CN103668541A - Degradable fibers containing PBAT (poly(butylene adipate-co-terephthalate)) and preparation method thereof - Google Patents

Degradable fibers containing PBAT (poly(butylene adipate-co-terephthalate)) and preparation method thereof Download PDF

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CN103668541A
CN103668541A CN201210349366.0A CN201210349366A CN103668541A CN 103668541 A CN103668541 A CN 103668541A CN 201210349366 A CN201210349366 A CN 201210349366A CN 103668541 A CN103668541 A CN 103668541A
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严莉莉
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Kangwei Holding Group Co ltd
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Hefei Genius New Materials Co Ltd
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Abstract

本发明涉及一种含PBAT的可降解纤维及其制备方法,由包含以下重量份的组分制成:聚己二酸/对苯二甲酸丁二酯(PBAT)30-90份,高分子聚合物10-70份;将聚己二酸/对苯二甲酸丁二酯及高分子聚合物真空干燥至水分含量为100ppm以下,并按比例混合后进行熔融纺丝,并冷却、绕卷成型,得到含PBAT的可降解纤维的预牵伸丝。与现有技术相比,本发明得到的纤维具有较好的可纺性、较高的力学强度以及持续稳定的柔软手感,具有广泛的应用领域,同时本发明的制备方法简单,易操作,一般的纺丝设备即可工业生产,而无需进行设备改造,节省成本。

Figure 201210349366

The invention relates to a degradable fiber containing PBAT and a preparation method thereof, which is made of the following components by weight: 30-90 parts of polyadipate/butylene terephthalate (PBAT), polymerized 10-70 parts of the product; vacuum-dry the poly(butylene adipate/terephthalate) and the high molecular weight polymer until the water content is below 100ppm, and mix them in proportion to carry out melt spinning, and cooling, winding and forming, The pre-drawn filaments of degradable fibers containing PBAT were obtained. Compared with the prior art, the fiber obtained by the present invention has better spinnability, higher mechanical strength and continuous and stable soft hand feeling, and has a wide range of application fields. At the same time, the preparation method of the present invention is simple and easy to operate. The spinning equipment can be industrially produced without equipment modification, which saves costs.

Figure 201210349366

Description

一种含PBAT的可降解纤维及其制备方法A kind of degradable fiber containing PBAT and preparation method thereof

技术领域 technical field

本发明涉及高分子材料技术领域中的可降解纤维及其制备方法,尤其是涉及一种含PBAT的可降解纤维及其制备方法。The invention relates to a degradable fiber in the technical field of polymer materials and a preparation method thereof, in particular to a degradable fiber containing PBAT and a preparation method thereof.

背景技术 Background technique

在可降解材料中,聚己二酸/对苯二甲酸丁二酯(PBAT)是对苯二甲酸、己二酸和丁二醇的三元共聚物,易加工,有较强的韧性和良好的生物降解性,在土壤或堆肥的条件下分解为二氧化碳、生物质和水,其他性能类似于低密度聚乙烯。同时PBAT纤维材料具有良好的生物降解性,手感较PLA等纤维材料柔软,具有较好的弹性,耐热性好,比普通材料耐高温,这些优点决定了其具有广阔的应用前景。但是,由于PBAT的合成过程采用无规共聚,使得其不容易结晶,制约了PBAT纤维制备技术的发展以及PBAT作为纤维材料的应用。因此,以PBAT为原料制备一种符合环保和可持续发展要求的可降解纤维,可拓展其应用领域,具有重要的市场意义。Among the degradable materials, polybutylene adipate/terephthalate (PBAT) is a terpolymer of terephthalic acid, adipic acid and butanediol, which is easy to process, has strong toughness and good Biodegradability, decomposes into carbon dioxide, biomass and water under soil or compost conditions, and other properties are similar to low-density polyethylene. At the same time, PBAT fiber material has good biodegradability, softer hand feeling than PLA and other fiber materials, good elasticity, good heat resistance, and high temperature resistance than ordinary materials. These advantages determine its broad application prospects. However, since the synthesis process of PBAT adopts random copolymerization, it is not easy to crystallize, which restricts the development of PBAT fiber preparation technology and the application of PBAT as a fiber material. Therefore, using PBAT as a raw material to prepare a degradable fiber that meets the requirements of environmental protection and sustainable development can expand its application field and has important market significance.

中国专利CN 101760796A介绍了一种PBT高弹丝的制作方法,通过该方法得到的纤维的强度为30.91-35.52cN/tex,伸长率为30-60%,有极好的伸长弹性回复率和柔软易染色的特点。但其纺丝温度较高,易产生热降解现象。阚瑞俊采用PBAT改变PHBV的结晶形态,PHBV/PBAT共混物相对纯PHBV有更宽的加工窗口,扩宽了其熔融可纺性,但是其共混物的熔喷无纺布的效果并不好,有待进一步的提高(东华大学,硕士论文,2010)。齐中华采用静电纺丝技术制备PHBV/Ecoflex(PBAT)共混体系的超细纤维毡,并分析了Ecoflex的加入对电纺纤维的平均直径和直径分布的影响,但在纺丝前需要配置PHBV/Ecoflex/二氯甲烷溶液,工艺较复杂(合成技术与应用,2008)。Chinese patent CN 101760796A introduces a method for making PBT high elastic yarn. The strength of the fiber obtained by this method is 30.91-35.52cN/tex, the elongation is 30-60%, and it has excellent elongation elastic recovery rate. And the characteristics of soft and easy to dye. However, its spinning temperature is high and it is prone to thermal degradation. Kan Ruijun used PBAT to change the crystal form of PHBV. The PHBV/PBAT blend has a wider processing window than pure PHBV, which broadens its melt spinnability, but the effect of the blend's melt-blown non-woven fabric is not good. , to be further improved (Donghua University, Master Thesis, 2010). Qi Zhonghua used electrospinning technology to prepare ultrafine fiber mats of PHBV/Ecoflex (PBAT) blend system, and analyzed the effect of the addition of Ecoflex on the average diameter and diameter distribution of electrospun fibers, but PHBV needs to be configured before spinning /Ecoflex/dichloromethane solution, the process is more complicated (Synthesis Technology and Application, 2008).

