WO2019233017A1 - Modified polyphenylene ether foam bead, preparation method and application thereof - Google Patents

Modified polyphenylene ether foam bead, preparation method and application thereof Download PDF

Info

Publication number
WO2019233017A1
WO2019233017A1 PCT/CN2018/111453 CN2018111453W WO2019233017A1 WO 2019233017 A1 WO2019233017 A1 WO 2019233017A1 CN 2018111453 W CN2018111453 W CN 2018111453W WO 2019233017 A1 WO2019233017 A1 WO 2019233017A1
Authority
WO
WIPO (PCT)
Prior art keywords
parts
polyphenylene ether
foamed
modified polyphenylene
mixing
Prior art date
Application number
PCT/CN2018/111453
Other languages
French (fr)
Chinese (zh)
Inventor
冯云平
Original Assignee
广东奔迪新材料科技有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 广东奔迪新材料科技有限公司 filed Critical 广东奔迪新材料科技有限公司
Publication of WO2019233017A1 publication Critical patent/WO2019233017A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/12Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
    • C08J9/122Hydrogen, oxygen, CO2, nitrogen or noble gases
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/0061Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof characterized by the use of several polymeric components
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/0095Mixtures of at least two compounding ingredients belonging to different one-dot groups
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2203/00Foams characterized by the expanding agent
    • C08J2203/06CO2, N2 or noble gases
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2203/00Foams characterized by the expanding agent
    • C08J2203/08Supercritical fluid
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/04Homopolymers or copolymers of ethene
    • C08J2323/06Polyethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/10Homopolymers or copolymers of propene
    • C08J2323/12Polypropene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2351/00Characterised by the use of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
    • C08J2351/04Characterised by the use of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers grafted on to rubbers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2355/00Characterised by the use of homopolymers or copolymers, obtained by polymerisation reactions only involving carbon-to-carbon unsaturated bonds, not provided for in groups C08J2323/00 - C08J2353/00
    • C08J2355/02Acrylonitrile-Butadiene-Styrene [ABS] polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2371/00Characterised by the use of polyethers obtained by reactions forming an ether link in the main chain; Derivatives of such polymers
    • C08J2371/08Polyethers derived from hydroxy compounds or from their metallic derivatives
    • C08J2371/10Polyethers derived from hydroxy compounds or from their metallic derivatives from phenols
    • C08J2371/12Polyphenylene oxides
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2377/00Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2423/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2423/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2423/04Homopolymers or copolymers of ethene
    • C08J2423/06Polyethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2423/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2423/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2423/10Homopolymers or copolymers of propene
    • C08J2423/12Polypropene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2451/00Characterised by the use of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
    • C08J2451/04Characterised by the use of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers grafted on to rubbers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2455/00Characterised by the use of homopolymers or copolymers, obtained by polymerisation reactions only involving carbon-to-carbon unsaturated bonds, not provided for in groups C08J2423/00 - C08J2453/00
    • C08J2455/02Acrylonitrile-Butadiene-Styrene [ABS] polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2477/00Characterised by the use of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2491/00Characterised by the use of oils, fats or waxes; Derivatives thereof
    • C08J2491/06Waxes

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

Disclosed is a formula of a modified polyphenylene ether foam bead, and a preparation method and an application thererof. The formula comprises the following components, in parts by weight: 30-90 parts of polyphenylene ether, 30-90 parts of modified polymer, 5-30 parts of a compatibilizer, 5-30 parts of a toughening agent, 5-20 parts of a flame retardant, 1-5 parts of an antioxidant, 1-5 parts of a secondary antioxidant, 1-3 parts of a lubricant, 1-3 parts of a coupling agent, 1-10 parts of a dispersant, and 2-6 parts of an inorganic nano-nucleating agent material. The invention can be used to produce a foam bead that is uniformly foamed, having large magnification, a high closed-cell ratio, uniform and fine cells, and that is not easy to shrink and collapse. The production of the modified polyphenylene ether foam bead is completed using fast, safe, energy-efficient pre-foaming equipment and processing.

Description

[根据细则37.2由ISA制定的发明名称] 一种改性聚苯醚发泡珠粒、制备方法及其应用[Name of invention formulated by ISA according to Rule 37.2] A modified polyphenylene ether foaming bead, preparation method and application thereof 技术领域Technical field
本发明涉及高分子材料技术领域,具体是一种改性聚苯醚发泡珠粒的配方、制备方法及其应用。The invention relates to the technical field of polymer materials, in particular to a formula, a preparation method and applications of modified polyphenylene ether foamed beads.
