WO2016106837A1 - Reactive thermoplastic resin composition and manufacturing method thereof - Google Patents

Reactive thermoplastic resin composition and manufacturing method thereof Download PDF

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WO2016106837A1
WO2016106837A1 PCT/CN2015/070579 CN2015070579W WO2016106837A1 WO 2016106837 A1 WO2016106837 A1 WO 2016106837A1 CN 2015070579 W CN2015070579 W CN 2015070579W WO 2016106837 A1 WO2016106837 A1 WO 2016106837A1
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resin composition
thermoplastic resin
portions
polybutylene terephthalate
impact
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PCT/CN2015/070579
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French (fr)
Chinese (zh)
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单桂芳
李强
罗明华
辛敏琦
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上海锦湖日丽塑料有限公司
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L69/00Compositions of polycarbonates; Compositions of derivatives of polycarbonates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/92Measuring, controlling or regulating
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/32Phosphorus-containing compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L51/00Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
    • C08L51/04Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers grafted on to rubbers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L55/00Compositions of homopolymers or copolymers, obtained by polymerisation reactions only involving carbon-to-carbon unsaturated bonds, not provided for in groups C08L23/00 - C08L53/00
    • C08L55/02ABS [Acrylonitrile-Butadiene-Styrene] polymers
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C2948/00Indexing scheme relating to extrusion moulding
    • B29C2948/92Measuring, controlling or regulating
    • B29C2948/92504Controlled parameter
    • B29C2948/92704Temperature
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/08Stabilised against heat, light or radiation or oxydation
    • 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

Definitions

  • the invention relates to a reactive thermoplastic resin composition and a preparation method thereof, and belongs to the technical field of polymer material processing.
  • CN101558121 discloses that a polyamide elastomer resin composition having a polyamide 6 and a reactive functional group is prepared by using a twin-screw extruder having a ratio of length to diameter (L/D) of more than 50, and the prepared resin composition is microscopically prepared.
  • the phase behavior is as follows: the nano-scale dispersed polyolefin elastomer contains a large number of smaller nano-scale polyamide 6 micelles, and exhibits remarkable excellent energy absorption properties at the macroscopic level, but its bending mode at room temperature.
  • the amount is only 1300 MPa; for the PC/PBT system, Chinese patents CN 103772934A and CN 101935446A both disclose the interface of the obtained PC/PBT resin composition by adding a functionalized elastomer together with an interface compatibilizer and a toughening agent.
  • the high-strength, high-notch impact performance is excellent; and the two-phase continuous structure having a structural period of 0.001 to 1 ⁇ m or 0.01 to 1 ⁇ m is constructed by a spinodal phase separation mechanism, as disclosed in US Pat. No. 7,523,612 and Japanese Patent No. 2003-286414. Excellent heat resistance and tensile properties.
  • the disadvantage of the rubber toughening system is that it has low rigidity and heat resistance at room temperature, and is not suitable for use as a structural member, and the introduction of a large amount of rubber components may cause difficulty in processability and thermal stability.
  • a series of problems for balance; for the PC/PBT system it is mainly concentrated in three aspects: (1) pay attention to the impact performance of the gap, and pay little attention to the surface impact performance; (2) focus on how to construct the double continuous using the Spinodal phase separation mechanism. Phase structure; (3) Pay attention to the phase interface strength of PC and PBT.
  • an object of the present invention is to provide a reactive thermoplastic resin composition and Preparation.
  • the present invention relates to a reactive thermoplastic resin composition
  • a reactive thermoplastic resin composition comprising the following components in parts by weight:
  • the polybutylene terephthalate has an intrinsic viscosity of 0.6 to 1.5 dl/gr and a terminal-COOH content of ⁇ 50 meq/kg.
  • One of PC or PBT forms a continuous phase, and the other forms a dispersed phase, and the dispersed phase has a particle size of 0.05 to 0.5 ⁇ m or an interparticle distance of 0.05 to 0.5 ⁇ m; preferably, the dispersed phase has a particle size of 0.05 to 0.2 ⁇ m. Or the distance between particles is 0.05 to 0.2 ⁇ m.
  • the polycarbonate resin is a bisphenol A type polycarbonate having a weight average molecular weight of 2.0 to 6.0 ⁇ 10 4 g/mol.
  • the polybutylene terephthalate has an intrinsic viscosity of 1.0 to 1.3 dl/gr and a terminal-COOH content of ⁇ 10 meq/kg.
  • the transesterification inhibitor is one of a phosphate and a phosphite.
  • the impact modifier is a rubber-modified styrene resin
  • examples thereof include an MBS resin (methyl methacrylate-butadiene rubber-styrene copolymer) and an ABS resin (acrylonitrile-butyl). Diene rubber-styrene copolymer), AAS resin (acrylonitrile-acrylic rubber-styrene copolymer), AES resin (acrylonitrile-ethylene propylene rubber-styrene copolymer) and HIPS (high impact polystyrene) Wait.
  • MBS resin methyl methacrylate-butadiene rubber-styrene copolymer
  • ABS resin acrylonitrile-butyl
  • the auxiliary agent comprises at least one of a stabilizer, a colorant, an antistatic agent, a plasticizer, and a lubricant.
  • the present invention also relates to a method for producing a thermoplastic resin composition according to the present invention, which comprises using a polycarbonate resin, a polybutylene terephthalate resin and an auxiliary agent in a double length to diameter ratio of 50 or less.
  • the screw extruder is melt-kneaded to control the temperature at which the polymer melt exits the twin-screw extruder die to be less than 320 °C.
  • the twin-screw extruder has an aspect ratio of not more than 35, and controls the temperature at which the polymer melt exits the twin-screw extruder die to be less than 300 °C.
  • the inventors of this patent have undergone extensive experiments and have surprisingly discovered that by adding transesterification inhibitors and controlling PBT
  • the end-COOH content while controlling the aspect ratio of the screw and the melt temperature, that is, simultaneously controlling the reaction time and the reaction temperature, can control the degree of transesterification of PC and PBT during the melt-kneading process, thereby controlling the embedding process generated by the transesterification process.
  • the content of the segment copolyester can further control the separation speed of spinodal phase.
  • the final construction of a large number of nanometer-scale dispersed dispersed phase-continuous phase structure can greatly improve the high-speed surface impact performance of PC/PBT system at low temperature.