针对上述问题,本发明采用PBAT与其它高分子材料共混后进行熔融纺丝,其中,用来纺丝的线性聚酯的分子量高,且分布较均匀时,得到的纤维的性能较好,在纺丝过程中加长冷却距离,从而有效的改善了PBAT纺丝过程中不易冷却,容易粘结的问题。同时工艺简单易行,可改善PBAT纤维的性能,有效拓宽PBAT纤维材料的应用领域。In view of the above problems, the present invention adopts PBAT to blend with other macromolecular materials to carry out melt spinning, wherein, the molecular weight of the linear polyester used for spinning is high, and when the distribution is relatively uniform, the performance of the fiber obtained is better, and in The cooling distance is lengthened during the spinning process, thus effectively improving the problem that PBAT is not easy to cool and easy to stick during the spinning process. At the same time, the process is simple and easy, which can improve the performance of the PBAT fiber and effectively broaden the application field of the PBAT fiber material.

发明内容 Contents of the invention

本发明的目的就是为了克服上述现有技术存在的缺陷而提供一种具有较好的可纺性、较高的力学强度以及持续稳定的柔软手感的含PBAT的可降解纤维及其制备方法。The purpose of the present invention is to provide a PBAT-containing degradable fiber with good spinnability, high mechanical strength and continuous and stable soft hand feeling and its preparation method in order to overcome the above-mentioned defects in the prior art.

本发明的目的可以通过以下技术方案来实现:The purpose of the present invention can be achieved through the following technical solutions:

一种含PBAT的可降解纤维,由包含以下重量份的组分制成:A kind of degradable fiber containing PBAT is made of components comprising the following parts by weight:

聚己二酸/对苯二甲酸丁二酯(PBAT)     30-90份Polybutylene adipate/terephthalate (PBAT) 30-90 parts

高分子聚合物                        10-70份。High molecular polymer 10-70 parts.

所述的聚己二酸/对苯二甲酸丁二酯的熔点为110~160℃,热分解温度高于300℃,重均分子量为4~12万,分子量分散度为1.5~3。The polybutylene adipate/terephthalate has a melting point of 110-160° C., a thermal decomposition temperature higher than 300° C., a weight-average molecular weight of 40,000-120,000, and a molecular weight dispersion of 1.5-3.

所述的聚己二酸/对苯二甲酸丁二酯的熔点优选为130~150℃,重均分子量优选为8~10万,分子量分散度优选为2~2.5。The melting point of the polybutylene adipate/terephthalate is preferably 130-150° C., the weight-average molecular weight is preferably 8-100,000, and the molecular weight dispersion is preferably 2-2.5.

所述的高分子聚合物选自聚羟基丁酸(PHB)、聚羟基丁酸-戊酸酯(PHBV)、聚丁二酸丁二醇酯(PBS)或聚乳酸(PLA)中的一种或两种。Described macromolecular polymer is selected from the one in polyhydroxybutyric acid (PHB), polyhydroxybutyrate-valerate (PHBV), polybutylene succinate (PBS) or polylactic acid (PLA) or two.

所述的聚羟基丁酸的重均分子量为7~30万,所述的聚羟基丁酸-戊酸酯的重均分子量为10~40万,所述的聚丁二酸丁二醇酯的重均分子量为9~15万,所述的聚乳酸的重均分子量为6~16万。The weight average molecular weight of the polyhydroxybutyric acid is 70,000 to 300,000, the weight average molecular weight of the polyhydroxybutyrate-valerate is 100,000 to 400,000, and the polybutylene succinate The weight average molecular weight is 90,000 to 150,000, and the weight average molecular weight of the polylactic acid is 60,000 to 160,000.

一种含PBAT的可降解纤维的制备方法,该方法包括以下步骤:A preparation method of degradable fiber containing PBAT, the method comprises the following steps:

(1)将聚己二酸/对苯二甲酸丁二酯及高分子聚合物真空干燥至水分含量为100ppm以下;(1) Vacuum drying the poly(butylene adipate/terephthalate) and polymer until the moisture content is below 100ppm;

(2)将干燥后的聚己二酸/对苯二甲酸丁二酯与高分子聚合物按比例混合后进行熔融纺丝,并冷却、绕卷成型,直接得到含PBAT的可降解纤维的预牵伸丝。(2) The dried polybutylene adipate/terephthalate and high molecular weight polymer are mixed in proportion to carry out melt spinning, and cooling, coiling and forming, directly obtain the preform of the degradable fiber containing PBAT Draw wire.

该方法还可以将干燥后的聚己二酸/对苯二甲酸丁二酯与高分子聚合物按比例混合后,用双螺杆挤出机熔融共混、挤出、造粒,得到共混颗粒;再将共混颗粒真空干燥至水分含量为100ppm以下后进行熔融纺丝,并冷却、绕卷成型,得到含PBAT的可降解纤维的预牵伸丝。In this method, after mixing the dried polybutylene adipate/terephthalate and the high molecular weight polymer in proportion, melt blending, extruding, and granulating with a twin-screw extruder to obtain blended granules and then vacuum-dry the blended particles until the moisture content is below 100ppm, then melt-spin, cool, and roll into shape to obtain pre-drawn filaments of degradable fibers containing PBAT.

所述的真空干燥的时间为24~48小时,真空干燥的温度为70~100℃,所述的熔融纺丝的温度为180~245℃,所述的冷却为采用加长距离冷却,冷却的距离为3~5m,卷绕的速度为500~1500m/min。The time of the vacuum drying is 24-48 hours, the temperature of the vacuum drying is 70-100°C, the temperature of the melt-spinning is 180-245°C, and the cooling is extended distance cooling, the cooling distance The winding speed is 3-5m, and the winding speed is 500-1500m/min.

所述的熔融纺丝采用螺杆型纺丝机。The melt spinning adopts a screw-type spinning machine.

所述的挤出的温度为170~220℃,双螺杆挤出机的螺杆的转速为100~500rpm。The extruding temperature is 170-220° C., and the screw speed of the twin-screw extruder is 100-500 rpm.

