WO2023279985A1 - 一种耐循环注塑的pbt组合物及其制备方法和制品 - Google Patents

一种耐循环注塑的pbt组合物及其制备方法和制品 Download PDF

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WO2023279985A1
WO2023279985A1 PCT/CN2022/101086 CN2022101086W WO2023279985A1 WO 2023279985 A1 WO2023279985 A1 WO 2023279985A1 CN 2022101086 W CN2022101086 W CN 2022101086W WO 2023279985 A1 WO2023279985 A1 WO 2023279985A1
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pbt
injection molding
zone
temperature
parts
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French (fr)
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陈伟
陈平绪
叶南飚
莫文杰
龚德君
冯健
付学俊
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金发科技股份有限公司
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L67/00Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
    • C08L67/02Polyesters derived from dicarboxylic acids and dihydroxy compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Definitions

  • the invention relates to the technical field of engineering plastics, more specifically, to a cycle-resistant injection-molded PBT composition, a preparation method and a product thereof.
  • Polybutylene terephthalate referred to as PBT
  • PBT Polybutylene terephthalate
  • the retention rate of the mechanical properties of the material is generally below 80% of the performance of the new material; after the third injection molding, the performance retention rate further drops below 60%, which cannot meet the requirements of the product in most cases. application requirements.
  • the PBT nozzle material in order to recycle the PBT nozzle material, the PBT nozzle material is usually blended with new and old materials in a certain proportion into the uninjected PBT raw material, so as to make up for the PBT material under multiple injection molding. performance degradation.
  • the nozzle material cannot be used directly, and the recycling efficiency is poor, and the loss of mechanical properties of the PBT material caused by repeated injection molding has not been completely solved.
  • the present invention provides a PBT composition resistant to cycle injection molding.
  • the post-mechanical performance retention rate is ⁇ 91%.
  • Another object of the present invention is to provide a preparation method of the above cycle injection resistant PBT composition.
  • Another object of the present invention is to provide the application of the above-mentioned PBT composition in the preparation of recycled PBT products.
  • a PBT composition resistant to cycle injection comprising the following components by weight:
  • TMPTA propane trimethylol triacrylate
  • the inventors have found that the main reason for the decline in the mechanical properties of PBT materials during the multiple-cycle injection molding process is the breakage of the PBT molecular chain, mainly polar ester bonds: The breakage of the chain segment degrades the PBT material, and its mechanical properties drop significantly.
  • TMPTA Propane trimethylol triacrylate
  • TMPTA is usually used as a cross-linking agent to provide intermolecular cross-linking under the conditions of heat, light or radiation effect.
  • TMPTA can bring good molecular chain protection to PBT materials after being added to the PBT system of the present invention.
  • the addition of TMPTA makes the linear PBT molecules connect to each other to form a network structure.
  • This "group-like" network structure makes the ester bonds of PBT highly protected during processing, and the probability of chain segment breakage is greatly reduced.
  • similar crosslinking agent products of TMPTA such as trimethylolpropane tri(meth)acrylate (TMPTMA) cannot provide the excellent protective effect on PBT molecular chains comparable to TMPTA.
  • EBA is usually added to PBT materials as a toughening agent.
  • the addition of EBA not only improves the initial toughness of the PBT composition, but also has excellent synergistic effect between EBA and TMPTA. Due to the existence of TMPTA, after multiple cycles of injection molding, the phase interface between EBA and PBT resin can be better maintained without being destroyed, thus greatly improving the toughness retention rate after cycle injection molding.
  • the viscosity of the TMPTA at 25°C is 80-120 CPS.
  • the viscosity detection method is GB/T 10247-2008.
  • the viscosity of TMPTA When the viscosity of TMPTA is high, its dispersibility in the PBT system is slightly poor, which will further make it difficult to uniformly disperse among the materials of the PBT composition of the present invention; when the viscosity of TMPTA is low, the molecular chain protection of PBT is weak.
  • the viscosity of TMPTA is 80-120CPS at 25°C, it can have good dispersibility, make the dispersion of each component more uniform, and has excellent molecular chain protection, so that the mechanical properties of the PBT composition can be maintained after multiple cycles of injection molding. High rate.
  • the viscosity of the TMPTA at 25°C is 90-110 CPS.