  • the present invention firstly reduces the transesterification reaction in the PC and PBT resin compositions by controlling the content of the transesterification inhibitor and the content of the end-COOH in the PBT from the material properties; and in combination with the extrusion process (screw length) Optimization of ratio and melt temperature further control reaction time and reaction temperature; thereby reducing the content of PC-PBT block copolyester, accelerating the separation speed of spinodal phase, and constructing a dispersed phase-continuous phase with a large number of nanoscale dispersions
  • the structure ultimately achieves the macroscopic properties of the composition, especially the high-speed surface impact performance at low temperatures.
  • the dispersed phase can absorb a large amount of impact energy by forming a sponge-like multiple void structure when subjected to high-speed surface impact at a low temperature. That is, the resin composition prepared by the present invention exhibits excellent rigidity and heat resistance at normal temperature, and exhibits toughness damage after penetrating the hammer at a low temperature subjected to high load and high speed surface impact, and does not generate more than 10 mm. The above cracks.
  • the present invention has the following beneficial effects:
  • the material composition Firstly, by designing the material composition properties, combined with the optimization of the extrusion process, controlling the degree of transesterification reaction, a special microscopic phase structure can be constructed, and the obtained resin composition has excellent rigidity and modulus, and is subjected to high load at low temperature.
  • the toughness can be broken after the hammer is penetrated, and cracks larger than 10 mm or more are not generated. It was found by transmission electron microscopy that, with the resin composition prepared by the present invention, the dispersed phase can absorb a large amount of impact energy by forming a sponge-like multiple void structure when impacted at a low temperature and high speed surface.
  • Figure 1 is a TEM photograph of a product of Example 1 of the present invention.
  • the thermoplastic resin composition of the present invention is a resin composition of polycarbonate and polybutylene terephthalate, which is heat
  • the plastic polyester is easily transesterified directly during the melt-kneading process to produce a block copolyester.
  • Copolyesters act as compatibilizers for PC and PBT alloys, so much research has focused on how to accelerate or even accelerate the transesterification reaction to enhance the phase interfacial strength of PC and PBT and improve the performance of the resin composition.
  • the inventors of this patent have found through extensive experiments that the presence of block copolyesters affects the phase separation rate of PC and PBT, and the content of block copolyesters can be controlled by controlling the degree of transesterification.
  • the phase separation speed of PC and PBT constructs a dispersed phase-continuous phase structure with a large number of nanoscale dispersions.
  • the dispersed phase is uniformly dispersed in the continuous phase at the nanometer scale (10-500 nm), and the inter-particle distance of the dispersed phase is on the nanometer scale (10-500 nm)
  • the nano-scale dispersed phase spacing makes the stress fields on the dispersed phase mutually Superposition forms macroscopic stresses of the resin composition in whole or in part, and this stress field superposition effect is more intense at low temperatures.
  • Stress-induced voiding can occur when the number of dispersed phases dispersed at the nanometer scale is further increased or by further reducing the phase domain size of the dispersed phase to increase the number of dispersed phases dispersed at the nanometer scale.
  • the continuous phase When subjected to high-speed impact in a low temperature environment, the continuous phase first undergoes shear deformation, and then a tensile stress is applied to the dispersed phase to cause multiple voiding of the dispersed phase to produce a sponge-like structure and absorb a large amount of energy.
  • the resin composition exhibits excellent surface impact properties at a low temperature and high speed.
  • the Ti catalyst remaining in the PBT synthesis process accelerates the transesterification reaction, and the addition of phosphate or phosphite can form a complex with the catalyst, which effectively inhibits the transesterification reaction;
  • the extrusion process In terms of reaction time and reaction temperature, it is an important condition affecting the transesterification reaction, wherein the reaction time is controlled by the aspect ratio of the screw, and the reaction temperature is controlled by the melt temperature. Note that the melt temperature is two concepts with the barrel temperature of the extruder.
  • the melt temperature of the extruder is determined by the barrel temperature of the extruder and the shear heat generation inside the extruder, while the shear heat generation accounts for most of the proportion; It is closely related to screw combination, screw speed, specific torque, barrel temperature and so on.
  • a resin composition having a specific structural period as described above it is preferred to form a structure by spinodal spinodal separation.
  • Compatibilization is preferably carried out by melt-kneading using a strong shear field using a twin-screw extruder.
  • the raw materials used are:
  • the weight average molecular weight of the polycarbonate is 35,000;
  • Polybutylene terephthalate (PBT1) has an intrinsic viscosity of 1.0 dl/g and a terminal-COOH content of 20 meq/kg;
  • the transesterification inhibitor is sodium dihydrogen phosphate
  • the impact modifier was an MBS resin (methyl methacrylate-butadiene rubber-styrene copolymer) having a particle diameter of 300 nm.
  • thermoplastic resin composition was prepared by the following method:
  • Step 1 weighing each component by weight
  • Step 2 the components are thoroughly mixed in a high speed mixer for 20 min to obtain a mixture
  • Step 3 the mixture is introduced from the main feed of the twin-screw extruder, and melt-extruded, cooled, dried, and pelletized to obtain the thermoplastic resin composition; the screw diameter of the twin-screw extruder is 30 mm.
  • the aspect ratio is 32, and the melt temperature is controlled to be 280 to 300 °C.
  • FIG. 1 A TEM photograph of the product of Example 1 is shown in Figure 1.
  • a large amount of PBT is uniformly dispersed in PC in a particle size of about 100 to 150 nm, and the pitch of PBT particles is 100 to 300 nm.
  • Comparative Examples 1 to 5 were used herein.
  • Comparative Example 1 is the effect of the end-COOH content of PBT.
  • the intrinsic viscosity of PBT (PBT2) is 1.0 dl/g and the end-COOH content is 60 meq/kg
  • Comparative Example 2 is the effect of transesterification inhibitor
  • Comparative Example 3 is Effect of screw length to diameter ratio (reaction time)
  • Comparative Example 4 is the influence of melt temperature (reaction temperature)
  • Comparative Example 5 is the influence of microscopic phase structure (co-continuous phase).
  • the weight ratio of the raw materials is shown in Table 1, and the preparation methods are the same as those in Examples 1 to 4.
