 66
- 238000006068 polycondensation reaction Methods 0.000 claims abstract description 65
- 239000000463 material Substances 0.000 claims abstract description 43
- WFNRNCNCXRGUKN-UHFFFAOYSA-N 2,3,5,6-tetrafluoroterephthalic acid Chemical compound OC(=O)C1=C(F)C(F)=C(C(O)=O)C(F)=C1F WFNRNCNCXRGUKN-UHFFFAOYSA-N 0.000 claims abstract description 29
- 238000009987 spinning Methods 0.000 claims abstract description 21
- 230000032050 esterification Effects 0.000 claims abstract description 19
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 claims abstract description 18
- 125000001153 fluoro group Chemical group F* 0.000 claims abstract description 10
- 239000003112 inhibitor Substances 0.000 claims abstract description 10
- 239000002994 raw material Substances 0.000 claims abstract description 9
- 238000006243 chemical reaction Methods 0.000 claims description 33
- 239000010410 layer Substances 0.000 claims description 21
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- VXUYXOFXAQZZMF-UHFFFAOYSA-N titanium(IV) isopropoxide Chemical compound CC(C)O[Ti](OC(C)C)(OC(C)C)OC(C)C VXUYXOFXAQZZMF-UHFFFAOYSA-N 0.000 claims description 8
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- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 claims description 6
- WVLBCYQITXONBZ-UHFFFAOYSA-N trimethyl phosphate Chemical compound COP(=O)(OC)OC WVLBCYQITXONBZ-UHFFFAOYSA-N 0.000 claims description 4
- XZZNDPSIHUTMOC-UHFFFAOYSA-N triphenyl phosphate Chemical group C=1C=CC=CC=1OP(OC=1C=CC=CC=1)(=O)OC1=CC=CC=C1 XZZNDPSIHUTMOC-UHFFFAOYSA-N 0.000 claims description 4
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- 229910052814 silicon oxide Inorganic materials 0.000 claims description 3
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- ISKQADXMHQSTHK-UHFFFAOYSA-N [4-(aminomethyl)phenyl]methanamine Chemical compound NCC1=CC=C(CN)C=C1 ISKQADXMHQSTHK-UHFFFAOYSA-N 0.000 claims description 2
- 125000004494 ethyl ester group Chemical group 0.000 claims 1
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- JMXKSZRRTHPKDL-UHFFFAOYSA-N titanium ethoxide Chemical compound [Ti+4].CC[O-].CC[O-].CC[O-].CC[O-] JMXKSZRRTHPKDL-UHFFFAOYSA-N 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
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- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
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- PEVRKKOYEFPFMN-UHFFFAOYSA-N 1,1,2,3,3,3-hexafluoroprop-1-ene;1,1,2,2-tetrafluoroethene Chemical compound FC(F)=C(F)F.FC(F)=C(F)C(F)(F)F PEVRKKOYEFPFMN-UHFFFAOYSA-N 0.000 description 1
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- ZFVMWEVVKGLCIJ-UHFFFAOYSA-N bisphenol AF Chemical compound C1=CC(O)=CC=C1C(C(F)(F)F)(C(F)(F)F)C1=CC=C(O)C=C1 ZFVMWEVVKGLCIJ-UHFFFAOYSA-N 0.000 description 1
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- VNGOYPQMJFJDLV-UHFFFAOYSA-N dimethyl benzene-1,3-dicarboxylate Chemical compound COC(=O)C1=CC=CC(C(=O)OC)=C1 VNGOYPQMJFJDLV-UHFFFAOYSA-N 0.000 description 1
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- Multicomponent Fibers (AREA)
Abstract
本发明涉及一种含氟PBT-PBT皮芯复合纤维的制备方法,包括皮层材料含氟PBT的制备和皮芯复合纤维的制备。含氟PBT是采用四氟对苯二甲酸和1,4-丁二醇作为原料,加入抑制剂,在适当的条件下进行酯化反应和缩聚反应得到的。然后以含氟PBT为皮、PBT为芯,采取合适的复合纺丝工艺制备得到皮芯复合纤维。本发明所得的含氟PBT具有良好的热稳定性及可加工性,氟原子的引入,提高了其憎水憎油性能。复合纺丝制得的纤维不仅具备PBT的良好力学性能,而且还有着良好的耐污性能,同时又大大节约了成本,使其在防水服,耐脏的工作服以及某些特殊行业的工作服制造中有巨大的前景。The invention relates to a preparation method of fluorine-containing PBT-PBT sheath-core composite fiber, which comprises the preparation of fluorine-containing PBT as a skin layer material and the preparation of the skin-core composite fiber. Fluorine-containing PBT is obtained by using tetrafluoroterephthalic acid and 1,4-butanediol as raw materials, adding inhibitors, and performing esterification and polycondensation reactions under appropriate conditions. Then use the fluorine-containing PBT as the sheath and the PBT as the core, and adopt a suitable composite spinning process to prepare the sheath-core composite fiber. The fluorine-containing PBT obtained by the invention has good thermal stability and processability, and the introduction of fluorine atoms improves its water-repellent and oil-repellent properties. The fiber made by composite spinning not only has good mechanical properties of PBT, but also has good stain resistance, and at the same time greatly saves costs, making it suitable for waterproof clothing, dirty work clothes and work clothes in some special industries. There are huge prospects.
Description
技术领域technical field
本发明涉及一种含氟PBT-PBT皮芯复合纤维的制备方法,包括皮层材料含氟PBT的制备和皮芯复合纤维的制备。特别是涉及一种以聚四氟对苯二甲酸丁二醇酯为皮层含氟PBT材料,以PBT为芯层材料的皮芯复合纤维的制备方法。The invention relates to a preparation method of fluorine-containing PBT-PBT sheath-core composite fiber, which comprises the preparation of fluorine-containing PBT as a skin layer material and the preparation of the skin-core composite fiber. In particular, it relates to a preparation method of a skin-core composite fiber with polytetrafluorobutylene terephthalate as the fluorine-containing PBT material in the skin layer and PBT as the core layer material.
背景技术Background technique
随着技术的发展和进步,人们要求的不断提升,单一材料的纤维已经不能很好的满足人们的需求,各种各样的复合纤维就应运而生。它们有着单一材料的纤维所不能同时具备的性能,兼具多种纤维的优点,能够提供更好的性能,其中,皮芯复合纤维就是一种很好的复合纤维。这种纤维不仅能够具有皮层纤维所具备的部分性能,还具有芯层纤维的部分性能,合理的性能组合就能得到性能优良的皮芯复合纤维,制备工艺简单,同时能减少皮层材料的用量,节约成本。With the development and progress of technology and the continuous improvement of people's requirements, the fiber of a single material can no longer meet people's needs very well, and various composite fibers have emerged as the times require. They have properties that cannot be possessed by fibers of a single material at the same time. They have the advantages of multiple fibers and can provide better performance. Among them, the skin-core composite fiber is a good composite fiber. This kind of fiber can not only have some properties of the skin fiber, but also have some properties of the core fiber. A reasonable combination of properties can obtain a skin-core composite fiber with excellent performance. The preparation process is simple, and at the same time, the amount of skin material can be reduced. save costs.