背景技术Background technique
近20多年来,各国汽车制造商都十分重视汽车轻量化的工作,投入大量的人力和资金进行研究,汽车轻量化取得了显著的成就,这主要归功于材料工程领域的科技进步。首先是诸多高强度轻质材料的开发及在汽车制造中的应用,取代了不少传统的钢铁制件;其次是新的成形工艺,不断涌现,优化了工件结构,大大减少了材料消耗。汽车轻量化目的的实现主要依靠材料的更新换代和加工技术的创新,认识新材料才能更新加工工艺,创造新的加工技术来实现目的。In the past 20 years, automobile manufacturers of various countries have attached great importance to the lightweighting of automobiles, invested a lot of manpower and funds for research, and achieved significant achievements in automotive lightweighting, mainly due to scientific and technological progress in the field of materials engineering. The first is the development of many high-strength lightweight materials and their application in automobile manufacturing, which has replaced many traditional steel parts; the second is the new forming process, which continues to emerge, optimizes the workpiece structure, and greatly reduces material consumption. The realization of lightweighting of automobiles mainly depends on the upgrading of materials and the innovation of processing technology. Knowledge of new materials can update the processing technology and create new processing technologies to achieve the purpose.
我国与其他国家相比,在这方面的研究还不够先进,应该投入更多的精力来发展此项工艺,即改变汽车的制造材料,又改变汽车的部分零件和结构设计,技术与材料相结合,推进汽车轻量化的发展。Compared with other countries, China's research in this area is not advanced enough, and more efforts should be invested to develop this process, that is, changing the manufacturing materials of automobiles, and changing some parts and structural designs of automobiles, combining technology and materials. To promote the development of lightweight vehicles.
电动汽车的电池箱作为纯电动汽车动力电池总成的承重与保护装置,是动力电池箱总成的关键组成部分。纯电动汽车装配大量的动力电池来满足电动汽车续航里程的要求,往往动力电池箱总成就要占整车总质量的30%-40%。而各大电池厂商目前大多使用厚重的箱体式的电池箱来装载动力电池,这无形中增加了纯电动汽车的整体质量。因此,在满足电池箱动静态性能、密封防水性、碰撞安全性等基本的要求的基础上,需对纯电动汽车的电池箱结构进行优化设计从而实现其轻量化设计,对推进纯电动汽车的快速发展具有重要的意义。The battery box of an electric vehicle is a key component of the power battery box assembly as a load-bearing and protection device for the battery pack of a pure electric vehicle. Pure electric vehicles are equipped with a large number of power batteries to meet the requirements of electric vehicle mileage. Often, the total achievement of the power battery box accounts for 30% -40% of the total mass of the vehicle. The major battery manufacturers currently use heavy box-type battery boxes to load power batteries, which virtually increases the overall quality of pure electric vehicles. Therefore, on the basis of meeting the basic requirements of battery box dynamic and static performance, waterproofness, and collision safety, the battery box structure of pure electric vehicles needs to be optimized to achieve its lightweight design. Rapid development is of great significance.
电动汽车的电池箱作为电动汽车所载有的动力源是电动汽车的关键部件,其性能的优劣将对电动汽车的应用前景产生重大影响,动力电池使用环 境一般都比较差,电池箱体作为动力电池的防护零件,需要满足诸多功能需求。在箱体结构设计上,需要考虑以下因素:耐振动强度和疲劳耐久性能;耐冲击性能,要求箱体外部及内部经历冲击不应有机械损坏、变形和紧固部位的松动现象;碰撞安全性能,车辆在发生正面碰撞、侧面碰撞及后碰撞过程中对电池箱体可能造成的挤压破坏而采取的有效保护措施;密封性能,电池位于车身底板下方,在车身外侧,且离路面很近,其防水、防尘的密封要求必不可少;防腐性能,电池的位置极易沾粘雨水、泥浆,是腐蚀重灾区,其防腐性能要求应很高;耐热性能,电池工作时产生较高的热量,防护箱体的材料必须有耐高温性能,轻量化,考虑到车辆能源的过量消耗和大气的污染,电池箱体愈轻愈好。所以现有传统方法是采用易于成型的金属箱体(如铝合金),共聚PP、m-PPE高强度塑料材料制作。The battery box of an electric vehicle as a power source carried by an electric vehicle is a key component of an electric vehicle. The performance of the battery box will have a significant impact on the application prospects of electric vehicles. The power battery environment is generally poor. The battery box is used as The protective parts of power batteries need to meet many functional requirements. In the design of the cabinet structure, the following factors need to be considered: vibration resistance and fatigue durability; impact resistance, which requires that the outside and inside of the cabinet undergo shock without mechanical damage, deformation and loosening of the fastening parts; collision safety performance , Effective protection measures taken by the vehicle during the frontal collision, side collision, and rear collision that may cause crush damage to the battery box; sealing performance, the battery is located below the body floor, outside the body, and close to the road, Its waterproof and dustproof sealing requirements are indispensable; anti-corrosion performance, the location of the battery is very easy to stick to rain, mud, is a severely corroded area, its anti-corrosion performance requirements should be high; heat resistance, high battery performance during work Heat, the material of the protective box must have high temperature resistance and light weight. Considering the excessive consumption of vehicle energy and atmospheric pollution, the lighter the battery box, the better. Therefore, the existing traditional method is to use an easily formed metal box (such as an aluminum alloy) and copolymerize PP and m-PPE high-strength plastic materials.