与现有技术相比,本发明具有以下优点及有益效果:Compared with the prior art, the present invention has the following advantages and beneficial effects:

与普通的PBAT纤维相比,本发明得到的纤维具有较好的可纺性、较高的力学强度以及持续稳定的柔软手感,因此可扩展其应用领域,广泛应用在纺织等领域。同时本发明的制备方法简单,易操作,一般的纺丝设备即可工业生产,而无需进行设备改造,节省成本。本发明中通过添加高分子聚合物提高PBAT纤维的性能,采用加长冷却距离的方式,有效改善纺丝过程中丝条粘结的问题,得到性能良好的纤维材料。Compared with ordinary PBAT fibers, the fibers obtained by the present invention have better spinnability, higher mechanical strength, and continuous and stable soft hand feeling, so their application fields can be expanded and widely used in textile and other fields. At the same time, the preparation method of the present invention is simple and easy to operate, and the general spinning equipment can be industrially produced without equipment modification, which saves costs. In the present invention, the performance of the PBAT fiber is improved by adding a high molecular polymer, and the method of lengthening the cooling distance is adopted to effectively improve the problem of thread sticking in the spinning process, and obtain a fiber material with good performance.

附图说明 Description of drawings

图1为螺杆型纺丝机的结构示意图。Figure 1 is a schematic structural view of a screw-type spinning machine.

具体实施方式 Detailed ways

下面结合附图和具体实施例对本发明进行详细说明。The present invention will be described in detail below in conjunction with the accompanying drawings and specific embodiments.

实施例1Example 1

(1)将聚对苯二甲酸丁二酯-己二酸丁二醇酯(PBAT,重均分子量为10万)、聚羟基丁酸-戊酸酯(PHBV,重均分子量为30万)和聚乳酸(PLA,重均分子量为8万)颗粒进行真空干燥,至水分为100ppm,干燥温度为95℃,干燥时间30h。(1) Polybutylene terephthalate-butylene adipate (PBAT, with a weight-average molecular weight of 100,000), polyhydroxybutyrate-valerate (PHBV, with a weight-average molecular weight of 300,000) and The particles of polylactic acid (PLA, with a weight average molecular weight of 80,000) were vacuum-dried until the water content was 100 ppm, the drying temperature was 95° C., and the drying time was 30 h.

(2)取干燥后的47份PBAT、45份PLA和8份的PHBV混合后用双螺杆挤出机熔融共混、挤出造粒,制成母粒,挤出温度为180℃,螺杆转速为300rpm。(2) Take 47 parts of PBAT after drying, 45 parts of PLA and 8 parts of PHBV and mix them with a twin-screw extruder to melt and blend, extrude and granulate to make master batches. The extrusion temperature is 180 °C and the screw speed 300rpm.

(3)将母粒干燥至水分含量达到100ppm,经如图1所示的螺杆型纺丝机中的料斗1、螺杆2、箱体3、计量泵4的熔融、挤出、过滤、计量处理,从喷丝板5挤出,加长距离6冷却后,经过集束上油装置7和卷绕辊8,得到含PBAT的可降解纤维。(3) Dry the masterbatch until the moisture content reaches 100ppm, and process through melting, extruding, filtering, and metering of the hopper 1, screw 2, box 3, and metering pump 4 in the screw-type spinning machine shown in Figure 1 , extruded from the spinneret 5, extended distance 6 after cooling, through the cluster oiling device 7 and winding roller 8, to obtain the degradable fiber containing PBAT.

其中,纺丝温度190℃,I区/II区/III区/IV区温度分别为180/190/190/190℃,箱体温度为190℃,管道温度为190℃,计量泵温度为190℃,卷绕速度800m/min,冷却距离为3m,制得纤维强度为1.5cN/tex,伸度为69%,手感柔软,在室温下放置一周后,手感仍柔软。Among them, the spinning temperature is 190°C, the temperature of zone I/II/III/IV is 180/190/190/190°C respectively, the temperature of the box is 190°C, the temperature of the pipeline is 190°C, and the temperature of the metering pump is 190°C , the winding speed is 800m/min, the cooling distance is 3m, the strength of the obtained fiber is 1.5cN/tex, the elongation is 69%, and the hand feels soft. After being placed at room temperature for a week, the hand feel is still soft.

实施例2Example 2

(1)将聚对苯二甲酸丁二酯-己二酸丁二醇酯(PBAT,重均分子量为12万)、聚羟基丁酸-戊酸酯(PHBV,重均分子量为20万)颗粒进行真空干燥,至水分为100ppm,干燥温度为80℃,干燥时间48h。(1) Polybutylene terephthalate-butylene adipate (PBAT, with a weight-average molecular weight of 120,000), polyhydroxybutyrate-valerate (PHBV, with a weight-average molecular weight of 200,000) particles Carry out vacuum drying until the water content is 100ppm, the drying temperature is 80°C, and the drying time is 48h.

(2)取干燥后的30份PBAT、70份的PHBV混合后经如图1所示的螺杆型纺丝机中的料斗1、螺杆2、箱体3、计量泵4的熔融、挤出、过滤、计量处理,从喷丝板5挤出,加长距离6冷却后,经过集束上油装置7和卷绕辊8,得到含PBAT的可降解纤维。(2) After getting 30 parts of PBAT after drying, the PHBV of 70 parts mixes through hopper 1 in the screw type spinning machine as shown in Figure 1, screw rod 2, casing 3, the melting of metering pump 4, extrusion, Filtration, metering treatment, extruding from spinneret 5, lengthening distance 6 and cooling, passing through cluster oiling device 7 and winding roller 8 to obtain degradable fibers containing PBAT.

其中,纺丝温度200℃,I区/II区/III区/IV区温度分别为190/200/200/200℃,箱体温度为200℃,管道温度为200℃,计量泵温度为200℃,卷绕速度1200m/min,冷却距离为4m,制得纤维强度为1.1cN/tex,伸度为92%,手感柔软,在室温下放置一周后,手感仍柔软。Among them, the spinning temperature is 200°C, the temperature of zone I/II/III/IV is 190/200/200/200°C respectively, the temperature of the box is 200°C, the temperature of the pipeline is 200°C, and the temperature of the metering pump is 200°C , the winding speed is 1200m/min, the cooling distance is 4m, the strength of the obtained fiber is 1.1cN/tex, the elongation is 92%, the hand feel is soft, and after being placed at room temperature for a week, the hand feel is still soft.