聚酯是目前人类使用最为广泛的合成高聚物之一,早在二十世纪40年代就合成出了对苯二甲酸乙二醇酯(PET),并发现其具有优异的性能,而广泛的应用于纺织、包装、医疗卫生、汽车、电子电器、安全防护、环境保护等领域。聚对苯二甲酸丁二醇酯(PBT)是一种结晶性线型饱和聚酯,具有耐高温、耐湿、电绝缘性能好、耐油、耐化学腐蚀、成型快等特点。其在工业中的一些应用实例显示出其在某些方面无可替代的优越性,现它已成为继聚酰胺(PA)、聚碳酸酯(PC)、聚甲醛(POM)和改性聚苯醚(MPPO)之后的第五大通用工程塑料,广泛应用于汽车工业、电子电器工业、食品医疗器械、包装材料、环境工程、通讯设备、运动休闲器械等。随着对PBT结构和性能的研究不断深化,不仅开发出不同级别、不同类型的工程塑料,如高冲击的、耐热的、阻燃的等,而且使它在合成纤维方面的应用越来越受重视。PBT纤维弹性优越,手感柔软,染色方便,兼有涤纶、锦纶、氨纶三者的优点。随着社会的进步,人民生活水平的提高,对聚酯纤维的差别化、功能化需要越来越高。因此聚酯的改性也变得尤为的重要,聚酯改性目的除了对普通聚酯性能进行优化外,主要是通过改性手段赋予新型聚酯差别化的功能性特征。例如:抗静电、阻燃、吸湿排汗、防污防臭等。目前,聚酯主要新品种有:抗静电聚酯、高强耐磨聚酯、仿棉超软聚酯、超疏水性聚酯、抗污聚酯等。目前,通过在聚合物中引入氟原子,从而改善材料的表面性能,如疏水疏油性及防污性等,以及赋予聚酯材料各种功能。由于含氟聚合物通常具有低表面能、低摩擦系数和不粘附性,灰尘污物难于附着等特性,因此含氟聚合物的抗污耐磨性好。而当前含氟聚合物以氟代烯烃类聚合物为主(例如:聚四氟乙烯、聚偏氟乙烯、全氟乙烯丙烯共聚物、乙烯-四氟乙烯共聚物等);含氟聚氨酯、含氟聚醚、含氟聚酯等的研究则相对滞后。许多学者对含氟化合物改性聚酯进行了研究,并取得了一定的成果。目前含氟化合物改性聚酯的方式主要是通过加入含氟封端剂,或者加入含氟二元醇、含氟二元酸等含氟化合物作为第三单体来改性聚酯。中国专利CN101139434A中采用含氟封端剂的加入,间苯二甲酸二甲酯和丁二醇采用酯交换法,加入含氟封端剂N-羟乙基全氟辛酰胺,制备出了含氟量低而耐沾污性能好的聚酯材料。胡娟(胡娟.含氟聚酯和光刻胶波导材料的分子设计与性能研究[D].硕士论文,吉林:吉林大学,2007.)利用分子设计的原理,通过添加含氟二元醇共聚的方式,将对苯二甲酰氯、六氟双酚A和含氟辛二醇三元共聚合成出了新型高含氟量的聚酯。该聚酯具有优异的性能而被应用于光波导材料。然而,将这些含有氟元素的聚酯应用于纺织及包装材料中有一定的局限性,主要问题在于现有技术的含有氟元素的聚酯分子量低,不能满足纺丝和成膜的要求;现有技术目前主要是通过织物的含氟后整理方式来赋予其防水防污功能,而这类方法最大的缺点在于难以解决时效性、耐久性及耐磨性等问题,并且费时费力。Polyester is currently one of the most widely used synthetic polymers. As early as the 1940s, polyethylene terephthalate (PET) was synthesized and found to have excellent properties. It is widely used in textile, packaging, medical and health, automobile, electronic appliances, safety protection, environmental protection and other fields. Polybutylene terephthalate (PBT) is a crystalline linear saturated polyester, which has the characteristics of high temperature resistance, humidity resistance, good electrical insulation performance, oil resistance, chemical corrosion resistance, and fast molding. Some of its application examples in the industry have shown its irreplaceable superiority in some aspects, and now it has become the next-generation polyamide (PA), polycarbonate (PC), polyoxymethylene (POM) and modified polyphenylene The fifth largest general-purpose engineering plastic after ether (MPPO), it is widely used in the automobile industry, electronic and electrical industry, food and medical equipment, packaging materials, environmental engineering, communication equipment, sports and leisure equipment, etc. With the continuous deepening of research on the structure and performance of PBT, not only have different grades and types of engineering plastics been developed, such as high-impact, heat-resistant, flame-retardant, etc., but also make its application in synthetic fibers more and more valued. PBT fiber has excellent elasticity, soft hand feeling, easy dyeing, and has the advantages of polyester, nylon and spandex. With the progress of society and the improvement of people's living standards, the demand for the differentiation and functionalization of polyester fibers is getting higher and higher. Therefore, the modification of polyester has become particularly important. The purpose of polyester modification is not only to optimize the performance of ordinary polyester, but also to endow new polyester with differentiated functional characteristics through modification means. For example: antistatic, flame retardant, moisture wicking, antifouling and deodorant, etc. At present, the main new varieties of polyester are: antistatic polyester, high-strength wear-resistant polyester, cotton-like supersoft polyester, superhydrophobic polyester, antifouling polyester, etc. At present, by introducing fluorine atoms into polymers, the surface properties of materials, such as hydrophobicity, oil repellency and anti-fouling properties, etc. are improved, and various functions are endowed to polyester materials. Because fluoropolymers usually have low surface energy, low coefficient of friction and non-adhesion, dust and dirt are difficult to adhere to, etc., so fluoropolymers have good anti-fouling and abrasion resistance. The current fluorine-containing polymers are mainly fluoroolefin polymers (for example: polytetrafluoroethylene, polyvinylidene fluoride, perfluoroethylene propylene copolymer, ethylene-tetrafluoroethylene copolymer, etc.); Research on fluoropolyethers and fluoropolyesters is relatively lagging behind. Many scholars have conducted research on fluorine-containing compound-modified polyester, and achieved certain results. At present, polyesters are modified by fluorine-containing compounds mainly by adding fluorine-containing end-capping agents, or by adding fluorine-containing diols, fluorine-containing dibasic acids and other fluorine-containing compounds as the third monomer to modify polyester. In Chinese patent CN101139434A, the addition of fluorine-containing end-capping agent is adopted. Dimethyl isophthalate and butanediol are transesterified, and fluorine-containing end-capping agent N-hydroxyethyl perfluorooctylamide is added to prepare a fluorine-containing end-capping agent. Polyester material with low weight and good stain resistance. Hu Juan (Hu Juan. Molecular design and performance research of fluorine-containing polyester and photoresist waveguide materials [D]. Master's thesis, Jilin: Jilin University, 2007.) Using the principle of molecular design, by adding fluorine-containing diols In the way of copolymerization, terephthaloyl chloride, hexafluorobisphenol A and fluorine-containing octanediol are terpolymerized to form a new type of polyester with high fluorine content. The polyester has excellent properties and is applied to optical waveguide materials. However, the application of these fluorine-containing polyesters to textiles and packaging materials has certain limitations. The main problem is that the prior art fluorine-containing polyesters have low molecular weight and cannot meet the requirements of spinning and film formation; At present, the existing technology mainly uses fluorine-containing finishing methods to endow fabrics with waterproof and anti-fouling functions, but the biggest disadvantage of this method is that it is difficult to solve the problems of timeliness, durability and wear resistance, and it is time-consuming and labor-intensive.