作为改性工程塑料聚苯醚(m-PPE),比重1.07g/cm3;其分子结构决定了其具有良好的热性能,它的玻璃化转变温度(Tg)可达210℃,在较宽的温度范围内能够保持优良的力学性能、电性能、保温性能,阻燃性能,并具有良好的耐热水和耐水蒸气性能。As a modified engineering plastic polyphenylene ether (m-PPE), its specific gravity is 1.07g / cm3; its molecular structure determines its good thermal properties. Its glass transition temperature (Tg) can reach 210 ° C. In the temperature range, it can maintain excellent mechanical properties, electrical properties, thermal insulation properties, flame retardant properties, and has good resistance to hot water and water vapor.
高性能聚苯醚树脂作为基本材料,其强度可达70MPa左右,大约是聚乙烯的3倍,弹性模量大于2000MPa,材料的抗冲击性能大于430J/m(Izod试验方法)。热变形温度高达120℃,线膨胀系数大约1.0--2.0X106℃,低于聚乙烯和聚丙烯,因此产品的尺寸稳定好,它的耐蠕变性能是五大工程塑料中最好的,长期使用强度具有较高的可靠性,聚苯醚材料还具有本征的阻燃性,且属于低烟无卤环保型阻燃,树脂本身的耐酸碱、耐水,卫生性能比较好。As a basic material, high-performance polyphenylene ether resin has a strength of about 70 MPa, about three times that of polyethylene, an elastic modulus of more than 2000 MPa, and an impact resistance of the material greater than 430 J / m (Izod test method). The heat distortion temperature is as high as 120 ℃, and the linear expansion coefficient is about 1.0--2.0X106 ℃, which is lower than that of polyethylene and polypropylene. Therefore, the size of the product is stable and its creep resistance is the best among the five engineering plastics. The strength has high reliability, the polyphenylene ether material also has intrinsic flame retardancy, and is a low-smoke, halogen-free and environmentally friendly flame retardant. The resin itself is acid and alkali resistant, water resistant, and has good hygienic performance.
但高性能聚苯醚树脂分子键刚性大,玻璃化转化温度高,不易取向,制品内残余内应力较高,熔融流动性差,加工困难,价格高等缺点。因此,通常采用掺混等合金化方法对PPE改性,并通过加入发泡剂,生产改性聚苯醚 的发泡材料。However, the high-performance polyphenylene ether resin has large molecular bonds, high glass transition temperature, difficult orientation, high residual internal stress in the product, poor melt fluidity, difficult processing, and high price. Therefore, PPE is usually modified by alloying methods such as blending, and by adding a foaming agent, a modified polyphenylene ether foam material is produced.
发明专利CN 1041165A公开一种聚苯醚和乙烯基芳香族化合物制造的可发泡聚合物及其制备方法和应用,发明是用一步法制备可发泡聚合物的方法,即在聚合过程中加入发泡剂。将水放入带有搅拌器的密封压力釜中,并在其中溶入悬浮剂,将含有己溶解的过氧苯甲酸和过苯甲酸叔丁酯的聚苯醚和苯乙烯加入到混合物中。将该反应混合物加热搅拌,然后加热至一定温度,此时在一定压力下加入戊烷。再过一定时间后,将悬浮聚合物筛分并干燥。干珠的戊烷含量为6-7%。将该物用蒸汽预发泡得到体积密度为40克/升。由该发泡聚合物制备的泡沫材料较好地用于热绝缘材料。该方法是在聚合过程中加入发泡剂,是一步法制备可发泡聚合物的方法。该方法工艺复杂,发泡珠粒粒径和珠粒气体含量控制困难,并且粒径的分布不均匀状况。Invention patent CN1041165A discloses a foamable polymer made of polyphenylene ether and vinyl aromatic compound, and a preparation method and application thereof. The invention is a method for preparing a foamable polymer by a one-step method, that is, it is added in the polymerization process. Foaming agent. Water was placed in a sealed autoclave with a stirrer, and a suspending agent was dissolved therein, and polyphenylene ether and styrene containing dissolved peroxybenzoic acid and t-butyl perbenzoate were added to the mixture. The reaction mixture was heated with stirring and then heated to a certain temperature, at which time pentane was added under a certain pressure. After a certain period of time, the suspended polymer is sieved and dried. The pentane content of the dry beads is 6-7%. This was pre-foamed with steam to obtain a bulk density of 40 g / l. A foam material prepared from the foamed polymer is preferably used for a thermal insulation material. The method is to add a foaming agent in the polymerization process, and is a one-step method for preparing a foamable polymer. The method is complicated in process, it is difficult to control the particle size and gas content of the beads, and the particle size distribution is not uniform.