  • the intrinsic viscosity of the PBT at 25°C is 1.0 ⁇ 1.3 dL/g.
  • the PBT intrinsic viscosity test method is based on GB/T 14190-2017.
  • the glass fiber is treated with a coupling agent, and the coupling agent is N-( ⁇ -aminoethyl)- ⁇ -aminopropyl trimethoxysilane, ⁇ -methacryloxypropyl trimethyl A blend of oxysilane, isopropyl bis(methacryl) isostearyl titanate.
  • the coupling agent is N-( ⁇ -aminoethyl)- ⁇ -aminopropyl trimethoxysilane, ⁇ -methacryloxypropyl trimethyl A blend of oxysilane, isopropyl bis(methacryl) isostearyl titanate.
  • the blending weight ratio of isostearyl titanate is 1:2:1.
  • the glass fiber treated with coupling agent has more excellent interfacial properties with PBT. Better performance retention can be maintained during overmolding or overmolding.
  • the epoxy resin is bisphenol A glycidyl ether, and the epoxy equivalent is less than 600g/eq.
  • test method of described epoxy equivalent is based on GB/T 4612-2008.
  • the mechanical property retention rate of the PBT composition of the present invention can be maintained at a good level during multiple injection molding cycles.
  • a large number of creative experimental data show that when a certain component or certain two components are missing, the PBT composition cannot achieve the mechanical property retention effect described in the present invention.
  • the epoxy equivalent of the epoxy resin is 450-500 g/eq.
  • the antioxidant is a hindered phenolic antioxidant.
  • the antioxidant is ⁇ (3,5 di-tert-butyl-4-hydroxyphenyl) octadecyl propionate (antioxidant 1076) and/or 1,3,5-tri(4 -tert-butyl-3-hydroxy-2,6-dimethylbenzyl)-1,3,5-triazine-2,4,6-(1H,3H,5H)-trione.
  • the ethylene-butyl acrylate copolymer is 2.5-5 parts by weight
  • the propane trimethylol triacrylate is 1-1.5 parts by weight
  • the epoxy resin is 1.5-2.5 parts by weight.
  • the present invention also protects the preparation method of the above-mentioned PBT composition, comprising the following steps:
  • PBT glass fiber
  • epoxy resin antioxidant
  • EBA antioxidant
  • TMPTA TMPTA
  • the extruder is a twin-screw extruder.
  • the temperature of the first zone of the twin-screw extruder from the feeding port to the machine head is 200-230°C
  • the temperature of the second zone is 240-260°C
  • the temperature of the third zone is 235-255°C
  • the temperature of the fourth zone is 235 ⁇ 255°C
  • the temperature in the fifth zone is 235 ⁇ 255°C
  • the temperature in the sixth zone is 240 ⁇ 260°C
  • the temperature in the seventh zone is 240 ⁇ 260°C
  • the temperature in the eighth zone is 220 ⁇ 240°C
  • the temperature in the ninth zone is 220 ⁇ 240°C
  • the temperature in the tenth zone is 240-260° C.
  • the screw speed of the twin-screw extruder is 200-450 rpm.
  • the present invention also protects the application of the above-mentioned PBT composition in the preparation of recycled PBT products.
  • the present invention also protects a regenerated PBT product, which is directly processed from the nozzle material of the above-mentioned PBT composition.
  • the invention effectively improves the retention rate of the mechanical properties of the PBT composition after multiple injections through the synergistic effect of propane trimethylol triacrylate, ethylene-butyl acrylate copolymer and epoxy resin.
  • Propane trimethylol triacrylate is directly added to the PBT system, which effectively prevents the breakage of the PBT molecular chain, thereby reducing the degradation of the PBT material in the multiple injection molding process; at the same time, due to the synergistic
  • the effect further improves the mechanical property retention rate of the PBT composition.
  • the mechanical property retention rate of the PBT composition of the present invention is ⁇ 97% after secondary injection molding, and the mechanical property retention rate is ⁇ 91% after three injection moldings, and is suitable for multiple cycle injection molding.
  • the raw material in embodiment and comparative example all can be obtained by commercially available, specifically as follows:
  • the reagents, methods and equipment used in the present invention are conventional reagents, methods and equipment in the technical field.