因此,开发新型含氟聚酯皮芯复合纤维用于纺织及包装材料的超疏水、憎水憎油、防污性能的改性,必将具有重要的理论意义和应用价值。在防水服,耐脏的工作服以及某些特殊行业的工作服制造中有巨大的前景。Therefore, the development of new fluorine-containing polyester sheath-core composite fibers for the modification of superhydrophobic, hydrophobic, oil-repellent, and antifouling properties of textile and packaging materials will have important theoretical significance and application value. It has great prospects in the manufacture of waterproof clothing, dirt-resistant work clothes and work clothes in some special industries.
发明内容Contents of the invention
本发明的目的是提供一种含氟PBT-PBT皮芯复合纤维的制备方法,包括皮层材料含氟PBT的制备和皮芯复合纤维的制备。其中含氟PBT是指聚四氟对苯二甲酸丁二醇酯。本发明所述的含氟PBT在聚合物的主链上引入了氟原子,并且制备出的含氟PBT切片可以直接用于纺丝,能够赋予含氟PBT纤维永久的憎水憎油性能,解决传统PBT纤维憎水憎油改性费时费力的问题。同时,采用复合纺丝法制备出以含氟PBT为皮层材料、PBT为芯层材料的皮芯复合纤维,不仅赋予了皮芯复合纤维良好的憎水憎油性能,还大大的节省了成本。The purpose of the present invention is to provide a method for preparing fluorine-containing PBT-PBT sheath-core composite fibers, including the preparation of fluorine-containing PBT as a skin layer material and the preparation of sheath-core composite fibers. Among them, fluorine-containing PBT refers to polytetrafluorobutylene terephthalate. The fluorine-containing PBT described in the present invention introduces fluorine atoms into the main chain of the polymer, and the prepared fluorine-containing PBT chips can be directly used for spinning, which can endow the fluorine-containing PBT fibers with permanent water and oil repellency, and solve the problem of The traditional PBT fiber hydrophobic and oil-repellent modification is time-consuming and labor-intensive. At the same time, the composite spinning method is used to prepare the skin-core composite fiber with fluorine-containing PBT as the skin material and PBT as the core material, which not only endows the skin-core composite fiber with good hydrophobic and oil-repellent properties, but also greatly saves the cost.
本发明的一种含氟PBT-PBT皮芯复合纤维的制备方法,皮层材料为含氟PBT,芯层材料为PBT;所述含氟PBT为聚四氟对苯二甲酸丁二醇酯,其结构通式为A preparation method of fluorine-containing PBT-PBT sheath-core composite fiber of the present invention, the material of the skin layer is PBT containing fluorine, and the material of the core layer is PBT; the PBT containing fluorine is polytetrafluorobutylene terephthalate, and The general structural formula is
其中n=70~150;所述含氟PBT-PBT皮芯复合纤维的皮层和芯层的截面积之比为2~5:5。Where n=70-150; the ratio of the cross-sectional area of the skin layer to the core layer of the fluorine-containing PBT-PBT sheath-core composite fiber is 2-5:5.
如上所述的一种含氟PBT-PBT皮芯复合纤维,所述含氟PBT-PBT皮芯复合纤维的单丝纤度为1~15dtex;包括含氟PBT的制备方法和皮芯复合纤维的制备方法,具体步骤为:A fluorine-containing PBT-PBT sheath-core composite fiber as described above, the monofilament fineness of the fluorine-containing PBT-PBT sheath-core composite fiber is 1 to 15 dtex; including the preparation method of fluorine-containing PBT and the preparation of the skin-core composite fiber method, the specific steps are:
1.含氟PBT的制备方法1. Preparation method of fluorine-containing PBT
分为酯化反应和缩聚反应两步;具体步骤为:It is divided into two steps of esterification reaction and polycondensation reaction; the specific steps are:
所述酯化反应:Described esterification reaction:
采用四氟对苯二甲酸和1,4-丁二醇作为原料,加入抑制剂,所述的抑制剂的加入量为所述四氟对苯二甲酸重量的0.01%~0.05%,配成均匀浆料后进行酯化反应;酯化反应在氮气氛围中加压,压力控制在小于绝对压力1KPa下进行,温度在160~220℃,时间为2~3小时,酯化水馏出量达到理论值的90%以上为酯化反应终点;Adopt tetrafluoroterephthalic acid and 1,4-butanediol as raw materials, add inhibitor, the addition amount of described inhibitor is 0.01%~0.05% of the weight of described tetrafluoroterephthalic acid, is made into uniform Esterification reaction is carried out after the slurry; the esterification reaction is pressurized in a nitrogen atmosphere, the pressure is controlled at less than 1KPa of absolute pressure, the temperature is 160-220°C, the time is 2-3 hours, and the distilled amount of esterification water reaches the theoretical level. More than 90% of the value is the end point of the esterification reaction;
所述抑制剂为氧化镁、氧化硅、氧化钙、氧化锌和氧化锰中的一种;由于所用的二元羧酸的苯环上存在氟原子,氟原子的电负性大,在酯化反应阶段氟原子的共轭效应使得二元羧酸的酸性增强,同时导致二元羧酸中羧基的活性增大,使得反应速度加快,而反应速度增加容易使副反应产生,这些副反应产物对后续的缩聚反应有较大的影响,特别是生成烯烃和醛的封端产物,制约了产物分子量的增加;从实验结果来看,如果不加入抑制剂,合成的聚酯分子量偏低,不能满足纺丝和成膜的需求;抑制剂的加入用于控制酯化反应阶段的速度,减少了副反应,提高了产物的分子量,使得满足纺丝要求。Described suppressor is a kind of in magnesium oxide, silicon oxide, calcium oxide, zinc oxide and manganese oxide; Because there is fluorine atom on the benzene ring of dibasic carboxylic acid used, the electronegativity of fluorine atom is big, in esterification The conjugation effect of the fluorine atom in the reaction stage increases the acidity of the dicarboxylic acid, and at the same time increases the activity of the carboxyl group in the dicarboxylic acid, which speeds up the reaction rate, and the increase in the reaction rate is likely to cause side reactions. The follow-up polycondensation reaction has a greater impact, especially the generation of end-capped products of olefins and aldehydes, which restricts the increase in the molecular weight of the product; from the experimental results, if no inhibitor is added, the molecular weight of the synthesized polyester is low, which cannot meet the requirements. Spinning and film-forming requirements; the addition of inhibitors is used to control the speed of the esterification reaction stage, reducing side reactions, increasing the molecular weight of the product, and meeting the spinning requirements.