发明内容Summary of the Invention
本发明的目的在于提供一种改性聚苯醚发泡珠粒的配方、制备方法及其应用,以解决上述背景技术中提出的问题。The purpose of the present invention is to provide a formula, a preparation method and an application of a modified polyphenylene ether foamed bead, so as to solve the problems raised in the background art described above.
为实现上述目的,本发明提供如下技术方案:To achieve the above objective, the present invention provides the following technical solutions:
一种改性聚苯醚发泡珠粒的配方;由包含以下重量份的组分制成:聚苯醚30-90份、改性聚合物30-90份、相容剂5-30份、增韧剂5-30份、阻燃剂5-20份、抗氧剂1-5份、助抗氧剂1-5份、润滑剂1-3份、偶联剂1--3份、分散剂1--10份、无机纳米成核剂材料2-6份。A formula of modified polyphenylene ether foam beads; made of the following components by weight: 30-90 parts of polyphenylene ether, 30-90 parts of modified polymer, 5-30 parts of compatibilizer, 5-30 parts of toughener, 5-20 parts of flame retardant, 1-5 parts of antioxidant, 1-5 parts of auxiliary antioxidant, 1-3 parts of lubricant, 1-3 parts of coupling agent, dispersion 1-10 parts of agent, 2-6 parts of inorganic nano nucleating agent material.
一种改性聚苯醚发泡珠粒的制备方法;包括如下步骤:A method for preparing modified polyphenylene ether foamed beads, including the following steps:
步骤一:材料改性,以聚苯醚材料为基料,加入改性聚合物,相容剂,无机纳米材料和有关助剂,混合加热,挤出得到发泡改性聚苯醚材料;Step 1: material modification, using polyphenylene ether material as the base material, adding modified polymer, compatibilizer, inorganic nano material and related auxiliary agents, mixing and heating, and extruding to obtain foamed modified polyphenylene ether material;
步骤二:水下切粒:物料按配方加入在高速混合机混合均匀,投入双、三螺杆挤出混合设备,高温熔融挤出物料,与水下切粒设备配合进行水下切粒,使得切出的颗粒粒径大小均匀,粒径0.3~6mm,颗粒形状圆度高,表面光 滑;Step 2: Underwater pelletizing: Add the materials according to the formula and mix them evenly in a high-speed mixer. Put in twin or three-screw extrusion mixing equipment to melt the materials at high temperature. Use the underwater pelletizing equipment to perform underwater pelletization to make the pellets cut out. Uniform particle size, particle size 0.3 ~ 6mm, high roundness of particle shape, smooth surface;
步骤三:预发泡粒子:在预发泡珠粒成型设备中加入超临界流体(二氧化碳,氮气),将水下切出的粒子,以高频加热方式,在120~250℃的温度下,高压喷入到预发泡珠粒成型设备中,通过气体渗透溶解,压力释放,冷却降温等过程,用高效节能的预发泡加工设备和工艺来完成改性聚苯醚材料发泡珠粒的生产,发泡倍率3-30倍,制造出适合发泡均匀,倍率大,闭孔率高,泡孔均匀细密,不容易收缩塌陷的发泡珠粒;使其达到要求发泡倍率的发泡粒子。Step 3: Pre-expanded particles: Add supercritical fluid (carbon dioxide, nitrogen) to the pre-expanded bead molding equipment, and cut the particles that are cut out underwater under high-frequency heating at a temperature of 120-250 ° C under high pressure. Sprayed into the pre-expanded bead molding equipment, through the processes of gas infiltration and dissolution, pressure release, cooling and cooling, etc., the production of modified polyphenylene ether foamed beads is completed with high-efficiency and energy-saving pre-expanded processing equipment and processes. , Foaming ratio of 3-30 times, making foaming beads suitable for uniform foaming, large magnification, high closed cell ratio, uniform and fine cells, and not easy to shrink and collapse; make it reach the required foaming ratio of foamed particles .