实施例3Example 3

(1)将聚对苯二甲酸丁二酯-己二酸丁二酯(PBAT,重均分子量为6万)、聚丁二酸丁二醇酯(PBS,重均分子量为10万)颗粒进行真空干燥,至水分为100ppm,干燥温度为85℃,干燥时间40h。(1) Polybutylene terephthalate-butylene adipate (PBAT, weight-average molecular weight is 60,000), polybutylene succinate (PBS, weight-average molecular weight is 100,000) particles Vacuum-dry until the water content is 100ppm, the drying temperature is 85°C, and the drying time is 40h.

(2)取干燥后的90份PBAT、10份的PBS混合后经料斗1、螺杆2、箱体3、计量泵4的熔融、挤出、过滤、计量处理,从喷丝板5挤出,加长距离6冷却后,经过集束上油装置7和卷绕辊8,得到含PBAT的可降解纤维。(2) After mixing 90 parts of PBAT and 10 parts of PBS after drying, they are melted, extruded, filtered and metered through hopper 1, screw 2, casing 3 and metering pump 4, extruded from spinneret 5, After lengthening the distance 6 and cooling, the degradable fiber containing PBAT is obtained through the clustering and oiling device 7 and the winding roller 8 .

其中,纺丝温度245℃,I区/II区/III区/IV区温度分别为235/245/245/245℃,箱体温度为245℃,管道温度为245℃,计量泵温度为245℃,卷绕速度1500m/min,冷却距离为3.5m,制得纤维强度为1.2cN/tex,伸度为84%,手感柔软。Among them, the spinning temperature is 245°C, the temperature of zone I/II/III/IV is 235/245/245/245°C respectively, the box temperature is 245°C, the pipeline temperature is 245°C, and the metering pump temperature is 245°C , the winding speed is 1500m/min, the cooling distance is 3.5m, the fiber strength is 1.2cN/tex, the elongation is 84%, and the hand feel is soft.

实施例4Example 4

(1)将聚对苯二甲酸丁二酯-己二酸丁二醇酯(PBAT,重均分子量为10万)和聚乳酸(PLA,重均分子量为12万)颗粒进行真空干燥,至水分为100ppm,干燥温度为95℃,干燥时间28h。(1) Polybutylene terephthalate-butylene adipate (PBAT, weight-average molecular weight is 100,000) and polylactic acid (PLA, weight-average molecular weight is 120,000) particles are vacuum-dried until moisture It is 100ppm, the drying temperature is 95°C, and the drying time is 28h.

(2)取干燥后的65份PBAT、35份PLA颗粒混合后用双螺杆挤出机熔融共混、挤出造粒,制成母粒,挤出温度为170℃,螺杆转速为100rpm。(2) After mixing 65 parts of PBAT and 35 parts of PLA pellets after drying, they were melt-blended with a twin-screw extruder, extruded and granulated to make master batches. The extrusion temperature was 170°C and the screw speed was 100rpm.

(3)然后将母粒干燥至水分含量达到100ppm,经料斗1、螺杆2、箱体3、计量泵4的熔融、挤出、过滤、计量处理,从喷丝板5挤出,加长距离6冷却后,经过集束上油装置7和卷绕辊8,得到含PBAT的可降解纤维。(3) Then the masterbatch is dried until the moisture content reaches 100ppm, melted, extruded, filtered, and metered by the hopper 1, the screw 2, the box body 3, and the metering pump 4, and then extruded from the spinneret 5 to extend the distance 6 After cooling, the degradable fibers containing PBAT are obtained through the bundle oiling device 7 and the winding roller 8 .

其中,纺丝温度210℃,I区/II区/III区/IV区温度分别为200/210/210/210℃,箱体温度为210℃,管道温度为210℃,计量泵温度为210℃,卷绕速度1000m/min,冷却距离为4m,制得纤维强度为1.4cN/tex,伸度为78%,手感柔软,。Among them, the spinning temperature is 210°C, the temperature in zone I/II/III/IV is 200/210/210/210°C respectively, the box temperature is 210°C, the pipeline temperature is 210°C, and the metering pump temperature is 210°C , The winding speed is 1000m/min, the cooling distance is 4m, the fiber strength is 1.4cN/tex, the elongation is 78%, and the hand feel is soft.

实施例5Example 5

(1)将聚对苯二甲酸丁二酯-己二酸丁二醇酯(PBAT,重均分子量为4万)、聚乳酸(PLA,重均分子量为6万)和聚丁二酸丁二醇酯(PBS,重均分子量为9万)颗粒进行真空干燥,至水分为100ppm,干燥温度为85℃,干燥时间30h。(1) Polybutylene terephthalate-butylene adipate (PBAT, with a weight average molecular weight of 40,000), polylactic acid (PLA, with a weight average molecular weight of 60,000) and polybutylene succinate Alcohol ester (PBS, weight-average molecular weight: 90,000) granules were vacuum-dried until the water content was 100 ppm, the drying temperature was 85° C., and the drying time was 30 h.

(2)取干燥后的40份PBAT、40份PLA和20份PBS颗粒混合后用双螺杆挤出机熔融共混、挤出造粒,制成母粒,挤出温度为190℃,螺杆转速为500rpm。(2) Take the dried 40 parts of PBAT, 40 parts of PLA and 20 parts of PBS granules and mix them with a twin-screw extruder to melt and blend, extrude and granulate to make masterbatches. The extrusion temperature is 190 °C and the screw speed 500rpm.

(3)然后将母粒干燥至水分含量达到100ppm,经料斗1、螺杆2、箱体3、计量泵4的熔融、挤出、过滤、计量处理,从喷丝板5挤出,加长距离6冷却后,经过集束上油装置7和卷绕辊8,得到含PBAT的可降解纤维。(3) Then the masterbatch is dried until the moisture content reaches 100ppm, melted, extruded, filtered, and metered by the hopper 1, the screw 2, the box body 3, and the metering pump 4, and then extruded from the spinneret 5 to extend the distance 6 After cooling, the degradable fibers containing PBAT are obtained through the bundle oiling device 7 and the winding roller 8 .