通常,聚酯酯化过程中是通过所用的二元羧酸电离出的氢离子作为酯化反应的催化剂,进行自催化反应,通过调节酯化反应的温度、压力以及小分子的排出来控制其酯化的速率,然而进行酯化反应的前提是要在一定的反应温度及压力下才可以进行酯化反应。温度过低或者压力不够的情况下,酯化反应不能够进行或者速度极慢,从而影响后续的工艺。若酯化反应中的小分子未能及时排出容易引起不必要的副反应。合成过程中,由于氟的共轭效应,在酯化反应阶段氟原子使得二元羧酸的酸性增强,同时导致二元羧酸中羧基的活性增大,使得反应速度加快,副反应增多,难以控制,进而影响产物分子量的增长,故加入抑制剂,即通过选择所用金属氧化物来调节。所述的金属氧化物可以按如下两种方式解离:Usually, in the polyester esterification process, the hydrogen ion ionized by the dicarboxylic acid used is used as a catalyst for the esterification reaction to carry out a self-catalyzed reaction, and the esterification reaction is controlled by adjusting the temperature, pressure and discharge of small molecules. However, the premise of the esterification reaction is that the esterification reaction can only be carried out under a certain reaction temperature and pressure. When the temperature is too low or the pressure is not enough, the esterification reaction cannot proceed or the speed is extremely slow, thereby affecting the subsequent process. If the small molecules in the esterification reaction are not discharged in time, it is easy to cause unnecessary side reactions. During the synthesis process, due to the conjugation effect of fluorine, the fluorine atom increases the acidity of the dicarboxylic acid in the esterification reaction stage, and at the same time increases the activity of the carboxyl group in the dicarboxylic acid, which makes the reaction speed faster and the side reactions increase. Control, and then affect the growth of the molecular weight of the product, so the addition of inhibitors is adjusted by selecting the metal oxide used. The metal oxide can be dissociated in the following two ways:
这里M为金属离子,如果M的电负性相当大,对氧离子的电子对有较强的吸引力,那么就能使O—H键减弱,有利于反应离解;相反,如果M的电负性小,那么就将生成碱中心。M—O—H和两性化合物相似,当有碱性物质存在时,反应将按酸式电离的方式进行;而当酸性物质存在时,则按碱式电离的方式进行。从酸式电离方式和碱式电离方式中逆反应的M-O-和M+可见,M+作为酸性中心,其强度仅和金属离子的电负性有直接的关系,而M-O-中的O离子作为碱中心的强度则和氧上的负电荷密度有关,负电荷密度愈大,强度也愈大。可见氧离子上的负电荷密度与金属离子电负性有着密切的关系,金属离子电负性越小,负电荷密度就越大。这样一来,金属氧化物的酸性以及碱性就都和金属离子的电负性联系起来了,金属离子的电负性大的氧化物主要是酸性,而电负性小的则是碱性。Here M is a metal ion. If the electronegativity of M is quite large, it has a strong attraction to the electron pairs of oxygen ions, which can weaken the O—H bond and facilitate the reaction dissociation; on the contrary, if the electronegativity of M If the sex is small, then the base center will be formed. M—O—H is similar to amphoteric compounds. When alkaline substances exist, the reaction will proceed in the form of acid ionization; when acidic substances exist, the reaction will proceed in the form of basic ionization. From the reverse reactions of MO - and M + in the acid ionization mode and base ionization mode, it can be seen that M + acts as an acidic center, and its strength is only directly related to the electronegativity of the metal ion, while the O ion in MO - acts as a base The intensity of the center is related to the negative charge density on the oxygen, the greater the negative charge density, the greater the intensity. It can be seen that the negative charge density on oxygen ions is closely related to the electronegativity of metal ions, the smaller the electronegativity of metal ions, the greater the negative charge density. In this way, the acidity and alkalinity of metal oxides are related to the electronegativity of metal ions. The oxides with high electronegativity of metal ions are mainly acidic, while those with low electronegativity are alkaline.
所述缩聚反应:Described polycondensation reaction:
包括缩聚反应低真空阶段和缩聚反应高真空阶段;Including the low vacuum stage of polycondensation reaction and the high vacuum stage of polycondensation reaction;
所述缩聚反应低真空阶段,在酯化产物中加入催化剂和稳定剂,在负压的条件下开始缩聚反应,所述负压是指绝对压力500Pa以下,温度控制在260~270℃,反应时间为40~60分钟;In the low-vacuum stage of the polycondensation reaction, a catalyst and a stabilizer are added to the esterification product, and the polycondensation reaction starts under negative pressure. 40-60 minutes;
所述缩聚反应高真空阶段,经所述缩聚反应低真空阶段后,继续抽真空,使反应压力降至绝对压力小于100Pa,反应温度控制在270~275℃,反应时间3~4小时。缩聚反应以反应釜搅拌电机功率或在线粘度计读数为准判断反应终点。In the high vacuum stage of the polycondensation reaction, after the low vacuum stage of the polycondensation reaction, the vacuum is continued to reduce the reaction pressure to an absolute pressure of less than 100 Pa, the reaction temperature is controlled at 270-275°C, and the reaction time is 3-4 hours. The polycondensation reaction is based on the power of the stirring motor of the reactor or the reading of the online viscometer to judge the end point of the reaction.
2.含氟PBT-PBT皮芯复合纤维的制备方法2. Preparation method of fluorine-containing PBT-PBT sheath-core composite fiber
将所述含氟PBT作为皮层材料,PBT作为芯层材料,进行皮芯复合纺丝,纺丝温度为270-280℃,卷绕速度控制在2700~3200m/min。The fluorine-containing PBT is used as the skin layer material, and the PBT is used as the core layer material to carry out sheath-core composite spinning, the spinning temperature is 270-280° C., and the winding speed is controlled at 2700-3200 m/min.