一种改性聚苯醚发泡珠粒在轻量化动力电池箱的应用;利用高效加热的高频技术成型设备,预发泡好的一定发泡倍率的发泡粒子风送进入模具,发泡粒子充满模具后,通过高频加热,加热温度高,发泡珠粒从里到外加热温度均匀,保证发泡制品质量;发泡粒子经加热熔接后,迅速冷却成型脱模,得到电动汽车塑料泡沫珠粒模压锂电电池箱制品;所述成型温度需要150℃,压力需要0.25MPa。Application of a modified polyphenylene ether foamed bead in a lightweight power battery box; using high-frequency heating molding equipment with high efficiency, pre-foamed foamed particles with a certain expansion ratio are blown into a mold and foamed After the particles are filled in the mold, the heating temperature is high through high-frequency heating, and the foamed beads are heated uniformly from the inside to the outside to ensure the quality of the foamed products. After the foamed particles are heated and welded, they are quickly cooled and molded to obtain the plastic of the electric vehicle. Foam beads are molded into lithium battery box products; the molding temperature needs to be 150 ° C, and the pressure needs to be 0.25 MPa.
作为本发明进一步的方案:所述改性聚合物是由ABS、PE、PPS、PA、HIPS、PP、BS以及GPPS按照等重量混合制造而成。As a further solution of the present invention, the modified polymer is manufactured by mixing ABS, PE, PPS, PA, HIPS, PP, BS and GPPS according to equal weight.
作为本发明再进一步的方案:所述相容剂是由PP-g-MAH、SEBS-g-MAH、PE-g-MAH、EPDM以及POE-g-GMA按照等重量混合制造而成。As a further solution of the present invention, the compatibilizer is made of PP-g-MAH, SEBS-g-MAH, PE-g-MAH, EPDM, and POE-g-GMA according to equal weight.
作为本发明再进一步的方案:所述增韧剂是由SBS、SEBS、聚丁烯、LCP、EPDM以及聚烯烃弹性体按照等重量混合制造而成。As a still further solution of the present invention, the toughening agent is made by mixing SBS, SEBS, polybutene, LCP, EPDM, and polyolefin elastomer according to equal weight.
作为本发明再进一步的方案:所述阻燃剂是由磷酸酯类的阻燃剂和无机纳米阻燃剂复配按照等重量混合制造而成;所述无机纳米阻燃剂:纳米氢氧化铝、纳米氢氧化镁、红磷、硼酸锌、纳米氧化锑、纳米钼化合物、层状硅酸盐和无水碳酸镁按照等重量混合制造而成。As a still further solution of the present invention, the flame retardant is prepared by mixing phosphate ester flame retardant and inorganic nano flame retardant in equal weight; the inorganic nano flame retardant: nano aluminum hydroxide , Nano-magnesium hydroxide, red phosphorus, zinc borate, nano-antimony oxide, nano-molybdenum compound, layered silicate and anhydrous magnesium carbonate are mixed and produced according to equal weight.
作为本发明再进一步的方案:所述抗氧剂为抗氧剂1010;助抗氧剂为助 抗氧剂168,润滑剂为液体石蜡,偶联剂是由硅烷偶联剂、钛酸酯偶联剂和铝酸偶联剂按照等重量混合制造而成,分散剂是由聚烯烃类超分散剂、聚醚型超分散剂以及聚丙烯酸酯型超分散剂按照等重量混合制造而成。As a further solution of the present invention: the antioxidant is antioxidant 1010; the auxiliary antioxidant is auxiliary antioxidant 168; the lubricant is liquid paraffin; and the coupling agent is a silane coupling agent and a titanate coupling agent. The cross-linking agent and the aluminate coupling agent are produced by mixing at equal weights. The dispersant is produced by mixing polyolefin-based hyperdispersants, polyether-based hyperdispersants, and polyacrylate-based hyperdispersants at equal weights.
与现有技术相比,本发明的有益效果是:本发明可以制造出适合发泡均匀,倍率大,闭孔率高,泡孔均匀细密,不容易收缩塌陷的发泡珠粒;快捷安全高效节能的预发泡加工设备和工艺来完成发泡改性聚苯醚发泡珠粒的生产;根据发泡珠粒软化温度比较高,创新开发加热高效的高频技术设备,改变现有的以蒸汽为加热介质的加热方式,成型压力较低,生产安全快捷。Compared with the prior art, the present invention has the beneficial effects that the present invention can produce foamed beads suitable for uniform foaming, large magnification, high closed cell ratio, uniform and fine cells, and difficult to shrink and collapse; fast, safe and efficient Energy-saving pre-foaming processing equipment and processes to complete the production of foamed modified polyphenylene ether foam beads; according to the relatively high softening temperature of foamed beads, innovatively develop heating and high-efficiency high-frequency technical equipment to change the existing Steam is the heating method of the heating medium, the forming pressure is low, and the production is safe and fast.