  • FIG. 2 A TEM photograph of the product of Comparative Example 1 is shown in Fig. 2. As shown in Fig. 2, a large amount of PBT is uniformly dispersed in the PC at a particle size of about 1.0 to 1.5 ⁇ m to form a bicontinuous phase structure.
  • thermoplastic resin composition As shown in Table 1, a total of 9 formulations were melt extruded, pellet cooled, and granulated according to the above preparation method to prepare a thermoplastic resin composition, and the material was dried at 80 ° C for 12 h to ensure the water absorption of the resin before injection molding was ⁇ 0.05%. The physical properties of the respective resin compositions were then tested by injection molding into splines under the same injection molding conditions in accordance with ASTM standards.
  • the tensile strength and elongation were measured according to the test procedure of ASTM D-638, and the tensile speed was 50 mm/min; the flexural strength and the flexural modulus were measured according to the test procedure of ASTM D-790, and the loading speed was 3 mm/min; based on ASTM The D-256 test procedure measures Izod (1/8") notched impact strength at -30 ° C; the heat distortion temperature is determined based on the ASTM D-648 test procedure.
  • a molded article having a length of 100 mm x a width of 100 mm and a thickness of 3 mm was prepared by injection molding, and the surface impact property was measured based on the test degree of ASTM D-3763, the ambient temperature was -40 ° C, and the impact speed was 20 m / s.
  • the crack fracture length after the penetration of the hammer body was measured, and the fracture length was determined to be a ductile fracture with a fracture length of less than 10 mm, and a brittle fracture was determined to be greater than 10 mm.
  • thermoplastic resin composition prepared according to the present invention has Excellent mechanical and thermal properties, and exhibits excellent low temperature impact properties and surface impact properties at low temperatures and high speeds, manifesting as toughness damage.
  • Comparative Example 1 is to change the content of -COOH in the middle of PBT
  • Comparative Example 2 is to change the content of transesterification inhibitor, which obviously changes the microscopic phase structure, so that the size of the dispersed phase domain becomes larger, and the impact performance of low-temperature high-speed surface changes. Poor, the composition exhibits brittle failure.
  • the phase structure of the resin composition was changed by changing the extrusion process (the aspect ratio of the twin-screw extruder and the melt temperature) to form a homogeneous structure (microphase scale ⁇ 50 nm), the low-temperature impact and surface impact properties of the resin composition were also significantly reduced, and the heat resistance was drastically lowered.
  • the invention firstly constructs a special large amount of nanometer-scale dispersed dispersed phase-continuous phase microscopic phase structure through the material component attribute design and the optimization of the extrusion process, and the obtained resin composition has excellent performance.
  • the rigidity and modulus while subjected to high-load, high-speed surface impact at low temperatures, can exhibit toughness damage after penetrating the hammer, and do not produce cracks greater than 10 mm.
  • the dispersed phase can absorb a large amount of impact energy by forming a sponge-like multiple void structure when impacted at a low temperature and high speed surface. That is, the resin composition prepared by the present invention exhibits excellent rigidity and heat resistance at normal temperature, and exhibits toughness damage after penetrating the hammer at a low temperature subjected to high load and high speed surface impact.

Abstract

A reactive thermoplastic resin composition, comprising the following components in portion by mass: 15-85 portions of polycarbonate resin; 15-85 portions of polybutylene terephthalate resin; 0.05-5 portions of ester exchange inhibitor; 0-30 portions of impact modifier; 0-5 portions of additive; the polybutylene terephthalate has an intrinsic viscosity of 0.6-1.5 dl/gr and an end-COOH content of < 50 meq/kg. The present invention, by designing components of the composition, then combining optimization of an extrusion process and controlling the degree of transesterification, constructs a special micro-phase structure, and the obtained resin composition has an excellent stiffness and modulus under a quasi-static state and exhibits an excellent toughness and energy absorption property when subject to a high speed surface impact at a low temperature.

Description

一种反应型热塑性树脂组合物及其制备方法Reactive thermoplastic resin composition and preparation method thereof 技术领域Technical field
本发明涉及一种反应型热塑性树脂组合物及其制备方法,属于高分子材料加工技术领域。The invention relates to a reactive thermoplastic resin composition and a preparation method thereof, and belongs to the technical field of polymer material processing.
背景技术Background technique
近年来,在汽车零部件和运动用品领域,人们对材料受到高速撞击时表现出来的能量吸收能力要求越来越多。比如,汽车仪表板上表面的头部冲击试验;其下边缘的膝盖撞击试验;座椅靠背的身体冲击试验等,均要求被检验的内饰塑料不能碎裂,更不能碎片四溅或出现棱角伤人。汽车外饰件必须满足行人安全保护标准。此外,由于其自身使用环境的需要,对汽车在低温环境下受撞击时的韧性破坏要求也越来越迫切。In recent years, in the field of automotive parts and sporting goods, there has been an increasing demand for energy absorption capacity when materials are subjected to high-speed impact. For example, the head impact test on the surface of the dashboard of the car; the knee impact test on the lower edge; the body impact test of the seat back, etc., all require that the interior plastic to be inspected cannot be broken, and the debris cannot be broken or edged. Injury. Automotive exterior trim must meet pedestrian safety standards. In addition, due to the needs of its own use environment, the toughness damage requirements of the car when it is impacted in a low temperature environment are becoming more and more urgent.