作为优选的技术方案:As a preferred technical solution:
如上所述的一种含氟PBT-PBT皮芯复合纤维的制备方法,所述的丁二醇与四氟对苯二甲酸的摩尔比为1.4~2.0:1。According to the method for preparing fluorine-containing PBT-PBT sheath-core composite fibers, the molar ratio of butanediol to tetrafluoroterephthalic acid is 1.4-2.0:1.
如上所述的一种含氟PBT-PBT皮芯复合纤维的制备方法,所述的催化剂选自钛酸四丁酯、钛酸四异丙酯、钛酸四乙酯、醋酸亚锡、二醋酸二丁基锡中的一种,催化剂用量为所述四氟对苯二甲酸重量的0.01%~0.05%。A kind of preparation method of fluorine-containing PBT-PBT sheath-core composite fiber as mentioned above, described catalyst is selected from tetrabutyl titanate, tetraisopropyl titanate, tetraethyl titanate, stannous acetate, diacetic acid One of dibutyltin, the amount of the catalyst used is 0.01% to 0.05% of the weight of the tetrafluoroterephthalic acid.
如上所述的一种含氟PBT-PBT皮芯复合纤维的制备方法,所述的稳定剂选自磷酸三苯酯、磷酸三甲酯和亚磷酸三甲酯中的一种,稳定剂用量为所述四氟对苯二甲酸重量的0.01%~0.05%。A kind of preparation method of fluorine-containing PBT-PBT sheath-core composite fiber as mentioned above, described stabilizer is selected from a kind of in triphenyl phosphate, trimethyl phosphate and trimethyl phosphite, and stabilizer consumption is 0.01%-0.05% of the weight of the tetrafluoroterephthalic acid.
本发明的酯化反应阶段中,反应终点由酯化中实际产生的水馏出量达到理论值90%以上来掌握。理论值为按化学反应方程式完全反应时所得水的馏出量。由于酯化反应本身为可逆反应,再者原料在输送管道中会有残留,并且随着反应的进行,体系的粘度增加,会导致酯化反应产生的水难以从中排出。In the esterification reaction stage of the present invention, the end point of the reaction is determined by the amount of water distilled out actually produced in the esterification reaching more than 90% of the theoretical value. The theoretical value is the distilled amount of water obtained when the chemical reaction equation is completely reacted. Since the esterification reaction itself is a reversible reaction, and the raw materials will remain in the pipeline, and as the reaction progresses, the viscosity of the system will increase, making it difficult to discharge the water produced by the esterification reaction.
本发明的缩聚反应高真空阶段中,反应终点由反应釜搅拌器马达功率及在线粘度计算值达到设定的数值来掌握。不同的装置其反应釜搅拌器马达功率及在线粘度计算值的设定数值不一定相同,设定数值的确定可以通过对聚酯切片的分析来获得。In the high vacuum stage of the polycondensation reaction of the present invention, the end point of the reaction is determined by the calculated value of the motor power of the reactor stirrer and the online viscosity reaching the set value. The set values of the motor power of the reactor agitator and the online viscosity calculation value of different devices are not necessarily the same, and the determination of the set values can be obtained by analyzing the polyester chips.
本发明所得的含氟PBT由于氟原子的引入,提高了PBT材料的憎水憎油性能,所以以本发明中的含氟PBT为皮层,PBT为芯层的皮芯复合纤维不仅有着良好的力学性能,还有着良好的永久耐油污性能,且成本大大降低,使其在防水服,耐脏的工作服以及某些特殊行业的工作服制造中有巨大的前景。The fluorine-containing PBT obtained in the present invention improves the hydrophobic and oil-repellent properties of the PBT material due to the introduction of fluorine atoms, so the skin-core composite fiber with the fluorine-containing PBT in the present invention as the skin layer and PBT as the core layer not only has good mechanical properties performance, and good permanent oil resistance, and the cost is greatly reduced, so that it has great prospects in the manufacture of waterproof clothing, dirt-resistant work clothes and work clothes in some special industries.
有益效果:Beneficial effect:
1、制得的PBT含氟原子,由于氟的强电负性,高的C-F键能以及对碳链的屏蔽保护作用使得合成出的共聚酯除了进一步提升传统聚酯的性能外,还降低了聚酯材料的表面能,使材料有着永久性的憎水憎油,抗油污性能。1. The prepared PBT contains fluorine atoms. Due to the strong electronegativity of fluorine, the high C-F bond energy and the shielding effect on the carbon chain, the synthesized copolyester not only further improves the performance of traditional polyester, but also reduces Improve the surface energy of the polyester material, so that the material has a permanent water-repellent, oil-repellent, and oil-resistant properties.
2、含氟PBT酯化过程中通过加抑制剂可以控制酯化反应的速度,减少副反应的产生。2. During the esterification process of fluorine-containing PBT, the speed of the esterification reaction can be controlled by adding inhibitors to reduce the occurrence of side reactions.
3、所得含氟PBT切片可以直接纺丝。3. The resulting fluorine-containing PBT chips can be directly spun.
4、所得含氟PBT具有良好的热稳定性及可加工性。4. The obtained fluorine-containing PBT has good thermal stability and processability.
5、采用含氟PBT为皮层材料、PBT为芯层材料制得的皮芯复合纤维有着良好的力学性能和永久耐油污性能,而且相比单独使用含氟PBT制备的纤维来说,成本大大降低,因而有着更好的应用价值。5. The skin-core composite fiber made of fluorine-containing PBT as the skin material and PBT as the core material has good mechanical properties and permanent oil resistance, and compared with fibers prepared by using fluorine-containing PBT alone, the cost is greatly reduced , so it has better application value.
具体实施方式detailed description
下面结合具体实施方式,进一步阐述本发明。应理解,这些实施例仅用于说明本发明而不用于限制本发明的范围。此外应理解,在阅读了本发明讲授的内容之后,本领域技术人员可以对本发明作各种改动或修改,这些等价形式同样落于本申请所附权利要求书所限定的范围。The present invention will be further described below in combination with specific embodiments. It should be understood that these examples are only used to illustrate the present invention and are not intended to limit the scope of the present invention. In addition, it should be understood that after reading the teachings of the present invention, those skilled in the art can make various changes or modifications to the present invention, and these equivalent forms also fall within the scope defined by the appended claims of the present application.
本发明的一种含氟PBT-PBT皮芯复合纤维,皮层材料为含氟PBT,芯层材料为PBT;所述含氟PBT为聚四氟对苯二甲酸丁二醇酯,其结构通式为A fluorine-containing PBT-PBT sheath-core composite fiber of the present invention, the material of the skin layer is PBT containing fluorine, and the material of the core layer is PBT; the PBT containing fluorine is polytetrafluorobutylene terephthalate, and its general structure is for
其中n=70~150。Wherein n=70~150.