  • the temperature of the first zone from the feed port to the head of the twin-screw extruder is 200-230°C
  • the temperature of the second zone is 240-260°C
  • the temperature of the third zone is 235-255°C
  • the temperature of the fourth zone is 235-255°C
  • the temperature of the fifth zone is 235-255°C.
  • the temperature in the zone is 235-255°C
  • the temperature in the sixth zone is 240-260°C
  • the temperature in the seventh zone is 240-260°C
  • the temperature in the eighth zone is 220-240°C
  • the temperature in the ninth zone is 220-240°C
  • the temperature in the tenth zone is 240-240°C 260°C
  • the screw speed of the twin-screw extruder is 200-450 rpm.
  • the preparation method is as follows: mix the components according to Table 2, add them into a twin-screw extruder, melt, extrude and granulate to obtain the PBT composition.
  • the temperature of the first zone from the feed port to the head of the twin-screw extruder is 200-230°C
  • the temperature of the second zone is 240-260°C
  • the temperature of the third zone is 235-255°C
  • the temperature of the fourth zone is 235-255°C
  • the temperature of the fifth zone is 235-255°C.
  • the temperature in the zone is 235-255°C
  • the temperature in the sixth zone is 240-260°C
  • the temperature in the seventh zone is 240-260°C
  • the temperature in the eighth zone is 220-240°C
  • the temperature in the ninth zone is 220-240°C
  • the temperature in the tenth zone is 240-240°C 260°C
  • the screw speed of the twin-screw extruder is 200-450 rpm.
  • the performance test of the PBT composition prepared by the above-mentioned embodiment and comparative example is carried out, and the test method is as follows.
  • Secondary injection molding crush the mechanical splines obtained by the primary injection molding with a crusher, dry the crushed particles in a blast drying oven at 120°C for 6 hours, and then inject them into ISO standard mechanical splines through an injection molding machine, which is the secondary injection molding.
  • Injection Molding Mechanics Splines
  • Three-time injection molding crush the mechanical splines obtained by secondary injection molding with a crusher, dry the crushed particles in a blast drying oven at 120°C for 6 hours, and then inject them into ISO standard mechanical splines through an injection molding machine, which is three-time injection molding Mechanics splines.
  • Notched impact strength tested according to the ISO180-2000 standard method, the unit is kJ/m 2 ;
  • the PBT composition in Examples 1 to 20 is through secondary injection molding, compared with the initial injection molding, the mechanical property retention rate is ⁇ 97%, and the PBT composition is through three injection moldings, compared with the initial injection molding, the mechanical property Retention rate ⁇ 91%. This shows that the PBT composition of the present invention has very little loss of mechanical properties after repeated injection molding, and still maintains good high rigidity and toughness.
  • the PBT compositions of comparative examples 1 to 3 lack propane trimethylol triacrylate, ethylene-butyl acrylate copolymer or epoxy resin respectively, and the mechanical properties after secondary injection molding are only 80% to 84% of the initial injection molding. After three injection molding The post-mechanical properties are only 71-78% of the initial injection molding, which has a relatively large decline. This shows that the three components of propane trimethylol triacrylate, ethylene-butyl acrylate copolymer or epoxy resin can only bring good cycle resistance to the PBT composition through a synergistic effect when they are added together. Injection performance. In comparative example 4, the content of propane trimethylol triacrylate and ethylene-butyl acrylate copolymer is less, and the retention rate of its mechanical properties is poor.
  • Comparative example 5 EBA is replaced by other kinds of toughening agent EMA; Comparative example 6, TMPTA is replaced by other kinds of crosslinking agent: TMPTMA, according to its test results, it can be seen that although compared with the mechanical properties of comparative examples 1 to 4, it remains The rate has been improved to a certain extent, but it still has not reached the excellent level that in the embodiment, the retention rate of the mechanical properties of the secondary injection molding is more than or equal to 97%, and the retention rate of the mechanical properties of the third injection molding is more than or equal to 91%.