目前,用于制备能量吸收部件的材料主要集中在橡胶增韧体系和PC/PBT体系。比如,中国CN101558121公开了利用长径比(L/D)大于50以上的双螺杆挤出机制备了聚酰胺6和带反应性官能团的聚烯烃弹性体树脂组合物,制备的树脂组合物在微观相态上表现为:纳米尺度分散的聚烯烃弹性体内部包藏了大量的更小纳米尺度的聚酰胺6微团,而在宏观上表现为显著优异的吸能特性,但其室温下的弯曲模量仅为1300MPa;对于PC/PBT体系,中国专利CN 103772934A和CN 101935446A都公开了通过添加官能团化的弹性体兼具界面相容剂和增韧剂的作用,所得PC/PBT树脂组合物的界面强度高,缺口冲击性能优异;美国专利US7235612和日本专利JP2003-286414号公报则都公开了通过spinodal相分离机理构筑结构周期为0.001~1μm或0.01~1μm的两相连续结构,所得树脂组合物的耐热性和拉伸性能优异。Currently, materials used to prepare energy absorbing components are mainly concentrated in rubber toughening systems and PC/PBT systems. For example, CN101558121 discloses that a polyamide elastomer resin composition having a polyamide 6 and a reactive functional group is prepared by using a twin-screw extruder having a ratio of length to diameter (L/D) of more than 50, and the prepared resin composition is microscopically prepared. The phase behavior is as follows: the nano-scale dispersed polyolefin elastomer contains a large number of smaller nano-scale polyamide 6 micelles, and exhibits remarkable excellent energy absorption properties at the macroscopic level, but its bending mode at room temperature. The amount is only 1300 MPa; for the PC/PBT system, Chinese patents CN 103772934A and CN 101935446A both disclose the interface of the obtained PC/PBT resin composition by adding a functionalized elastomer together with an interface compatibilizer and a toughening agent. The high-strength, high-notch impact performance is excellent; and the two-phase continuous structure having a structural period of 0.001 to 1 μm or 0.01 to 1 μm is constructed by a spinodal phase separation mechanism, as disclosed in US Pat. No. 7,523,612 and Japanese Patent No. 2003-286414. Excellent heat resistance and tensile properties.
如前所述,橡胶增韧体系的不足之处在于其常温下的刚性和耐热性能较低,不宜作为结构件使用,而且大量橡胶组分的引入会引发加工性、热稳定性等性能不易平衡的一系列问题;而对于PC/PBT体系,目前主要集中在三个方面:(1)关注缺口冲击性能,对于面冲击性能关注甚少;(2)关注如何利用Spinodal相分离机理构筑双连续相结构;(3)关注PC和PBT的相界面强度。As mentioned above, the disadvantage of the rubber toughening system is that it has low rigidity and heat resistance at room temperature, and is not suitable for use as a structural member, and the introduction of a large amount of rubber components may cause difficulty in processability and thermal stability. A series of problems for balance; for the PC/PBT system, it is mainly concentrated in three aspects: (1) pay attention to the impact performance of the gap, and pay little attention to the surface impact performance; (2) focus on how to construct the double continuous using the Spinodal phase separation mechanism. Phase structure; (3) Pay attention to the phase interface strength of PC and PBT.
发明内容Summary of the invention
针对现有技术中的缺陷,本发明的目的是提供一种反应型热塑性树脂组合物及其 制备方法。In view of the deficiencies in the prior art, an object of the present invention is to provide a reactive thermoplastic resin composition and Preparation.
本发明的目的是通过以下技术方案实现的:The object of the invention is achieved by the following technical solutions:
本发明涉及一种反应型热塑性树脂组合物,其包括按重量份数计的如下组分:The present invention relates to a reactive thermoplastic resin composition comprising the following components in parts by weight:
Figure PCTCN2015070579-appb-000001
Figure PCTCN2015070579-appb-000001
其中,所述聚对苯二甲酸丁二醇酯的特性粘度为0.6~1.5dl/gr,端-COOH含量<50meq/kg。Wherein, the polybutylene terephthalate has an intrinsic viscosity of 0.6 to 1.5 dl/gr and a terminal-COOH content of <50 meq/kg.
PC或PBT的一者形成连续相,另一者形成分散相,分散相的粒子尺寸为0.05~0.5μm或粒子间距离为0.05~0.5μm;优选地,分散相的粒子尺寸为0.05~0.2μm或粒子间距离为0.05~0.2μm。One of PC or PBT forms a continuous phase, and the other forms a dispersed phase, and the dispersed phase has a particle size of 0.05 to 0.5 μm or an interparticle distance of 0.05 to 0.5 μm; preferably, the dispersed phase has a particle size of 0.05 to 0.2 μm. Or the distance between particles is 0.05 to 0.2 μm.
作为优选方案,所述聚碳酸酯树脂为双酚A型聚碳酸酯,其重均分子量为2.0~6.0×104g/mol。Preferably, the polycarbonate resin is a bisphenol A type polycarbonate having a weight average molecular weight of 2.0 to 6.0 × 10 4 g/mol.
作为优选方案,所述聚对苯二甲酸丁二醇酯的特性粘度为1.0~1.3dl/gr,端-COOH含量<10meq/kg。Preferably, the polybutylene terephthalate has an intrinsic viscosity of 1.0 to 1.3 dl/gr and a terminal-COOH content of <10 meq/kg.
作为优选方案,所述酯交换抑制剂为磷酸盐和亚磷酸盐中的一种。Preferably, the transesterification inhibitor is one of a phosphate and a phosphite.
作为优选方案,所述抗冲击改性剂为橡胶改性苯乙烯系树脂,可以列举如MBS树脂(甲基丙烯酸甲酯-丁二烯橡胶-苯乙烯共聚物)、ABS树脂(丙烯腈-丁二烯橡胶-苯乙烯共聚物)、AAS树脂(丙烯腈-丙烯酸橡胶-苯乙烯共聚物)、AES树脂(丙烯腈-乙丙橡胶-苯乙烯共聚物)和HIPS(高抗冲聚苯乙烯)等。Preferably, the impact modifier is a rubber-modified styrene resin, and examples thereof include an MBS resin (methyl methacrylate-butadiene rubber-styrene copolymer) and an ABS resin (acrylonitrile-butyl). Diene rubber-styrene copolymer), AAS resin (acrylonitrile-acrylic rubber-styrene copolymer), AES resin (acrylonitrile-ethylene propylene rubber-styrene copolymer) and HIPS (high impact polystyrene) Wait.
作为优选方案,所述助剂包含稳定剂、着色剂、抗静电剂、增塑剂、润滑剂中的至少一种。Preferably, the auxiliary agent comprises at least one of a stabilizer, a colorant, an antistatic agent, a plasticizer, and a lubricant.
本发明还涉及一种如本发明所述的热塑性树脂组合物的制备方法,其是将聚碳酸酯树脂、聚对苯二甲酸丁二醇酯树脂和助剂利用长径比在50以下的双螺杆挤出机进行熔融混炼,控制聚合物熔体出所述双螺杆挤出机口模时的温度小于320℃。The present invention also relates to a method for producing a thermoplastic resin composition according to the present invention, which comprises using a polycarbonate resin, a polybutylene terephthalate resin and an auxiliary agent in a double length to diameter ratio of 50 or less. The screw extruder is melt-kneaded to control the temperature at which the polymer melt exits the twin-screw extruder die to be less than 320 °C.