如上所述的一种含氟PBT-PBT皮芯复合纤维,所述含氟PBT-PBT皮芯复合纤维的皮层和芯层的截面积之比为2~5:5。According to the above-mentioned fluorine-containing PBT-PBT sheath-core composite fiber, the ratio of the cross-sectional area of the skin layer to the core layer of the fluorine-containing PBT-PBT sheath-core composite fiber is 2-5:5.
如上所述的一种含氟PBT-PBT皮芯复合纤维,所述含氟PBT-PBT皮芯复合纤维的单丝纤度为1~15dtex。A fluorine-containing PBT-PBT sheath-core composite fiber as described above, wherein the monofilament fineness of the fluorine-containing PBT-PBT sheath-core composite fiber is 1-15 dtex.
实施例1Example 1
1.含氟PBT聚酯的制备方法,分为酯化反应和缩聚反应两步。具体步骤为:1. The preparation method of fluorine-containing PBT polyester is divided into two steps of esterification reaction and polycondensation reaction. The specific steps are:
所述酯化反应:Described esterification reaction:
采用摩尔比为1.4:1的1,4-丁二醇和四氟对苯二甲酸作为原料,同时加入四氟对苯二甲酸重量的0.01%的氧化镁,配成均匀浆料后进行酯化反应;酯化反应在氮气氛围中,压力控制在1KPa以下,温度控制在220℃,酯化水馏出量达到理论值的90%为酯化反应终点。Use 1,4-butanediol and tetrafluoroterephthalic acid with a molar ratio of 1.4:1 as raw materials, and add 0.01% magnesium oxide based on the weight of tetrafluoroterephthalic acid at the same time, make a uniform slurry and carry out esterification reaction ; The esterification reaction is carried out in a nitrogen atmosphere, the pressure is controlled below 1KPa, the temperature is controlled at 220°C, and the esterification water distillate reaches 90% of the theoretical value, which is the end point of the esterification reaction.
所述缩聚反应:Described polycondensation reaction:
包括缩聚反应低真空阶段和缩聚反应高真空阶段:Including low vacuum stage of polycondensation reaction and high vacuum stage of polycondensation reaction:
所述缩聚反应低真空阶段,在酯化产物中加入四氟对苯二甲酸重量的0.01%的催化剂钛酸四丁酯和四氟对苯二甲酸重量的0.01%的稳定剂磷酸三苯酯,在负压的条件下开始缩聚反应,所述负压是指绝对压力小于500Pa,温度控制在265℃,反应时间为60分钟。In the low-vacuum stage of the polycondensation reaction, 0.01% of the weight of tetrafluoroterephthalic acid is added to the esterified product. The catalyst tetrabutyl titanate and the stabilizer triphenyl phosphate of 0.01% of the weight of tetrafluoroterephthalic acid are added, The polycondensation reaction starts under the condition of negative pressure, said negative pressure means that the absolute pressure is less than 500 Pa, the temperature is controlled at 265° C., and the reaction time is 60 minutes.
所述缩聚反应高真空阶段,经所述缩聚反应低真空阶段后,继续抽真空,使反应压力降至绝对压力小于100Pa,反应温度控制在270℃,反应时间4小时。缩聚反应以反应釜搅拌电机功率或在线粘度计读数为准判断反应终点。当聚合物粘度达到所需值时出料,经铸带、冷却、切粒,即得到含氟PBT聚酯切片。In the high vacuum stage of the polycondensation reaction, after the low vacuum stage of the polycondensation reaction, the vacuum is continued to reduce the reaction pressure to an absolute pressure of less than 100 Pa, the reaction temperature is controlled at 270° C., and the reaction time is 4 hours. The polycondensation reaction is based on the power of the stirring motor of the reactor or the reading of the online viscometer to judge the end point of the reaction. When the viscosity of the polymer reaches the desired value, the material is discharged, and after casting, cooling and pelletizing, the fluorine-containing PBT polyester chips are obtained.
2.皮芯复合纤维的制备:将所述含氟PBT作为皮层材料,PBT作为芯层材料,进行皮芯复合纺丝,皮层和芯层的横截面积之比为2:5,纺丝温度为270℃,卷绕速度控制在2700m/min,所得含氟PBT-PBT皮芯复合纤维的单丝纤度为1dtex。2. Preparation of skin-core composite fiber: use the fluorine-containing PBT as the skin layer material, PBT as the core layer material, and carry out skin-core composite spinning, the ratio of the cross-sectional area of the skin layer and the core layer is 2:5, and the spinning temperature The temperature is 270°C, the winding speed is controlled at 2700m/min, and the monofilament fineness of the obtained fluorine-containing PBT-PBT sheath-core composite fiber is 1dtex.
实施例2Example 2
1.含氟PBT聚酯的制备方法,分为酯化反应和缩聚反应两步。具体步骤为:1. The preparation method of fluorine-containing PBT polyester is divided into two steps of esterification reaction and polycondensation reaction. The specific steps are:
所述酯化反应:Described esterification reaction:
采用摩尔比为1.6:1的1,4-丁二醇和四氟对苯二甲酸作为原料,同时加入四氟对苯二甲酸重量的0.02%的氧化硅,配成均匀浆料后进行酯化反应;酯化反应在氮气氛围中,压力控制在900Pa以下,温度控制在200℃,酯化水馏出量达到理论值的90%为酯化反应终点。Use 1,4-butanediol and tetrafluoroterephthalic acid with a molar ratio of 1.6:1 as raw materials, and add 0.02% silicon oxide based on the weight of tetrafluoroterephthalic acid at the same time, make a uniform slurry and carry out esterification reaction ; The esterification reaction is carried out in a nitrogen atmosphere, the pressure is controlled below 900Pa, the temperature is controlled at 200°C, and the esterification water distillate reaches 90% of the theoretical value, which is the end point of the esterification reaction.
所述缩聚反应:Described polycondensation reaction:
包括缩聚反应低真空阶段和缩聚反应高真空阶段:Including low vacuum stage of polycondensation reaction and high vacuum stage of polycondensation reaction:
所述缩聚反应低真空阶段,在酯化产物中加入四氟对苯二甲酸重量的0.02%的催化剂钛酸四异丙脂和四氟对苯二甲酸重量的0.02%的稳定剂磷酸三苯酯,在负压的条件下开始缩聚反应,所述负压是指绝对压力小于400Pa,温度控制在260℃,反应时间为60分钟。In the low-vacuum stage of the polycondensation reaction, 0.02% of the weight of tetrafluoroterephthalic acid is added to the esterification product. The catalyst tetraisopropyl titanate and the stabilizer triphenyl phosphate of 0.02% of the weight of tetrafluoroterephthalic acid are added. , the polycondensation reaction starts under the condition of negative pressure, said negative pressure means that the absolute pressure is less than 400Pa, the temperature is controlled at 260°C, and the reaction time is 60 minutes.