其中,纺丝温度220℃,I区/II区/III区/IV区温度分别为210/220/220/220℃,箱体温度为220℃,管道温度为220℃,计量泵温度为220℃,卷绕速度500m/min,冷却距离为3.5m,制得纤维强度为1.7cN/tex,伸度为53%,手感柔软。Among them, the spinning temperature is 220°C, the temperature of zone I/II/III/IV is 210/220/220/220°C respectively, the box temperature is 220°C, the pipeline temperature is 220°C, and the metering pump temperature is 220°C , the winding speed is 500m/min, the cooling distance is 3.5m, the fiber strength is 1.7cN/tex, the elongation is 53%, and the hand feel is soft.

实施例6Example 6

(1)将聚对苯二甲酸丁二酯-己二酸丁二醇酯(PBAT,重均分子量为9万)、聚羟基丁酸(PHB,重均分子量为17万)颗粒进行真空干燥,至水分为100ppm,干燥温度为80℃,干燥时间48h。(1) Polybutylene terephthalate-butylene adipate (PBAT, weight-average molecular weight is 90,000), polyhydroxybutyric acid (PHB, weight-average molecular weight is 170,000) particles are vacuum-dried, Until the water content is 100ppm, the drying temperature is 80°C, and the drying time is 48h.

(2)取干燥后的70份PBAT、30份的PHB混合后经料斗1、螺杆2、箱体3、计量泵4的熔融、挤出、过滤、计量处理,从喷丝板5挤出,加长距离6冷却后,经过集束上油装置7和卷绕辊8,得到含PBAT的可降解纤维。(2) After mixing 70 parts of PBAT and 30 parts of PHB after drying, they are melted, extruded, filtered and metered through hopper 1, screw 2, casing 3 and metering pump 4, extruded from spinneret 5, After lengthening the distance 6 and cooling, the degradable fiber containing PBAT is obtained through the clustering and oiling device 7 and the winding roller 8 .

其中,纺丝温度230℃,I区/II区/IN区/IV区温度分别为220/230/230/230℃,箱体温度为230℃,管道温度为230℃,计量泵温度为230℃,卷绕速度900m/min,冷却距离为4.5m,制得纤维强度为1.3cN/tex,伸度为77%,手感柔软。Among them, the spinning temperature is 230°C, the temperature of zone I/II/IN/IV is 220/230/230/230°C respectively, the temperature of the box is 230°C, the temperature of the pipeline is 230°C, and the temperature of the metering pump is 230°C , the winding speed is 900m/min, the cooling distance is 4.5m, the fiber strength is 1.3cN/tex, the elongation is 77%, and the hand feel is soft.

实施例7Example 7

一种含PBAT的可降解纤维,由包含以下重量份的组分制成:A kind of degradable fiber containing PBAT is made of components comprising the following parts by weight:

聚己二酸/对苯二甲酸丁二酯(PBAT)        30份Polybutylene adipate/terephthalate (PBAT) 30 parts

高分子聚合物            70份。High molecular polymer 70 parts.

其中,聚己二酸/对苯二甲酸丁二酯的熔点为110℃,热分解温度高于300℃,重均分子量为8万,分子量分散度为1.5。Among them, polybutylene adipate/terephthalate has a melting point of 110° C., a thermal decomposition temperature higher than 300° C., a weight average molecular weight of 80,000, and a molecular weight dispersion of 1.5.

高分子聚合物为聚羟基丁酸(PHB)与聚羟基丁酸-戊酸酯(PHBV)的混合物,各占35份。其中聚羟基丁酸的重均分子量为7万,聚羟基丁酸-戊酸酯的重均分子量为10万。The polymer is a mixture of polyhydroxybutyrate (PHB) and polyhydroxybutyrate-valerate (PHBV), each accounting for 35 parts. Wherein the weight average molecular weight of polyhydroxybutyric acid is 70,000, and the weight average molecular weight of polyhydroxybutyrate-valerate is 100,000.

一种含PBAT的可降解纤维的制备方法,该方法包括以下步骤:A preparation method of degradable fiber containing PBAT, the method comprises the following steps:

(1)将聚己二酸/对苯二甲酸丁二酯及高分子聚合物真空干燥至水分含量为100ppm以下;(1) Vacuum drying the poly(butylene adipate/terephthalate) and polymer until the moisture content is below 100ppm;

(2)将干燥后的聚己二酸/对苯二甲酸丁二酯与高分子聚合物按比例混合,用双螺杆挤出机熔融共混、挤出、造粒,得到共混颗粒;(2) mixing the dried polybutylene adipate/terephthalate and high molecular weight polymer in proportion, melt blending, extruding and granulating with a twin-screw extruder to obtain blended granules;

(3)将步骤(2)得到的共混颗粒干燥至水分含量为100ppm以下后采用螺杆型纺丝机进行熔融纺丝,并冷却、绕卷成型,得到含PBAT的可降解纤维的预牵伸丝。(3) Dry the blended particles obtained in step (2) until the moisture content is below 100ppm, and then use a screw-type spinning machine to carry out melt spinning, and cooling, winding and forming, to obtain the pre-drawing of the degradable fiber containing PBAT Silk.

步骤(1)真空干燥的时间为24小时,真空干燥的温度为100℃;步骤(2)挤出的温度为220℃,螺杆的转速为500rpm;步骤(3)熔融纺丝的温度为180℃,冷却为采用加长距离冷却,冷却的距离为3m,卷绕的速度为500m/min。制得纤维强度为1.2cN/tex,伸度为80%,手感较柔软。The time of step (1) vacuum drying is 24 hours, and the temperature of vacuum drying is 100°C; the temperature of step (2) extrusion is 220°C, and the rotating speed of the screw is 500rpm; the temperature of step (3) melt spinning is 180°C , the cooling is extended distance cooling, the cooling distance is 3m, and the winding speed is 500m/min. The strength of the obtained fiber is 1.2cN/tex, the elongation is 80%, and the handle is soft.

实施例8Example 8

一种含PBAT的可降解纤维,由包含以下重量份的组分制成:A kind of degradable fiber containing PBAT is made of components comprising the following parts by weight:

聚己二酸/对苯二甲酸丁二酯(PBAT)        90份Polybutylene adipate/terephthalate (PBAT) 90 parts

高分子聚合物                           10份。Polymer 10 parts.