作为优选方法,所述双螺杆挤出机的长径比不大于35,控制聚合物熔体出所述双螺杆挤出机口模时的温度小于300℃。As a preferred method, the twin-screw extruder has an aspect ratio of not more than 35, and controls the temperature at which the polymer melt exits the twin-screw extruder die to be less than 300 °C.
本专利的发明人经过大量的试验,惊人地发现通过加入酯交换抑制剂和控制PBT 的端-COOH含量,同时控制螺杆长径比和熔体温度,即同时控制反应时间和反应温度,可以控制熔融混炼过程中PC和PBT的酯交换反应程度,从而控制酯交换过程产生的嵌段共聚酯的含量,可以进一步控制spinodal相分离速度,最终构筑的大量纳米尺度分散的分散相-连续相结构可以极大地改善PC/PBT体系低温下的高速面冲击性能。The inventors of this patent have undergone extensive experiments and have surprisingly discovered that by adding transesterification inhibitors and controlling PBT The end-COOH content, while controlling the aspect ratio of the screw and the melt temperature, that is, simultaneously controlling the reaction time and the reaction temperature, can control the degree of transesterification of PC and PBT during the melt-kneading process, thereby controlling the embedding process generated by the transesterification process. The content of the segment copolyester can further control the separation speed of spinodal phase. The final construction of a large number of nanometer-scale dispersed dispersed phase-continuous phase structure can greatly improve the high-speed surface impact performance of PC/PBT system at low temperature.
基于上述原理,本发明首先从材料属性出发,通过控制酯交换抑制剂的含量和PBT中端-COOH的含量,减少PC和PBT树脂组合物中的酯交换反应;再结合挤出工艺(螺杆长径比和熔体温度)的优化进一步控制反应时间和反应温度;从而减少PC-PBT嵌段共聚酯的含量,加速spinodal相分离速度,构筑出具有大量纳米级尺度分散的分散相-连续相结构,最终达到组合物宏观性能,尤其是低温下的高速面冲击性能的提升。通过透射电子显微镜观察发现,利用本发明制备的树脂组合物,分散相在低温下经历高速面冲击时能通过形成类似海绵状的多重空洞化结构吸收大量冲击能量。即利用本发明制备的树脂组合物在常温下表现优异的刚性和耐热性能,而在低温遭受高负荷、高速度的面冲击时,能在锤体穿透后表现韧性破坏,不产生大于10mm以上的龟裂。Based on the above principle, the present invention firstly reduces the transesterification reaction in the PC and PBT resin compositions by controlling the content of the transesterification inhibitor and the content of the end-COOH in the PBT from the material properties; and in combination with the extrusion process (screw length) Optimization of ratio and melt temperature further control reaction time and reaction temperature; thereby reducing the content of PC-PBT block copolyester, accelerating the separation speed of spinodal phase, and constructing a dispersed phase-continuous phase with a large number of nanoscale dispersions The structure ultimately achieves the macroscopic properties of the composition, especially the high-speed surface impact performance at low temperatures. It was found by transmission electron microscopy that, with the resin composition prepared by the present invention, the dispersed phase can absorb a large amount of impact energy by forming a sponge-like multiple void structure when subjected to high-speed surface impact at a low temperature. That is, the resin composition prepared by the present invention exhibits excellent rigidity and heat resistance at normal temperature, and exhibits toughness damage after penetrating the hammer at a low temperature subjected to high load and high speed surface impact, and does not generate more than 10 mm. The above cracks.
与现有技术相比,本发明具有如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
首先通过材料组分属性设计,再结合挤出工艺的优化,控制酯交换反应程度,可以构筑特殊的微观相态结构,获得的树脂组合物具有优异的刚性和模量,而在低温遭受高负荷、高速度的面冲击时,能在锤体穿透后表现韧性破坏,不产生大于10mm以上的龟裂。通过透射电子显微镜观察发现,利用本发明制备的树脂组合物,分散相在低温高速面冲击时能通过形成类似海绵状的多重空洞化结构吸收大量冲击能量。Firstly, by designing the material composition properties, combined with the optimization of the extrusion process, controlling the degree of transesterification reaction, a special microscopic phase structure can be constructed, and the obtained resin composition has excellent rigidity and modulus, and is subjected to high load at low temperature. When the surface is impacted at a high speed, the toughness can be broken after the hammer is penetrated, and cracks larger than 10 mm or more are not generated. It was found by transmission electron microscopy that, with the resin composition prepared by the present invention, the dispersed phase can absorb a large amount of impact energy by forming a sponge-like multiple void structure when impacted at a low temperature and high speed surface.
附图说明DRAWINGS
通过阅读参照以下附图对非限制性实施例所作的详细描述,本发明的其它特征、目的和优点将会变得更明显:Other features, objects, and advantages of the present invention will become apparent from the Detailed Description of Description
图1为本发明的实施例1的产品的TEM照片;Figure 1 is a TEM photograph of a product of Example 1 of the present invention;
图2为本发明的对比例1的产品的TEM照片。2 is a TEM photograph of the product of Comparative Example 1 of the present invention.
具体实施方式detailed description
下面结合具体实施例对本发明进行详细说明。以下实施例将有助于本领域的技术人员进一步理解本发明,但不以任何形式限制本发明。应当指出的是,对本领域的普通技术人员来说,在不脱离本发明构思的前提下,还可以做出若干变形和改进。这些都属于本发明的保护范围。The invention will now be described in detail in connection with specific embodiments. The following examples are intended to further understand the invention, but are not intended to limit the invention in any way. It should be noted that a number of variations and modifications may be made by those skilled in the art without departing from the inventive concept. These are all within the scope of protection of the present invention.