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Abstract

本发明公开了一种耐循环注塑的PBT组合物及其制备方法。本发明的耐循环注塑的PBT组合物,包括如下重量份的组分:PBT 50~80份,玻璃纤维10~40份,环氧树脂1~3份,抗氧剂0.1~0.3份,乙烯-丙烯酸丁酯共聚物2~8份,三丙烯酸丙烷三甲醇酯0.5~2份。本发明通过三丙烯酸丙烷三甲醇酯、乙烯-丙烯酸丁酯共聚物和环氧树脂的协同作用,有效阻止了PBT分子链的断裂,从而降低了PBT材料在多次注塑过程中的降解程度,进一步提高了PBT组合物的多次注塑后力学性能保持率。本发明的PBT组合物经过二次注塑力学性能保持率≥97%,三次注塑后力学性能保持率≥91%,适合多次循环注塑使用。

Description

一种耐循环注塑的PBT组合物及其制备方法和制品 技术领域
本发明涉及工程塑料技术领域,更具体的,涉及一种耐循环注塑的PBT组合物及其制备方法和制品。
背景技术
随着塑料工业的迅速发展,越来越多的塑胶材料通过注塑成为塑料制品,应用于各类生产生活场景。注塑过程中一般会产生大量无使用价值的浇注系统凝料,即注塑产品外的浇口和流道的成型物,又称为水口材料。一般而言,若将浇注系统凝料粉碎后二次注塑成型,材料的性能会大幅劣化,因而无法多次循环注塑使用,造成巨大浪费。
聚对苯二甲酸丁二醇酯,简称PBT,广泛应用于汽车、家电、工具及其它各类电子电气部件场合。但该类材料在二次注塑使用后,材料机械性能保持率一般在全新料性能80%以下;三次注塑使用后,性能保持率进一步降至60%以下,在绝大部分场合已经无法满足制品的应用要求。
现有技术中,为了回收利用PBT的水口材料,通常以新旧料共混的方式,将PBT的水口材料以一定的比例掺进未经注塑的PBT原料中,以弥补PBT材料在多次注塑下的性能下降。但该方法中水口材料仍不能直接使用,回收再利用效率差,未彻底解决多次循环注塑对PBT材料的力学性能损耗。
因此,需要开发出一种耐多次循环注塑的PBT组合物。
发明内容
本发明为克服上述现有技术所述的多次注塑后力学性能差的缺陷,提供一种耐循环注塑的PBT组合物,该PBT组合物经过二次注塑力学性能保持率≥97%,三次注塑后力学性能保持率≥91%。
本发明的另一目的在于提供上述耐循环注塑的PBT组合物的制备方法。
本发明的另一目的在于提供上述PBT组合物在制备再生PBT制品中的应用。
为解决上述技术问题,本发明采用的技术方案是:
一种耐循环注塑的PBT组合物,包括如下重量份的组分:
PBT50~80份,
玻璃纤维10~40份,
环氧树脂1~3份,
抗氧剂0.1~0.3份,
乙烯-丙烯酸丁酯共聚物(EBA)2~8份,
三丙烯酸丙烷三甲醇酯(TMPTA)0.5~2份。
发明人研究发现,PBT材料在多次循环注塑过程中,影响其力学性能下降的主要原因是PBT分子链的断裂,主要是极性酯键:
Figure PCTCN2022101086-appb-000001
链段的断裂,从而使得PBT材料降解,其力学性能大幅下降。
三丙烯酸丙烷三甲醇酯(TMPTA),分子式为(CH 2=CHCOOCH 2) 3-CCH 2CH 3,TMPTA通常作为交联剂,在热、光或辐照的条件下提供分子间的促交联作用。
发明人研究发现,TMPTA加入本发明的PBT体系中后,能为PBT材料带来良好的分子链保护作用。TMPTA的加入使得线型的PBT分子之间相互连接,形成网状结构,这种“抱团式”网状结构使得加工过程中PBT的酯键受到高度保护,链段断裂的几率大大降低。而TMPTA的同类交联剂产品,如三羟甲基丙烷三(甲基)丙烯酸酯(TMPTMA),无法提供与TMPTA相当的对PBT分子链的优异保护作用。