其中,聚己二酸/对苯二甲酸丁二酯的熔点为130℃,热分解温度高于300℃,重均分子量为8万,分子量分散度为2。Among them, polybutylene adipate/terephthalate has a melting point of 130°C, a thermal decomposition temperature higher than 300°C, a weight average molecular weight of 80,000, and a molecular weight dispersion of 2.

高分子聚合物为聚羟基丁酸(PHB)与聚乳酸(PLA)的混合物,各占5份。其中,聚羟基丁酸的重均分子量为30万,聚乳酸的重均分子量为16万。The polymer is a mixture of polyhydroxybutyric acid (PHB) and polylactic acid (PLA), each accounting for 5 parts. Among them, the weight average molecular weight of polyhydroxybutyric acid is 300,000, and the weight average molecular weight of polylactic acid is 160,000.

一种含PBAT的可降解纤维的制备方法,该方法包括以下步骤:A preparation method of degradable fiber containing PBAT, the method comprises the following steps:

(1)将聚己二酸/对苯二甲酸丁二酯及高分子聚合物真空干燥至水分含量为100ppm以下;(1) Vacuum drying the poly(butylene adipate/terephthalate) and polymer until the moisture content is below 100ppm;

(2)将干燥后的聚己二酸/对苯二甲酸丁二酯与高分子聚合物按比例混合后进行熔融纺丝,并冷却、绕卷成型,直接得到含PBAT的可降解纤维的预牵伸丝。(2) The dried polybutylene adipate/terephthalate and high molecular weight polymer are mixed in proportion to carry out melt spinning, and cooling, coiling and forming, directly obtain the preform of the degradable fiber containing PBAT Draw wire.

熔融纺丝采用螺杆型纺丝机。Melt spinning uses a screw type spinning machine.

步骤(1)真空干燥的时间为48小时,真空干燥的温度为70℃步骤(2)熔融纺丝的温度为180℃,冷却为采用加长距离冷却,冷却的距离为5m,卷绕的速度为1500m/min。制得纤维强度为1.4cN/tex,伸度为91%,手感柔软。The time of step (1) vacuum drying is 48 hours, and the temperature of vacuum drying is 70 DEG C. The temperature of step (2) melt spinning is 180 DEG C, and cooling is to adopt extended distance cooling, and the distance of cooling is 5m, and the speed of coiling is 1500m/min. The strength of the obtained fiber is 1.4cN/tex, the elongation is 91%, and the hand feeling is soft.

实施例9Example 9

一种含PBAT的可降解纤维,由包含以下重量份的组分制成:A kind of degradable fiber containing PBAT is made of components comprising the following parts by weight:

聚己二酸/对苯二甲酸丁二酯(PBAT)     50份Polybutylene adipate/terephthalate (PBAT) 50 parts

高分子聚合物                        50份。Polymer 50 parts.

其中,聚己二酸/对苯二甲酸丁二酯的熔点为150℃,热分解温度高于300℃,重均分子量为10万,分子量分散度为2.5。Among them, polybutylene adipate/terephthalate has a melting point of 150° C., a thermal decomposition temperature higher than 300° C., a weight average molecular weight of 100,000, and a molecular weight dispersion of 2.5.

高分子聚合物为聚羟基丁酸-戊酸酯(PHBV)与聚丁二酸丁二醇酯(PBS)的混合物,各占25份。其中,聚羟基丁酸-戊酸酯的重均分子量为40万,聚丁二酸丁二醇酯的重均分子量为15万。The polymer is a mixture of polyhydroxybutyrate-valerate (PHBV) and polybutylene succinate (PBS), each accounting for 25 parts. Among them, the weight average molecular weight of polyhydroxybutyrate-valerate is 400,000, and the weight average molecular weight of polybutylene succinate is 150,000.

一种含PBAT的可降解纤维的制备方法,该方法包括以下步骤:A preparation method of degradable fiber containing PBAT, the method comprises the following steps:

(1)将聚己二酸/对苯二甲酸丁二酯及高分子聚合物真空干燥至水分含量为100ppm以下;(1) Vacuum drying the poly(butylene adipate/terephthalate) and polymer until the moisture content is below 100ppm;

(2)将干燥后的聚己二酸/对苯二甲酸丁二酯与高分子聚合物按比例混合,用双螺杆挤出机熔融共混、挤出、造粒,得到共混颗粒;(2) mixing the dried polybutylene adipate/terephthalate and high molecular weight polymer in proportion, melt blending, extruding and granulating with a twin-screw extruder to obtain blended granules;

(3)将步骤(2)得到的共混颗粒干燥至水分含量为100ppm以下后采用螺杆型纺丝机进行熔融纺丝,并冷却、绕卷成型,得到含PBAT的可降解纤维的预牵伸丝。(3) Dry the blended particles obtained in step (2) until the moisture content is below 100ppm, and then use a screw-type spinning machine to carry out melt spinning, and cooling, winding and forming, to obtain the pre-drawing of the degradable fiber containing PBAT Silk.

步骤(1)真空干燥的时间为48小时,真空干燥的温度为70℃;步骤(2)挤出的温度为170℃,螺杆的转速为400rpm;步骤(3)熔融纺丝的温度为180℃,冷却为采用加长距离冷却,冷却的距离为4.5m,卷绕的速度为1000m/min。制得纤维强度为1.2cN/tex,伸度为71%,手感柔软。The time of step (1) vacuum drying is 48 hours, and the temperature of vacuum drying is 70°C; the temperature of step (2) extrusion is 170°C, and the rotating speed of the screw is 400rpm; the temperature of step (3) melt spinning is 180°C , the cooling is extended distance cooling, the cooling distance is 4.5m, and the winding speed is 1000m/min. The obtained fiber has a strength of 1.2cN/tex, an elongation of 71%, and a soft hand.

实施例10Example 10

一种含PBAT的可降解纤维,由包含以下重量份的组分制成:A kind of degradable fiber containing PBAT is made of components comprising the following parts by weight:

聚己二酸/对苯二甲酸丁二酯(PBAT)         60份Polybutylene adipate/terephthalate (PBAT) 60 parts

高分子聚合物                            40份。High molecular polymer 40 parts.