本发明的热塑性树脂组合物是聚碳酸酯和聚对苯二甲酸丁二醇酯的树脂组合物,热 塑性聚酯在熔融混炼过程中很容易直接发生酯交换反应,产生嵌段共聚酯。共聚酯对PC和PBT合金能起到相容剂的作用,因此大量的研究集中在如何利用甚至加速酯交换反应来增强PC和PBT的相界面强度,改善树脂组合物的性能。事实上,本专利的发明人通过大量的实验发现,嵌段共聚酯的存在会影响PC和PBT的相分离速度,通过控制酯交换反应的程度可以控制嵌段共聚酯的含量,从而控制PC和PBT的相分离速度,构筑出具有大量纳米级尺度分散的分散相-连续相结构。当分散相以纳米尺度(10~500nm)均匀地分散在连续相中,以及分散相的粒间距离为纳米尺度(10~500nm)时,纳米尺度的分散相间距使得分散相上的应力场互相叠加,便形成了树脂组合物整体或局部的宏观应力,而这种应力场叠加效应在低温下表现更强烈。进一步增加纳米尺度分散的分散相数量或者通过进一步减小分散相相畴尺寸以增加纳米尺度分散的分散相数量,都可以发生应力诱导空洞化现象。在低温环境下受到高速冲击时,连续相首先发生剪切变形,随后对分散相施加一个拉伸应力,使分散相发生多重空洞化而产生类似海绵状结构,吸收大量的能量。树脂组合物表现出优异的低温高速时的面冲击性能。The thermoplastic resin composition of the present invention is a resin composition of polycarbonate and polybutylene terephthalate, which is heat The plastic polyester is easily transesterified directly during the melt-kneading process to produce a block copolyester. Copolyesters act as compatibilizers for PC and PBT alloys, so much research has focused on how to accelerate or even accelerate the transesterification reaction to enhance the phase interfacial strength of PC and PBT and improve the performance of the resin composition. In fact, the inventors of this patent have found through extensive experiments that the presence of block copolyesters affects the phase separation rate of PC and PBT, and the content of block copolyesters can be controlled by controlling the degree of transesterification. The phase separation speed of PC and PBT constructs a dispersed phase-continuous phase structure with a large number of nanoscale dispersions. When the dispersed phase is uniformly dispersed in the continuous phase at the nanometer scale (10-500 nm), and the inter-particle distance of the dispersed phase is on the nanometer scale (10-500 nm), the nano-scale dispersed phase spacing makes the stress fields on the dispersed phase mutually Superposition forms macroscopic stresses of the resin composition in whole or in part, and this stress field superposition effect is more intense at low temperatures. Stress-induced voiding can occur when the number of dispersed phases dispersed at the nanometer scale is further increased or by further reducing the phase domain size of the dispersed phase to increase the number of dispersed phases dispersed at the nanometer scale. When subjected to high-speed impact in a low temperature environment, the continuous phase first undergoes shear deformation, and then a tensile stress is applied to the dispersed phase to cause multiple voiding of the dispersed phase to produce a sponge-like structure and absorb a large amount of energy. The resin composition exhibits excellent surface impact properties at a low temperature and high speed.
因此,如何将酯交换反应控制到一个合理的水平是影响PC和PBT低温下高速面冲击性能的关键。首先,原材料方面,PBT合成过程中残留的Ti催化剂会加速酯交换反应,而加入磷酸盐类或亚磷酸盐类可与催化剂形成络合物,有效抑制酯交换反应的发生;其次,挤出工艺方面,反应时间和反应温度是影响酯交换反应的重要条件,其中反应时间通过螺杆长径比控制,反应温度则由熔体温度控制。注意,熔体温度是与挤出机的料筒温度是两个概念。挤出机的熔体温度是由挤出机的料筒温度和挤出机内部的剪切生热两部分决定的,而剪切生热占据了绝大部分的比例;而剪切生热又与螺杆组合、螺杆转速、比扭矩、料筒温度等都密切相关。Therefore, how to control the transesterification reaction to a reasonable level is the key to affect the high-speed surface impact performance of PC and PBT at low temperatures. First, in terms of raw materials, the Ti catalyst remaining in the PBT synthesis process accelerates the transesterification reaction, and the addition of phosphate or phosphite can form a complex with the catalyst, which effectively inhibits the transesterification reaction; secondly, the extrusion process In terms of reaction time and reaction temperature, it is an important condition affecting the transesterification reaction, wherein the reaction time is controlled by the aspect ratio of the screw, and the reaction temperature is controlled by the melt temperature. Note that the melt temperature is two concepts with the barrel temperature of the extruder. The melt temperature of the extruder is determined by the barrel temperature of the extruder and the shear heat generation inside the extruder, while the shear heat generation accounts for most of the proportion; It is closely related to screw combination, screw speed, specific torque, barrel temperature and so on.
为了获得具有特定上述结构周期的树脂组合物,优选利用spinodal旋节线分离来形成结构。优选使用双螺杆挤出机利用强剪切场熔融混炼进行相容化。In order to obtain a resin composition having a specific structural period as described above, it is preferred to form a structure by spinodal spinodal separation. Compatibilization is preferably carried out by melt-kneading using a strong shear field using a twin-screw extruder.
各实施例和对比例得到的产品在进行性能检测时,先制备成100mm×100mm×3mm的样板,然后根据依据ASTMD3763标准进行检测,锤头直径是12.7mm,底部支撑环直径是76mm,试验温度是-40℃,试验速度是20m/s。The products obtained in each of the examples and the comparative examples were prepared into a sample of 100 mm × 100 mm × 3 mm in the performance test, and then tested according to ASTM D3763, the diameter of the hammer head was 12.7 mm, and the diameter of the bottom support ring was 76 mm, the test temperature. It is -40 ° C and the test speed is 20 m / s.
实施例1~4Examples 1 to 4
采用的原材料为:The raw materials used are:
聚碳酸酯的重均分子量为3.5万;The weight average molecular weight of the polycarbonate is 35,000;
聚对苯二甲酸丁二醇酯(PBT1)的特性粘度为1.0dl/g,端-COOH含量20meq/kg; Polybutylene terephthalate (PBT1) has an intrinsic viscosity of 1.0 dl/g and a terminal-COOH content of 20 meq/kg;
酯交换抑制剂为磷酸二氢钠;The transesterification inhibitor is sodium dihydrogen phosphate;
抗冲击改性剂为MBS树脂(甲基丙烯酸甲酯-丁二烯橡胶-苯乙烯共聚物),粒径为300nm。The impact modifier was an MBS resin (methyl methacrylate-butadiene rubber-styrene copolymer) having a particle diameter of 300 nm.