EBA通常作为增韧剂加至PBT材料中。但在本发明的技术方案中,EBA的加入不仅提高了PBT组合物的初始韧性,且EBA与TMPTA具有优异的协同增效作用。由于TMPTA的存在,经多次循环注塑后,EBA与PBT树脂间的相界面能得到更好的保持而不被破坏,从而大幅改善了循环注塑后的韧性保持率。
优选地,所述TMPTA在25℃下的粘度为80~120CPS。所述粘度检测方法为GB/T 10247-2008。
TMPTA的粘度较高时,其在PBT体系内分散性稍差,会进一步使得本发明PBT组合物的物料之间难以均匀分散;TMPTA的粘度较低时,对PBT的分子链保护作用较弱。TMPTA的粘度在25℃下为80~120CPS时,能兼具良好的分散性,使得各组分分散更均一,又具有优异的分子链保护作用,使得PBT组合物经多次循环注塑力学性能保持率高。
更优选地,所述TMPTA在25℃下的粘度为90~110CPS。
优选地,所述PBT在25℃下的特性粘度为1.0~1.3dL/g。
PBT特性粘度测试方法依据GB/T 14190-2017。
发明人研究发现,该粘度范围的PBT能使得本发明的PBT组合物具有更高的多次注塑性能保持率。
优选地,所述玻璃纤维经偶联剂处理,所述偶联剂为N-(β-氨基乙基)-γ-氨基丙基三甲氧基硅烷、γ-甲基丙烯酰氧基丙基三甲氧基硅烷、异丙基二(甲基丙烯酰基)异硬脂酰基钛酸酯的共混物。
更优选地,所述N-(β-氨基乙基)-γ-氨基丙基三甲氧基硅烷、γ-甲基丙烯酰氧基丙基三甲氧基硅烷、异丙基二(甲基丙烯酰基)异硬脂酰基钛酸酯的共混重量比为1:2:1。
经偶联剂处理的玻璃纤维,具有与PBT间更优异的界面性能。在二次注塑或三次注塑的过程中,能够维持更优的性能保持率。
优选地,所述环氧树脂为双酚A型缩水甘油醚,环氧当量<600g/eq。
所述环氧当量的测试方法依据GB/T 4612-2008。
在环氧树脂、EBA和TMPTA的共用作用下,本发明所述PBT组合物在多次循环注塑的过程中力学性能保持率才得以维持良好水平。大量的创造性实验数据表明,当缺少某一组分或某两种组分,PBT组合物均无法达到本发明所述的力学性能保持效果。
更优选地,所述环氧树脂的环氧当量为450~500g/eq。
优选地,所述抗氧剂为受阻酚类抗氧剂。
可选的,所述抗氧剂为β(3,5二叔丁基-4-羟基苯基)丙酸十八醇酯(抗氧剂1076)和/或1,3,5-三(4-叔丁基-3-羟基-2,6-二甲基苄基)-1,3,5-三嗪-2,4,6-(1H,3H,5H)-三酮。
优选地,所述PBT组合物中,乙烯-丙烯酸丁酯共聚物为2.5~5重量份,三丙烯酸丙烷三甲醇酯为1~1.5重量份,环氧树脂为1.5~2.5重量份。
本发明还保护上述PBT组合物的制备方法,包括如下步骤:
将PBT、玻璃纤维、环氧树脂、抗氧剂、EBA和TMPTA混合后加入挤出机,经熔融挤出造粒,得到所述PBT组合物。
优选地,所述挤出机为双螺杆挤出机。
更优选地,所述双螺杆挤出机从喂料口到机头的一区温度为200~230℃,二区温度为240~260℃,三区温度为235~255℃,四区温度为235~255℃,五区温度为235~255℃,六区温度为240~260℃,七区温度为240~260℃,八区温度为 220~240℃,九区温度为220~240℃,十区温度为240~260℃,所述双螺杆挤出机的螺杆转速为200~450转/分钟。
本发明还保护上述PBT组合物在制备再生PBT制品中的应用。
本发明还保护一种再生PBT制品,所述再生PBT制品由上述PBT组合物的水口材料直接加工制得。
与现有技术相比,本发明的有益效果是:
本发明通过三丙烯酸丙烷三甲醇酯、乙烯-丙烯酸丁酯共聚物和环氧树脂的协同作用,有效提高了PBT组合物的多次注塑后力学性能保持率。三丙烯酸丙烷三甲醇酯直接加至PBT体系中,有效阻止了PBT分子链的断裂,从而降低了PBT材料在多次注塑过程中的降解;同时由于三丙烯酸丙烷三甲醇酯和环氧树脂的协同作用,进一步提高了PBT组合物的力学性能保持率。本发明的PBT组合物经过二次注塑力学性能保持率≥97%,三次注塑后力学性能保持率≥91%,适合多次循环注塑使用。