其中,聚己二酸/对苯二甲酸丁二酯的熔点为160℃,热分解温度高于300℃,重均分子量为8万,分子量分散度为3。Among them, polybutylene adipate/terephthalate has a melting point of 160°C, a thermal decomposition temperature higher than 300°C, a weight average molecular weight of 80,000, and a molecular weight dispersion of 3.

高分子聚合物选自聚羟基丁酸(PHB)。其中,聚羟基丁酸的重均分子量为20万。The high molecular polymer is selected from polyhydroxybutyric acid (PHB). Wherein, the weight average molecular weight of polyhydroxybutyric acid is 200,000.

一种含PBAT的可降解纤维的制备方法,该方法包括以下步骤:A preparation method of degradable fiber containing PBAT, the method comprises the following steps:

(1)将聚己二酸/对苯二甲酸丁二酯及高分子聚合物真空干燥至水分含量为100ppm以下;(1) Vacuum drying the poly(butylene adipate/terephthalate) and polymer until the moisture content is below 100ppm;

(2)将干燥后的聚己二酸/对苯二甲酸丁二酯与高分子聚合物按比例混合后进行熔融纺丝,并冷却、绕卷成型,直接得到含PBAT的可降解纤维的预牵伸丝。(2) The dried polybutylene adipate/terephthalate and high molecular weight polymer are mixed in proportion to carry out melt spinning, and cooling, coiling and forming, directly obtain the preform of the degradable fiber containing PBAT Draw wire.

其中,熔融纺丝采用螺杆型纺丝机。步骤(1)真空干燥的时间为24小时,真空干燥的温度为100℃;步骤(2)熔融纺丝的温度为245℃,冷却为采用加长距离冷却,冷却的距离为5m,卷绕的速度为800m/min。制得纤维强度为1.1cN/tex,伸度为87%,手感柔软。Among them, a screw type spinning machine is used for the melt spinning. The time of step (1) vacuum drying is 24 hours, and the temperature of vacuum drying is 100°C; the temperature of step (2) melt spinning is 245°C, and the cooling is to adopt extended distance cooling, the cooling distance is 5m, and the winding speed It is 800m/min. The obtained fiber has a strength of 1.1cN/tex, an elongation of 87%, and a soft hand.

比较例1Comparative example 1

(1)将聚对苯二甲酸丁二酯-己二酸丁二醇酯(PBAT,重均分子量为8万)颗粒进行真空干燥,至水分为100ppm,干燥温度为80℃,干燥时间24h。(1) The particles of polybutylene terephthalate-adipate (PBAT, with a weight average molecular weight of 80,000) were vacuum-dried until the moisture content was 100 ppm, the drying temperature was 80° C., and the drying time was 24 hours.

(2)将干燥后的PBAT经料斗1、螺杆2、箱体3、计量泵4的熔融、挤出、过滤、计量处理,从喷丝板5挤出,加长距离6冷却后,经过集束上油装置7和卷绕辊8,得到PBAT可降解纤维。(2) The dried PBAT is melted, extruded, filtered, and metered through the hopper 1, the screw 2, the box body 3, and the metering pump 4, extruded from the spinneret 5, cooled by the extended distance 6, and passed through the cluster Oil device 7 and winding roll 8 to obtain PBAT degradable fibers.

其中,纺丝温度240℃,I区/II区/III区/IV区温度分别为230/240/240/240℃,箱体温度为240℃,管道温度为240℃,计量泵温度为240℃,卷绕速度1000m/min,冷却距离为4m,制得纤维强度为0.78eN/tex,伸度为237%,手感柔软。其强度为0.78cN/tex,伸度为237%。在纺丝过程中,出现粘结及断丝现象,制成的纤维强度较差。Among them, the spinning temperature is 240°C, the temperature of zone I/II/III/IV is 230/240/240/240°C respectively, the box temperature is 240°C, the pipeline temperature is 240°C, and the metering pump temperature is 240°C , the winding speed is 1000m/min, the cooling distance is 4m, the fiber strength is 0.78eN/tex, the elongation is 237%, and the hand feel is soft. Its strength is 0.78cN/tex and its elongation is 237%. During the spinning process, bonding and broken filaments occur, and the strength of the resulting fiber is poor.

比较例2Comparative example 2

(1)将聚对苯二甲酸丁二酯-5二酸丁二醇酯(PBAT,重均分子量为8万)和聚丁二酸丁二醇酯(PBS,重均分子量为12万)进行真空干燥,至水分为100ppm,干燥温度为90℃,干燥时间30h。(1) Polybutylene terephthalate-5-dioic acid butylene glycol ester (PBAT, weight-average molecular weight is 80,000) and polybutylene succinate (PBS, weight-average molecular weight is 120,000) Vacuum drying to 100ppm moisture, drying temperature is 90°C, and drying time is 30h.

(2)取干燥后的95份PBAT和5份PBS混合后用双螺杆挤出机熔融共混、挤出造粒,制成母粒,挤出温度为180℃,螺杆转速为200rpm。(2) After mixing 95 parts of PBAT and 5 parts of PBS after drying, they were melt-blended with a twin-screw extruder, extruded and granulated to make master batches. The extrusion temperature was 180° C., and the screw speed was 200 rpm.

(3)然后将母粒干燥至水分含量达到100ppm,经料斗1、螺杆2、箱体3、计量泵4的熔融、挤出、过滤、计量处理,从喷丝板5挤出,加长距离6冷却后,经过集束上油装置7和卷绕辊8,得到含PBAT的可降解纤维。(3) Then the masterbatch is dried until the moisture content reaches 100ppm, melted, extruded, filtered, and metered by the hopper 1, the screw 2, the box body 3, and the metering pump 4, and then extruded from the spinneret 5 to extend the distance 6 After cooling, the degradable fibers containing PBAT are obtained through the bundle oiling device 7 and the winding roller 8 .