按照表1所示的重量份数取各组分,之后采用如下方法制备所述热塑性树脂组合物:Each component was taken in parts by weight as shown in Table 1, and then the thermoplastic resin composition was prepared by the following method:
步骤1,按照重量份数称取各组分; Step 1, weighing each component by weight;
步骤2,将各组分在高速混合机中充分混合20min,得混合物;Step 2, the components are thoroughly mixed in a high speed mixer for 20 min to obtain a mixture;
步骤3,将混合物从双螺杆挤出机的主喂料进入,经过熔融挤出、冷却、干燥、切粒,即得所述的热塑性树脂组合物;双螺杆挤出机的螺杆直径为30mm,长径比为32,控制熔体温度为280~300℃。Step 3, the mixture is introduced from the main feed of the twin-screw extruder, and melt-extruded, cooled, dried, and pelletized to obtain the thermoplastic resin composition; the screw diameter of the twin-screw extruder is 30 mm. The aspect ratio is 32, and the melt temperature is controlled to be 280 to 300 °C.
实施例1的产品的TEM照片见图1。如图1所示,大量的PBT以100~150nm左右的颗粒尺寸均匀分散在PC中,PBT颗粒间距为100~300nm。A TEM photograph of the product of Example 1 is shown in Figure 1. As shown in Fig. 1, a large amount of PBT is uniformly dispersed in PC in a particle size of about 100 to 150 nm, and the pitch of PBT particles is 100 to 300 nm.
对比例1~5Comparative Example 1 to 5
为了较好地体现上述用于热塑性树脂组合物的特点,在此使用对比例1~5。对比例1是PBT中端-COOH含量的影响,设置PBT(PBT2)的特性粘度为1.0dl/g,端-COOH含量60meq/kg;对比例2是酯交换抑制剂的影响;对比例3是螺杆长径比(反应时间)的影响;对比例4是熔体温度(反应温度)的影响;对比例5是微观相态结构(共连续相)的影响。原料重量比例见表1,制备方法同实施例1~4。In order to better embody the above characteristics for the thermoplastic resin composition, Comparative Examples 1 to 5 were used herein. Comparative Example 1 is the effect of the end-COOH content of PBT. The intrinsic viscosity of PBT (PBT2) is 1.0 dl/g and the end-COOH content is 60 meq/kg; Comparative Example 2 is the effect of transesterification inhibitor; Comparative Example 3 is Effect of screw length to diameter ratio (reaction time); Comparative Example 4 is the influence of melt temperature (reaction temperature); Comparative Example 5 is the influence of microscopic phase structure (co-continuous phase). The weight ratio of the raw materials is shown in Table 1, and the preparation methods are the same as those in Examples 1 to 4.
对比例1的产品的TEM照片见图2。如图2所示,大量的PBT以1.0~1.5μm左右的颗粒尺寸均匀分散在PC中,形成类似双连续相结构。A TEM photograph of the product of Comparative Example 1 is shown in Fig. 2. As shown in Fig. 2, a large amount of PBT is uniformly dispersed in the PC at a particle size of about 1.0 to 1.5 μm to form a bicontinuous phase structure.
如表1所示,共有9个配方按照上述制备方法进行熔融挤出、拉粒冷却、造粒制备热塑性树脂组合物,将物料在80℃干燥12h,保证注塑前树脂的吸水率<0.05%,然后按照ASTM标准,在同一注塑条件下注塑成样条,测试各个树脂组合物的物理性能。其中,基于ASTM D-638的测试程序测定抗拉强度和伸长,拉伸速度50mm/min;基于ASTM D-790的测试程序测定挠曲强度和挠曲模量,加载速度3mm/min;基于ASTM D-256的测试程序测定-30℃时的Izod(1/8”)缺口冲击强度;基于ASTM D-648的测试程序测定热变形温度。As shown in Table 1, a total of 9 formulations were melt extruded, pellet cooled, and granulated according to the above preparation method to prepare a thermoplastic resin composition, and the material was dried at 80 ° C for 12 h to ensure the water absorption of the resin before injection molding was <0.05%. The physical properties of the respective resin compositions were then tested by injection molding into splines under the same injection molding conditions in accordance with ASTM standards. Among them, the tensile strength and elongation were measured according to the test procedure of ASTM D-638, and the tensile speed was 50 mm/min; the flexural strength and the flexural modulus were measured according to the test procedure of ASTM D-790, and the loading speed was 3 mm/min; based on ASTM The D-256 test procedure measures Izod (1/8") notched impact strength at -30 ° C; the heat distortion temperature is determined based on the ASTM D-648 test procedure.
注塑制备长100mmⅹ宽100mmⅹ厚3mm的成形品,基于ASTM D-3763的测试程度测定面冲击性能,环境温度为-40℃,冲击速度为20m/s。测量锤体穿透之后的裂纹断裂长度,将断裂长度小于10mm判定为韧性断裂,大于10mm判定为脆性断裂。A molded article having a length of 100 mm x a width of 100 mm and a thickness of 3 mm was prepared by injection molding, and the surface impact property was measured based on the test degree of ASTM D-3763, the ambient temperature was -40 ° C, and the impact speed was 20 m / s. The crack fracture length after the penetration of the hammer body was measured, and the fracture length was determined to be a ductile fracture with a fracture length of less than 10 mm, and a brittle fracture was determined to be greater than 10 mm.
从实施例1~4的实验结果可以看出,依据本发明制备的热塑性树脂组合物,具有 优异的机械性能和热性能,且表现出优异的低温冲击性能和低温高速时的面冲击性能,表现为韧性破坏。It can be seen from the experimental results of Examples 1 to 4 that the thermoplastic resin composition prepared according to the present invention has Excellent mechanical and thermal properties, and exhibits excellent low temperature impact properties and surface impact properties at low temperatures and high speeds, manifesting as toughness damage.
与对比例1~2相比较,改变树脂组合物的组分性质和含量都能明显改变微观相态结构。对比例1是改变PBT中端-COOH的含量,对比例2是改变酯交换抑制剂的含量,都明显改变了微观相态结构,使得形成的分散相畴尺寸变大,低温高速面冲击性能变差,组合物表现脆性破坏。Compared with Comparative Examples 1 to 2, changing the composition properties and content of the resin composition can significantly change the microscopic phase structure. Comparative Example 1 is to change the content of -COOH in the middle of PBT, and Comparative Example 2 is to change the content of transesterification inhibitor, which obviously changes the microscopic phase structure, so that the size of the dispersed phase domain becomes larger, and the impact performance of low-temperature high-speed surface changes. Poor, the composition exhibits brittle failure.