具体实施方式
下面结合具体实施方式对本发明作进一步的说明。
实施例及对比例中的原料均可通过市售得到,具体如下:
Figure PCTCN2022101086-appb-000002
Figure PCTCN2022101086-appb-000003
除非特别说明,本发明采用的试剂、方法和设备为本技术领域常规试剂、方法和设备。
实施例1~20
实施例1~20的PBT组合物中各组分的含量如表1所示。
其制备方法为:将偶联剂N-(β-氨基乙基)-γ-氨基丙基三甲氧基硅烷、γ-甲基丙烯酰氧基丙基三甲氧基硅烷、异丙基二(甲基丙烯酰基)异硬脂酰基钛酸酯按照重量比1:2:1共混后,对玻璃纤维进行偶联处理,得到经偶联处理的玻璃纤维;
根据表1将PBT、经偶联处理的玻璃纤维或未经偶联处理的玻璃纤维、环氧树脂、抗氧剂、EBA和TMPTA混合后加入双螺杆挤出机,经熔融挤出造粒,得到所述PBT组合物。
双螺杆挤出机从喂料口到机头的一区温度为200~230℃,二区温度为240~260℃,三区温度为235~255℃,四区温度为235~255℃,五区温度为235~255℃,六区温度为240~260℃,七区温度为240~260℃,八区温度为220~240℃,九区温度为220~240℃,十区温度为240~260℃,双螺杆挤出机的螺杆转速为200~450转/分钟。
表1 实施例1~20的PBT组合物中各组分的含量(重量份)
Figure PCTCN2022101086-appb-000004
Figure PCTCN2022101086-appb-000005
Figure PCTCN2022101086-appb-000006
对比例1~6
对比例1~6的PBT组合物中各组分的含量如表2所示。
其制备方法为:根据表2将各组分混合后加入双螺杆挤出机,经熔融挤出造粒,得到所述PBT组合物。
双螺杆挤出机从喂料口到机头的一区温度为200~230℃,二区温度为240~260℃,三区温度为235~255℃,四区温度为235~255℃,五区温度为235~255℃,六区温度为240~260℃,七区温度为240~260℃,八区温度为220~240℃,九区温度为220~240℃,十区温度为240~260℃,双螺杆挤出机的螺杆转速为200~450转/分钟。
表2 对比例1~6的PBT组合物中各组分的含量(重量份)
Figure PCTCN2022101086-appb-000007
Figure PCTCN2022101086-appb-000008
性能测试
对上述实施例及对比例制备的PBT组合物进行性能测试,测试方法如下。
对上述PBT组合物进行初次注塑、二次注塑、三次注塑,具体方法为:
初次注塑:将经挤出造粒的PBT组合物粒料在120℃鼓风干燥箱中干燥6h,然后通过注塑机注塑成ISO标准力学样条,即为初次注塑力学样条;
二次注塑:将初次注塑得到的力学样条使用破碎机进行破碎,将破碎后的颗粒在120℃鼓风干燥箱中干燥6h,然后通过注塑机注塑成ISO标准力学样条,即为二次注塑力学样条;
三次注塑:将二次注塑得到的力学样条使用破碎机进行破碎,将破碎后的颗粒在120℃鼓风干燥箱中干燥6h,然后通过注塑机注塑成ISO标准力学样条,即为三次注塑力学样条。
分别将初次/二次/三次注塑力学样条进行力学性能测试,力学性能测试的具体方法为:
拉伸强度:按照ISO527-2012标准方法检测,单位为MPa;
缺口冲击强度:按照ISO180-2000标准方法检测,单位为kJ/m 2
保持率:(二次注塑或三次注塑的检测值/初次注塑的对应检测值)*100%。测试结果
实施例1~20的性能测试结果见表3,对比例1~6的性能测试结果见表4。
表3 实施例1~20的性能测试结果
Figure PCTCN2022101086-appb-000009
Figure PCTCN2022101086-appb-000010