其中,纺丝温度220℃,I区/II区/III区/IV区温度分别为210/220/220/220℃,箱体温度为220℃,管道温度为220℃,计量泵温度为220℃,卷绕速度900m/min,冷却距离为3.5m,制得纤维强度为0.71cN/tex,伸度为241%,手感柔软。由于PBS添加量太小,且经过两次熔融过程,可纺性下降,出现断丝现象。Among them, the spinning temperature is 220°C, the temperature of zone I/II/III/IV is 210/220/220/220°C respectively, the box temperature is 220°C, the pipeline temperature is 220°C, and the metering pump temperature is 220°C , the winding speed is 900m/min, the cooling distance is 3.5m, the fiber strength is 0.71cN/tex, the elongation is 241%, and the hand feel is soft. Because the amount of PBS added is too small, and after two melting processes, the spinnability decreases and the phenomenon of broken filaments occurs.

比较例3Comparative example 3

(1)将聚乳酸(PLA,重均分子量为8万)进行真空干燥,至水分为100ppm,干燥温度为I00℃,干燥时间32h。(1) Polylactic acid (PLA, with a weight-average molecular weight of 80,000) was vacuum-dried until the moisture content was 100 ppm, the drying temperature was 100° C., and the drying time was 32 hours.

(2)将干燥后的PLA经料斗1、螺杆2、箱体3、计量泵4的熔融、挤出、过滤、计量处理,从喷丝板5挤出,加长距离6冷却后,经过集束上油装置7和卷绕辊8,得到PLA纤维。(2) The dried PLA is melted, extruded, filtered, and metered through the hopper 1, the screw 2, the box body 3, and the metering pump 4, extruded from the spinneret 5, cooled by the extended distance 6, and passed through the cluster Oil device 7 and winding roll 8 to obtain PLA fibers.

其中,纺丝温度250℃,I区/II区/III区/IV区温度分别为240/250/250/250℃,箱体温度为250℃,管道温度为250℃,计量泵温度为250℃,卷绕速度1000m/min,冷却距离为5m,制得纤维强度为2.35cN/tex,伸度为89%,PLA纤维无弹性且硬,限制了其应用领域。Among them, the spinning temperature is 250°C, the temperature of zone I/II/III/IV is 240/250/250/250°C respectively, the box temperature is 250°C, the pipeline temperature is 250°C, and the metering pump temperature is 250°C , the winding speed is 1000m/min, the cooling distance is 5m, the strength of the obtained fiber is 2.35cN/tex, and the elongation is 89%. The PLA fiber is inelastic and hard, which limits its application field.

通过以上实施例和比较例的结果可知,本发明中得到的含PBAT的可降解纤维,其强度≥1.1eN/dtex,伸度为70-100%。当冷却距离加长后,可有效改善纺丝过程出现的粘结问题,同时PBAT具有良好的弹性及耐热性,与其他可降解高分子材料共混后进行纺丝,不仅可提高共混纤维的性能,而且得到的含PBAT的纤维手感柔软,仍具有可降解性。According to the results of the above examples and comparative examples, the degradable fiber containing PBAT obtained in the present invention has a strength ≥ 1.1 eN/dtex and an elongation of 70-100%. When the cooling distance is lengthened, it can effectively improve the sticking problem in the spinning process. At the same time, PBAT has good elasticity and heat resistance. Blending with other degradable polymer materials for spinning can not only improve the blending fiber Performance, and the obtained PBAT-containing fiber feels soft and still has degradability.

Claims (10)

1. containing a biodegradable fiber of PBAT, it is characterized in that, by the component that comprises following weight portion, made:
Poly-adipic acid/butylene terephthalate (PBAT) 30-90 part
High molecular polymer 10-70 part.
2. a kind of biodegradable fiber containing PBAT according to claim 1, it is characterized in that, the fusing point of described poly-adipic acid/butylene terephthalate is 110~160 ℃, and heat decomposition temperature is higher than 300 ℃, weight average molecular weight is 4~120,000, and molecular weight dispersity is 1.5~3.
3. a kind of biodegradable fiber containing PBAT according to claim 2, is characterized in that, the fusing point of described poly-adipic acid/butylene terephthalate is preferably 130~150 ℃, and weight average molecular weight is preferably 8~100,000, and molecular weight dispersity is preferably 2~2.5.
4. a kind of biodegradable fiber containing PBAT according to claim 1, is characterized in that, described high molecular polymer is selected from one or both in poly butyric, poly butyric-valerate, poly butylene succinate or PLA.
5. a kind of biodegradable fiber containing PBAT according to claim 4, it is characterized in that, the weight average molecular weight of described poly butyric is 7~300,000, the weight average molecular weight of described poly butyric-valerate is 10~400,000, the weight average molecular weight of described poly butylene succinate is 9~150,000, and the weight average molecular weight of described PLA is 6~160,000.
6. a preparation method for the biodegradable fiber containing PBAT as described in as arbitrary in claim 1~5, is characterized in that, the method comprises the following steps:
(1) will gather adipic acid/butylene terephthalate and high molecular polymer vacuumize to moisture is below 100ppm;
(2) carry out melt spinning after dried poly-adipic acid/butylene terephthalate is mixed in proportion with high molecular polymer, and cooling, around roll forming, directly obtain the preliminary draft silk containing the biodegradable fiber of PBAT.
7. the preparation method of a kind of biodegradable fiber containing PBAT according to claim 6, it is characterized in that, after the method can also be mixed dried poly-adipic acid/butylene terephthalate with high molecular polymer in proportion, with double screw extruder melt blending, extrude, granulation, obtain blended particles; By blended particles vacuumize to moisture, be to carry out melt spinning after below 100ppm again, and cooling, around roll forming, obtain the preliminary draft silk containing the biodegradable fiber of PBAT.
8. according to the preparation method of a kind of biodegradable fiber containing PBAT described in claim 6 or 7, it is characterized in that, the described vacuum drying time is 24~48 hours, vacuum drying temperature is 70~100 ℃, the temperature of described melt spinning is 180~245 ℃, described being cooled to adopts lengthening distance cooling, and cooling distance is 3~5m, and the speed of coiling is 500~1500m/min.
9. according to the preparation method of a kind of biodegradable fiber containing PBAT described in claim 6 or 7, it is characterized in that, described melt spinning adopts screw type spinning machine.
10. the preparation method of a kind of biodegradable fiber containing PBAT according to claim 7, is characterized in that, the described temperature of extruding is 170~220 ℃, and the rotating speed of the screw rod of double screw extruder is 100~500rpm.
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