与对比例3~4相比较,利用改变挤出工艺(双螺杆挤出机长径比和熔体温度)的方式改变树脂组合物的相态结构,使其形成均相结构(微相尺度<50nm),树脂组合物的低温冲击和面冲击性能下降幅度也很明显,且耐热性能急剧下降。Compared with Comparative Examples 3 to 4, the phase structure of the resin composition was changed by changing the extrusion process (the aspect ratio of the twin-screw extruder and the melt temperature) to form a homogeneous structure (microphase scale < 50 nm), the low-temperature impact and surface impact properties of the resin composition were also significantly reduced, and the heat resistance was drastically lowered.
与对比例5相比较,利用同时改变组分配比和挤出工艺使得形成周期性的共连续相结构,最终获得的树脂组合物的低温冲击和面冲击性能也不如本发明提及的分散相-连续相结构。Compared with Comparative Example 5, by simultaneously changing the group distribution ratio and the extrusion process to form a periodic co-continuous phase structure, the resulting low-temperature impact and surface impact properties of the resin composition are also not as the dispersed phase mentioned in the present invention - Continuous phase structure.
表1Table 1
Figure PCTCN2015070579-appb-000002
Figure PCTCN2015070579-appb-000002
综上所述,本发明首先通过材料组分属性设计,再结合挤出工艺的优化,可以构筑特殊的大量纳米尺度分散的分散相-连续相微观相态结构,获得的树脂组合物具有优异 的刚性和模量,而在低温遭受高负荷、高速度的面冲击时,能在锤体穿透后表现韧性破坏,不产生大于10mm以上的龟裂。通过透射电子显微镜观察发现,利用本发明制备的树脂组合物,分散相在低温高速面冲击时能通过形成类似海绵状的多重空洞化结构吸收大量冲击能量。即利用本发明制备的树脂组合物在常温下表现优异的刚性和耐热性能,而在低温遭受高负荷、高速度的面冲击时,能在锤体穿透后表现韧性破坏。In summary, the invention firstly constructs a special large amount of nanometer-scale dispersed dispersed phase-continuous phase microscopic phase structure through the material component attribute design and the optimization of the extrusion process, and the obtained resin composition has excellent performance. The rigidity and modulus, while subjected to high-load, high-speed surface impact at low temperatures, can exhibit toughness damage after penetrating the hammer, and do not produce cracks greater than 10 mm. It was found by transmission electron microscopy that, with the resin composition prepared by the present invention, the dispersed phase can absorb a large amount of impact energy by forming a sponge-like multiple void structure when impacted at a low temperature and high speed surface. That is, the resin composition prepared by the present invention exhibits excellent rigidity and heat resistance at normal temperature, and exhibits toughness damage after penetrating the hammer at a low temperature subjected to high load and high speed surface impact.
以上对本发明的具体实施例进行了描述。需要理解的是,本发明并不局限于上述特定实施方式,本领域技术人员可以在权利要求的范围内做出各种变形或修改,这并不影响本发明的实质内容。 The specific embodiments of the present invention have been described above. It is to be understood that the invention is not limited to the specific embodiments described above, and various modifications and changes may be made by those skilled in the art without departing from the scope of the invention.

Claims (6)

  1. 一种反应型热塑性树脂组合物,其特征在于,包括按重量份数计的如下组分:A reactive thermoplastic resin composition characterized by comprising the following components in parts by weight:
    Figure PCTCN2015070579-appb-100001
    Figure PCTCN2015070579-appb-100001
    其中,所述聚对苯二甲酸丁二醇酯的特性粘度为0.6~1.5dl/gr,端-COOH含量<50meq/kg。Wherein, the polybutylene terephthalate has an intrinsic viscosity of 0.6 to 1.5 dl/gr and a terminal-COOH content of <50 meq/kg.
  2. 如权利要求1所述的反应型热塑性树脂组合物,其特征在于,所述聚碳酸酯树脂为双酚A型聚碳酸酯,其重均分子量为2.0~6.0×104g/mol。The reaction type thermoplastic resin composition according to claim 1, wherein the polycarbonate resin is a bisphenol A type polycarbonate having a weight average molecular weight of 2.0 to 6.0 × 10 4 g/mol.
  3. 如权利要求1所述的反应型热塑性树脂组合物,其特征在于,所述聚对苯二甲酸丁二醇酯的特性粘度为1.0~1.3dl/gr,端-COOH含量<10meq/kg。The reactive thermoplastic resin composition according to claim 1, wherein the polybutylene terephthalate has an intrinsic viscosity of 1.0 to 1.3 dl/gr and a terminal-COOH content of <10 meq/kg.
  4. 如权利要求1所述的反应型热塑性树脂组合物,其特征在于,所述酯交换抑制剂为磷酸盐和亚磷酸盐中的一种。The reactive thermoplastic resin composition according to claim 1, wherein the transesterification inhibitor is one of a phosphate and a phosphite.
  5. 如权利要求1所述的热塑性树脂组合物,其特征在于,所述助剂包含稳定剂、着色剂、抗静电剂、增塑剂、润滑剂中的至少一种。The thermoplastic resin composition according to claim 1, wherein the auxiliary agent comprises at least one of a stabilizer, a colorant, an antistatic agent, a plasticizer, and a lubricant.
  6. 一种如权利要求1所述的热塑性树脂组合物的制备方法,其特征在于,是将聚碳酸酯树脂、聚对苯二甲酸丁二醇酯树脂和助剂利用长径比在50以下的双螺杆挤出机进行熔融混炼,控制聚合物熔体出所述双螺杆挤出机口模时的温度小于320℃。 A method for producing a thermoplastic resin composition according to claim 1, wherein the polycarbonate resin, the polybutylene terephthalate resin, and the auxiliary agent are doubled having an aspect ratio of 50 or less. The screw extruder is melt-kneaded to control the temperature at which the polymer melt exits the twin-screw extruder die to be less than 320 °C.
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