具体实施方式Detailed ways
下面结合具体实施方式对本发明的技术方案作进一步详细地说明。The technical solution of the present invention will be further described in detail in combination with specific embodiments below.
实施例1Example 1
一种改性聚苯醚发泡珠粒的配方;由包含以下重量份的组分制成:聚苯醚30-90份、改性聚合物90份、相容剂30份、增韧剂30份、阻燃剂20份、抗氧剂5份、助抗氧剂5份、润滑剂3份、偶联剂3份、分散剂10份、无机纳米成核剂材料6份。A formula of modified polyphenylene ether foam beads; made of the following components by weight: 30-90 parts of polyphenylene ether, 90 parts of modified polymer, 30 parts of compatibilizer, and 30 of toughening agent Parts, 20 parts flame retardants, 5 parts antioxidants, 5 parts auxiliary antioxidants, 3 parts lubricants, 3 parts coupling agents, 10 parts dispersants, 6 parts inorganic nucleating agent materials.
一种改性聚苯醚发泡珠粒的制备方法;包括如下步骤:A method for preparing modified polyphenylene ether foamed beads, including the following steps:
步骤一:材料改性,以聚苯醚材料为基料,加入改性聚合物,相容剂,无机纳米材料和有关助剂,混合加热,挤出得到发泡改性聚苯醚材料;Step 1: material modification, using polyphenylene ether material as the base material, adding modified polymer, compatibilizer, inorganic nano material and related auxiliary agents, mixing and heating, and extruding to obtain foamed modified polyphenylene ether material;
步骤二:水下切粒:物料按配方加入在高速混合机混合均匀,投入双、三螺杆挤出混合设备,高温熔融挤出物料,与水下切粒设备配合进行水下切粒,使得切出的颗粒粒径大小均匀,粒径6mm,颗粒形状圆度高,表面光滑;Step 2: Underwater pelletizing: Add the materials according to the formula and mix them evenly in a high-speed mixer. Put in twin or three-screw extrusion mixing equipment to melt the materials at high temperature. Use the underwater pelletizing equipment to perform underwater pelletization to make the pellets cut out. Uniform particle size, particle diameter 6mm, high roundness of particle shape, smooth surface;
步骤三:预发泡粒子:在预发泡珠粒成型设备中加入超临界流体(二氧化碳,氮气),将水下切出的粒子,以高频加热方式,在250℃的温度下,高压喷入到预发泡珠粒成型设备中,通过气体渗透溶解,压力释放,冷却降温 等过程,用高效节能的预发泡加工设备和工艺来完成改性聚苯醚材料发泡珠粒的生产,发泡倍率30倍,制造出适合发泡均匀,倍率大,闭孔率高,泡孔均匀细密,不容易收缩塌陷的发泡珠粒;使其达到要求发泡倍率的发泡粒子。Step 3: Pre-expanded particles: Supercritical fluid (carbon dioxide, nitrogen) is added to the pre-expanded bead molding equipment, and the particles cut out underwater are sprayed under high pressure at a temperature of 250 ° C by high-frequency heating. In the pre-expanded bead molding equipment, through the processes of gas infiltration and dissolution, pressure release, cooling and cooling, etc., the production of modified polyphenylene ether foamed beads is completed with efficient and energy-saving pre-expanded processing equipment and processes. The foaming ratio is 30 times, and the foaming beads suitable for uniform foaming, large magnification, high closed cell ratio, uniform and fine cells, and difficult to shrink and collapse are produced;
一种改性聚苯醚发泡珠粒在轻量化动力电池箱的应用;利用高效加热的高频技术成型设备,预发泡好的一定发泡倍率的发泡粒子风送进入模具,发泡粒子充满模具后,通过高频加热,加热温度高,发泡珠粒从里到外加热温度均匀,保证发泡制品质量;发泡粒子经加热熔接后,迅速冷却成型脱模,得到电动汽车塑料泡沫珠粒模压锂电电池箱制品;所述成型温度需要150℃,压力需要0.25MPa。Application of a modified polyphenylene ether foamed bead in a lightweight power battery box; using high-frequency heating molding equipment with high efficiency, pre-foamed foamed particles with a certain expansion ratio are blown into a mold and foamed After the particles are filled in the mold, the heating temperature is high through high-frequency heating, and the foamed beads are heated uniformly from the inside to the outside to ensure the quality of the foamed products. After the foamed particles are heated and welded, they are quickly cooled and molded to obtain the plastic of the electric vehicle Foam beads are molded into lithium battery box products; the molding temperature needs to be 150 ° C, and the pressure needs to be 0.25 MPa.