表4 对比例1~6的性能测试结果
Figure PCTCN2022101086-appb-000011
Figure PCTCN2022101086-appb-000012
根据表3的测试结果,实施例1~20中PBT组合物经过二次注塑,与初次注塑相比,力学性能保持率≥97%,PBT组合物经三次注塑,与初次注塑相比,力学性能保持率≥91%。这说明本发明的PBT组合物经过多次循环注塑后,力学性能损失极少,仍维持良较高的刚性和韧性。
对比例1~3的PBT组合物分别缺少三丙烯酸丙烷三甲醇酯、乙烯-丙烯酸丁酯共聚物或环氧树脂,经过二次注塑后力学性能仅为初次注塑的80~84%,经过三次注塑后力学性能仅为初次注塑的71~78%,有较大幅度的下降。这说明三丙烯酸丙烷三甲醇酯、乙烯-丙烯酸丁酯共聚物或环氧树脂这三个组分仅在共同添加的情况下,经过协同增效作用,才能为PBT组合物带来良好的耐循环注塑性能。对比例4中,三丙烯酸丙烷三甲醇酯和乙烯-丙烯酸丁酯共聚物的含量较少,其力学性能保持率较差。
对比例5,EBA替换为其他种增韧剂EMA;对比例6,TMPTA替换为其他种交联剂:TMPTMA,根据其测试结果可以看出,虽然相比于对比例1~4的力学性能保持率有一定程度的提升,但仍未达到实施例中,二次注塑力学性能保持率≥97%,三次注塑力学性能保持率≥91%的优异水平。
显然,本发明的上述实施例仅仅是为清楚地说明本发明所作的举例,而并非是对本发明的实施方式的限定。对于所属领域的普通技术人员来说,在上述说明的基础上还可以做出其它不同形式的变化或变动。这里无需也无法对所有的实施方式予以穷举。凡在本发明的精神和原则之内所作的任何修改、等同替换和改进等,均应包含在本发明权利要求的保护范围之内。

Claims (10)

  1. 一种耐循环注塑的PBT组合物,其特征在于,包括如下重量份的组分:
    PBT 50~80份,玻璃纤维10~40份,环氧树脂1~3份,抗氧剂0.1~0.3份,乙烯-丙烯酸丁酯共聚物2~8份,三丙烯酸丙烷三甲醇酯0.5~2份。
  2. 根据权利要求1所述PBT组合物,其特征在于,所述三丙烯酸丙烷三甲醇酯在25℃下的粘度为80~120CPS。
  3. 根据权利要求1所述PBT组合物,其特征在于,所述PBT在25℃下的特性粘度为1.0~1.3dL/g。
  4. 根据权利要求1所述PBT组合物,其特征在于,所述环氧树脂为双酚A型缩水甘油醚,环氧当量<600g/eq。
  5. 根据权利要求1所述PBT组合物,其特征在于,所述玻璃纤维经偶联剂处理。
  6. 根据权利要求5所述PBT组合物,其特征在于,所述偶联剂为N-(β-氨基乙基)-γ-氨基丙基三甲氧基硅烷、γ-甲基丙烯酰氧基丙基三甲氧基硅烷和异丙基二(甲基丙烯酰基)异硬脂酰基钛酸酯的共混物。
  7. 权利要求1~6任一项所述PBT组合物的制备方法,其特征在于,包括如下步骤:
    将PBT、玻璃纤维、环氧树脂、抗氧剂、乙烯-丙烯酸丁酯共聚物和三丙烯酸丙烷三甲醇酯混合后加入挤出机,经熔融挤出造粒,得到所述PBT组合物。
  8. 根据权利要求7所述制备方法,其特征在于,所述挤出机为双螺杆挤出机;优选地,所述双螺杆挤出机从喂料口到机头的一区温度为200~230℃,二区温度为240~260℃,三区温度为235~255℃,四区温度为235~255℃,五区温度为235~255℃,六区温度为240~260℃,七区温度为240~260℃,八区温度为220~240℃,九区温度为220~240℃,十区温度为240~260℃。
  9. 权利要求1~6任一项所述PBT组合物在制备再生PBT制品中的应用。
  10. 一种再生PBT制品,其特征在于,由权利要求1~6任一项所述PBT组合物的水口材料直接加工制得。
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