所述缩聚反应高真空阶段,经所述缩聚反应低真空阶段后,继续抽真空,使反应压力降至绝对压力小于80Pa,反应温度控制在270℃,反应时间4小时。缩聚反应以反应釜搅拌电机功率或在线粘度计读数为准判断反应终点。当聚合物粘度达到所需值时出料,经铸带、冷却、切粒,即得到含氟PBT聚酯切片。In the high vacuum stage of the polycondensation reaction, after the low vacuum stage of the polycondensation reaction, the vacuum is continued to reduce the reaction pressure to an absolute pressure of less than 80 Pa, the reaction temperature is controlled at 270° C., and the reaction time is 4 hours. The polycondensation reaction is based on the power of the stirring motor of the reactor or the reading of the online viscometer to judge the end point of the reaction. When the viscosity of the polymer reaches the desired value, the material is discharged, and after casting, cooling and pelletizing, the fluorine-containing PBT polyester chips are obtained.
2.皮芯复合纤维的制备:将所述含氟PBT作为皮层材料,PBT作为芯层材料,进行皮芯复合纺丝,皮层和芯层的横截面积之比为4:5,纺丝温度为274℃,卷绕速度控制在3200m/min,所得含氟PBT-PBT皮芯复合纤维的单丝纤度为15dtex。2. Preparation of skin-core composite fiber: use the fluorine-containing PBT as the skin layer material, PBT as the core layer material, and carry out skin-core composite spinning, the ratio of the cross-sectional area of the skin layer and the core layer is 4:5, and the spinning temperature The temperature is 274°C, the winding speed is controlled at 3200m/min, and the monofilament fineness of the obtained fluorine-containing PBT-PBT sheath-core composite fiber is 15dtex.
实施例3Example 3
1.含氟PBT聚酯的制备方法,分为酯化反应和缩聚反应两步。具体步骤为:1. The preparation method of fluorine-containing PBT polyester is divided into two steps of esterification reaction and polycondensation reaction. The specific steps are:
所述酯化反应:Described esterification reaction:
采用摩尔比为1.8:1的1,4-丁二醇和四氟对苯二甲酸作为原料,同时加入四氟对苯二甲酸重量的0.03%的氧化钙,配成均匀浆料后进行酯化反应;酯化反应在氮气氛围中,压力控制在800Pa以下,温度控制在180℃,酯化水馏出量达到理论值的90%为酯化反应终点。Use 1,4-butanediol and tetrafluoroterephthalic acid with a molar ratio of 1.8:1 as raw materials, and add 0.03% calcium oxide based on the weight of tetrafluoroterephthalic acid at the same time, make a uniform slurry and carry out esterification reaction ; The esterification reaction is carried out in a nitrogen atmosphere, the pressure is controlled below 800Pa, the temperature is controlled at 180°C, and the esterification water distillate reaches 90% of the theoretical value, which is the end point of the esterification reaction.
所述缩聚反应:Described polycondensation reaction:
包括缩聚反应低真空阶段和缩聚反应高真空阶段:Including low vacuum stage of polycondensation reaction and high vacuum stage of polycondensation reaction:
所述缩聚反应低真空阶段,在酯化产物中加入四氟对苯二甲酸重量的0.03%的催化剂钛酸四乙酯和四氟对苯二甲酸重量的0.03%的稳定剂磷酸三甲酯,在负压的条件下开始缩聚反应,所述负压是指绝对压力小于300Pa,温度控制在265℃,反应时间为50分钟。In the low-vacuum stage of the polycondensation reaction, 0.03% of the catalyst tetraethyl titanate and 0.03% of the weight of the tetrafluoroterephthalic acid are added to the esterification product, and the stabilizer trimethyl phosphate is added, The polycondensation reaction is started under the condition of negative pressure, said negative pressure means that the absolute pressure is less than 300 Pa, the temperature is controlled at 265° C., and the reaction time is 50 minutes.
所述缩聚反应高真空阶段,经所述缩聚反应低真空阶段后,继续抽真空,使反应压力降至绝对压力小于60Pa,反应温度控制在275℃,反应时间3.5小时。缩聚反应以反应釜搅拌电机功率或在线粘度计读数为准判断反应终点。当聚合物粘度达到所需值时出料,经铸带、冷却、切粒,即得到含氟PBT聚酯切片。In the high vacuum stage of the polycondensation reaction, after the low vacuum stage of the polycondensation reaction, the vacuum was continued to reduce the reaction pressure to an absolute pressure of less than 60 Pa, the reaction temperature was controlled at 275° C., and the reaction time was 3.5 hours. The polycondensation reaction is based on the power of the stirring motor of the reactor or the reading of the online viscometer to judge the end point of the reaction. When the viscosity of the polymer reaches the desired value, the material is discharged, and after casting, cooling and pelletizing, the fluorine-containing PBT polyester chips are obtained.
2.皮芯复合纤维的制备:将所述含氟PBT作为皮层材料,PBT作为芯层材料,进行皮芯复合纺丝,皮层和芯层的横截面积之比为3:5,纺丝温度为279℃,卷绕速度控制在2900m/min,所得含氟PBT-PBT皮芯复合纤维的单丝纤度为10dtex。2. Preparation of skin-core composite fiber: use the fluorine-containing PBT as the skin layer material, PBT as the core layer material, and carry out skin-core composite spinning, the ratio of the cross-sectional area of the skin layer and the core layer is 3:5, and the spinning temperature The temperature is 279°C, the winding speed is controlled at 2900m/min, and the monofilament fineness of the obtained fluorine-containing PBT-PBT sheath-core composite fiber is 10dtex.
实施例4Example 4
1.含氟PBT聚酯的制备方法,分为酯化反应和缩聚反应两步。具体步骤为:1. The preparation method of fluorine-containing PBT polyester is divided into two steps of esterification reaction and polycondensation reaction. The specific steps are:
所述酯化反应:Described esterification reaction:
采用摩尔比为1.9:1的1,4-丁二醇和四氟对苯二甲酸作为原料,同时加入四氟对苯二甲酸重量的0.04%的氧化锌,配成均匀浆料后进行酯化反应;酯化反应在氮气氛围中,压力控制在700Pa以下,温度控制在170℃,酯化水馏出量达到理论值的90%为酯化反应终点。Use 1,4-butanediol and tetrafluoroterephthalic acid with a molar ratio of 1.9:1 as raw materials, and add 0.04% zinc oxide based on the weight of tetrafluoroterephthalic acid at the same time, make a uniform slurry and carry out esterification reaction ; The esterification reaction is carried out in a nitrogen atmosphere, the pressure is controlled below 700Pa, the temperature is controlled at 170°C, and the esterification water distillate reaches 90% of the theoretical value, which is the end point of the esterification reaction.