实施例2Example 2
一种改性聚苯醚发泡珠粒的配方;由包含以下重量份的组分制成:聚苯醚30份、改性聚合物30份、相容剂5份、增韧剂5份、阻燃剂5份、抗氧剂1份、助抗氧剂1份、润滑剂1份、偶联剂1份、分散剂1份、无机纳米成核剂材料2份。A formula of modified polyphenylene ether foam beads; made of the following components by weight: 30 parts polyphenylene ether, 30 parts modified polymer, 5 parts compatibilizer, 5 parts toughener, 5 parts flame retardant, 1 part antioxidant, 1 part auxiliary antioxidant, 1 part lubricant, 1 part coupling agent, 1 part dispersant, and 2 parts inorganic inorganic nucleating agent material.
一种改性聚苯醚发泡珠粒的制备方法;包括如下步骤:A method for preparing modified polyphenylene ether foamed beads, including the following steps:
步骤一:材料改性,以聚苯醚材料为基料,加入改性聚合物,相容剂,无机纳米材料和有关助剂,混合加热,挤出得到发泡改性聚苯醚材料;Step 1: material modification, using polyphenylene ether material as the base material, adding modified polymer, compatibilizer, inorganic nano material and related auxiliary agents, mixing and heating, and extruding to obtain foamed modified polyphenylene ether material;
步骤二:水下切粒:物料按配方加入在高速混合机混合均匀,投入双、三螺杆挤出混合设备,高温熔融挤出物料,与水下切粒设备配合进行水下切粒,使得切出的颗粒粒径大小均匀,粒径0.3,颗粒形状圆度高,表面光滑;Step 2: Underwater pelletizing: Add the materials according to the formula and mix them evenly in a high-speed mixer. Put in twin or three-screw extrusion mixing equipment to melt the materials at high temperature. Use the underwater pelletizing equipment to perform underwater pelletization to make the pellets cut out. Uniform particle size, particle size 0.3, high roundness of particle shape, smooth surface;
步骤三:预发泡粒子:在预发泡珠粒成型设备中加入超临界流体(二氧化碳,氮气),将水下切出的粒子,以高频加热方式,在120℃的温度下,高压喷入到预发泡珠粒成型设备中,通过气体渗透溶解,压力释放,冷却降温等过程,用高效节能的预发泡加工设备和工艺来完成改性聚苯醚材料发泡珠粒的生产,发泡倍率3倍,制造出适合发泡均匀,倍率大,闭孔率高,泡孔 均匀细密,不容易收缩塌陷的发泡珠粒;使其达到要求发泡倍率的发泡粒子。Step 3: Pre-expanded particles: Supercritical fluid (carbon dioxide, nitrogen) is added to the pre-expanded bead molding equipment, and the particles cut out underwater are sprayed under high pressure at a temperature of 120 ° C by means of high-frequency heating. In the pre-expanded bead molding equipment, through the processes of gas infiltration and dissolution, pressure release, cooling and cooling, etc., the production of modified polyphenylene ether foamed beads is completed with efficient and energy-saving pre-expanded processing equipment and processes. The foaming ratio is 3 times, and the foaming beads suitable for uniform foaming, large magnification, high closed cell ratio, uniform and fine cells, and difficult to shrink and collapse are produced;
一种改性聚苯醚发泡珠粒在轻量化动力电池箱的应用;利用高效加热的高频技术成型设备,预发泡好的一定发泡倍率的发泡粒子风送进入模具,发泡粒子充满模具后,通过高频加热,加热温度高,发泡珠粒从里到外加热温度均匀,保证发泡制品质量;发泡粒子经加热熔接后,迅速冷却成型脱模,得到电动汽车塑料泡沫珠粒模压锂电电池箱制品;所述成型温度需要150℃,压力需要0.25MPa。Application of a modified polyphenylene ether foamed bead in a lightweight power battery box; using high-frequency heating molding equipment with high efficiency, pre-foamed foamed particles with a certain expansion ratio are blown into a mold and foamed After the particles are filled in the mold, the heating temperature is high through high-frequency heating, and the foamed beads are heated uniformly from the inside to the outside to ensure the quality of the foamed products. After the foamed particles are heated and welded, they are quickly cooled and molded to obtain the plastic of the electric vehicle. Foam beads are molded into lithium battery box products; the molding temperature needs to be 150 ° C, and the pressure needs to be 0.25 MPa.