所述缩聚反应:Described polycondensation reaction:
包括缩聚反应低真空阶段和缩聚反应高真空阶段:Including low vacuum stage of polycondensation reaction and high vacuum stage of polycondensation reaction:
所述缩聚反应低真空阶段,在酯化产物中加入四氟对苯二甲酸重量的0.04%的催化剂醋酸亚锡和四氟对苯二甲酸重量的0.04%的稳定剂磷酸三甲酯,在负压的条件下开始缩聚反应,所述负压是指绝对压力小于300Pa,温度控制在270℃,反应时间为40分钟。In the low vacuum stage of the polycondensation reaction, add 0.04% of the catalyst stannous acetate of tetrafluoroterephthalic acid weight and 0.04% of the stabilizer trimethyl phosphate of tetrafluoroterephthalic acid weight in the esterification product, The polycondensation reaction starts under the condition of pressure, the said negative pressure means that the absolute pressure is less than 300Pa, the temperature is controlled at 270°C, and the reaction time is 40 minutes.
所述缩聚反应高真空阶段,经所述缩聚反应低真空阶段后,继续抽真空,使反应压力降至绝对压力小于60Pa,反应温度控制在275℃,反应时间3小时。缩聚反应以反应釜搅拌电机功率或在线粘度计读数为准判断反应终点。当聚合物粘度达到所需值时出料,经铸带、冷却、切粒,即得到含氟PBT聚酯切片。In the high vacuum stage of the polycondensation reaction, after the low vacuum stage of the polycondensation reaction, the vacuum is continued to reduce the reaction pressure to an absolute pressure of less than 60 Pa, the reaction temperature is controlled at 275° C., and the reaction time is 3 hours. The polycondensation reaction is based on the power of the stirring motor of the reactor or the reading of the online viscometer to judge the end point of the reaction. When the viscosity of the polymer reaches the desired value, the material is discharged, and after casting, cooling and pelletizing, the fluorine-containing PBT polyester chips are obtained.
2.皮芯复合纤维的制备:将所述含氟PBT作为皮层材料,PBT作为芯层材料,进行皮芯复合纺丝,皮层和芯层的横截面积之比为5:5,纺丝温度为275℃,卷绕速度控制在2800m/min,所得含氟PBT-PBT皮芯复合纤维的单丝纤度为5dtex。2. Preparation of skin-core composite fiber: use the fluorine-containing PBT as the skin layer material, PBT as the core layer material, and carry out skin-core composite spinning, the ratio of the cross-sectional area of the skin layer and the core layer is 5:5, and the spinning temperature The temperature is 275°C, the winding speed is controlled at 2800m/min, and the monofilament fineness of the obtained fluorine-containing PBT-PBT sheath-core composite fiber is 5dtex.
实施例5Example 5
1.含氟PBT聚酯的制备方法,分为酯化反应和缩聚反应两步。具体步骤为:1. The preparation method of fluorine-containing PBT polyester is divided into two steps of esterification reaction and polycondensation reaction. The specific steps are:
所述酯化反应:Described esterification reaction:
采用摩尔比为2.0:1的1,4-丁二醇和四氟对苯二甲酸作为原料,同时加入四氟对苯二甲酸重量的0.05%的氧化锰,配成均匀浆料后进行酯化反应;酯化反应在氮气氛围中,压力控制在600Pa以下,温度控制在160℃,酯化水馏出量达到理论值的90%为酯化反应终点。Use 1,4-butanediol and tetrafluoroterephthalic acid with a molar ratio of 2.0:1 as raw materials, and add 0.05% manganese oxide by weight of tetrafluoroterephthalic acid at the same time, make a uniform slurry and carry out esterification reaction ; The esterification reaction is carried out in a nitrogen atmosphere, the pressure is controlled below 600Pa, the temperature is controlled at 160°C, and the esterification water distillate reaches 90% of the theoretical value, which is the end point of the esterification reaction.
所述缩聚反应:Described polycondensation reaction:
包括缩聚反应低真空阶段和缩聚反应高真空阶段:Including low vacuum stage of polycondensation reaction and high vacuum stage of polycondensation reaction:
所述缩聚反应低真空阶段,在酯化产物中加入四氟对苯二甲酸重量的0.05%的催化剂二醋酸二丁基锡和四氟对苯二甲酸重量的0.05%的稳定剂亚磷酸三甲酯,在负压的条件下开始缩聚反应,所述负压是指绝对压力小于300Pa,温度控制在265℃,反应时间为40分钟。In the low-vacuum stage of the polycondensation reaction, add 0.05% of the catalyst dibutyltin diacetate and 0.05% of the tetrafluoroterephthalic acid weight in the esterification product. Stabilizer trimethyl phosphite, The polycondensation reaction starts under the condition of negative pressure, said negative pressure means that the absolute pressure is less than 300 Pa, the temperature is controlled at 265° C., and the reaction time is 40 minutes.
所述缩聚反应高真空阶段,经所述缩聚反应低真空阶段后,继续抽真空,使反应压力降至绝对压力小于50Pa,反应温度控制在275℃,反应时间3小时。缩聚反应以反应釜搅拌电机功率或在线粘度计读数为准判断反应终点。当聚合物粘度达到所需值时出料,经铸带、冷却、切粒,即得到含氟PBT聚酯切片。In the high vacuum stage of the polycondensation reaction, after the low vacuum stage of the polycondensation reaction, the vacuum is continued to reduce the reaction pressure to an absolute pressure of less than 50 Pa, the reaction temperature is controlled at 275° C., and the reaction time is 3 hours. The polycondensation reaction is based on the power of the stirring motor of the reactor or the reading of the online viscometer to judge the end point of the reaction. When the viscosity of the polymer reaches the desired value, the material is discharged, and after casting, cooling and pelletizing, the fluorine-containing PBT polyester chips are obtained.
2.皮芯复合纤维的制备:将所述含氟PBT作为皮层材料,PBT作为芯层材料,进行皮芯复合纺丝,皮层和芯层的横截面积之比为1:2,纺丝温度为280℃,卷绕速度控制在3100m/min,所得含氟PBT-PBT皮芯复合纤维的单丝纤度为3dtex。2. Preparation of skin-core composite fiber: use the fluorine-containing PBT as the skin layer material and PBT as the core layer material to carry out skin-core composite spinning. The ratio of the cross-sectional area of the skin layer to the core layer is 1:2, and the spinning temperature is The temperature is 280°C, the winding speed is controlled at 3100m/min, and the monofilament fineness of the obtained fluorine-containing PBT-PBT sheath-core composite fiber is 3dtex.
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