实施例3Example 3
一种改性聚苯醚发泡珠粒的配方;由包含以下重量份的组分制成:聚苯醚30-90份、改性聚合物60份、相容剂18份、增韧剂17份、阻燃剂13份、抗氧剂3份、助抗氧剂3份、润滑剂2份、偶联剂2份、分散剂6份、无机纳米成核剂材料4份。A formula of modified polyphenylene ether foam beads; made of the following components by weight: 30-90 parts of polyphenylene ether, 60 parts of modified polymer, 18 parts of compatibilizer, and 17 of toughening agent Parts, 13 parts flame retardant, 3 parts antioxidant, 3 parts auxiliary antioxidant, 2 parts lubricant, 2 parts coupling agent, 6 parts dispersant, and 4 parts inorganic inorganic nucleating agent material.
一种改性聚苯醚发泡珠粒的制备方法;包括如下步骤:A method for preparing modified polyphenylene ether foamed beads, including the following steps:
步骤一:材料改性,以聚苯醚材料为基料,加入改性聚合物,相容剂,无机纳米材料和有关助剂,混合加热,挤出得到发泡改性聚苯醚材料;Step 1: material modification, using polyphenylene ether material as the base material, adding modified polymer, compatibilizer, inorganic nano material and related auxiliary agents, mixing and heating, and extruding to obtain foamed modified polyphenylene ether material;
步骤二:水下切粒:物料按配方加入在高速混合机混合均匀,投入双、三螺杆挤出混合设备,高温熔融挤出物料,与水下切粒设备配合进行水下切粒,使得切出的颗粒粒径大小均匀,粒径2mm,颗粒形状圆度高,表面光滑;Step 2: Underwater pelletizing: Add the materials according to the formula and mix them evenly in a high-speed mixer. Put in twin or three-screw extrusion mixing equipment to melt the materials at high temperature. Use the underwater pelletizing equipment to perform underwater pelletization to make the pellets cut out. Uniform particle size, particle size 2mm, high roundness of particle shape, smooth surface;
步骤三:预发泡粒子:在预发泡珠粒成型设备中加入超临界流体(二氧化碳,氮气),将水下切出的粒子,以高频加热方式,在135℃的温度下,高压喷入到预发泡珠粒成型设备中,通过气体渗透溶解,压力释放,冷却降温等过程,用高效节能的预发泡加工设备和工艺来完成改性聚苯醚材料发泡珠粒的生产,发泡倍率16倍,制造出适合发泡均匀,倍率大,闭孔率高,泡孔均匀细密,不容易收缩塌陷的发泡珠粒;使其达到要求发泡倍率的发泡粒子。Step 3: Pre-expanded particles: Add supercritical fluid (carbon dioxide, nitrogen) to the pre-expanded bead molding equipment, and use high-frequency heating at a temperature of 135 ° C to inject the particles cut out underwater under high pressure. In the pre-expanded bead molding equipment, through the processes of gas infiltration and dissolution, pressure release, cooling and cooling, etc., the production of modified polyphenylene ether foamed beads is completed with efficient and energy-saving pre-expanded processing equipment and processes. The foaming ratio is 16 times, and the foaming beads suitable for uniform foaming, large magnification, high closed cell ratio, uniform and fine cells, and difficult to shrink and collapse are produced;
一种改性聚苯醚发泡珠粒在轻量化动力电池箱的应用;利用高效加热的 高频技术成型设备,预发泡好的一定发泡倍率的发泡粒子风送进入模具,发泡粒子充满模具后,通过高频加热,加热温度高,发泡珠粒从里到外加热温度均匀,保证发泡制品质量;发泡粒子经加热熔接后,迅速冷却成型脱模,得到电动汽车塑料泡沫珠粒模压锂电电池箱制品;所述成型温度需要150℃,压力需要0.25MPa。Application of a modified polyphenylene ether foamed bead in a lightweight power battery box; using high-frequency heating molding equipment with high efficiency, pre-foamed foamed particles with a certain expansion ratio are blown into a mold and foamed After the particles are filled in the mold, the heating temperature is high through high-frequency heating, and the foamed beads are heated uniformly from the inside to the outside to ensure the quality of the foamed products. After the foamed particles are heated and welded, they are quickly cooled and molded to obtain the plastic of the electric vehicle. Foam beads are molded into lithium battery box products; the molding temperature needs to be 150 ° C, and the pressure needs to be 0.25 MPa.
经测试产品技术指标:Technical indicators of tested products:
Figure PCTCN2018111453-appb-000001
Figure PCTCN2018111453-appb-000001
耐热性:负荷0.2MPa,截面积13mm×6mm,支撑距离64mm,温度105℃,发泡率5(cc/g),形变≤0.34mm。制品成型尺寸公差:0.2~0.7%。Heat resistance: load 0.2MPa, cross-sectional area 13mm × 6mm, support distance 64mm, temperature 105 ° C, foaming rate 5 (cc / g), deformation ≤ 0.34mm. Product forming dimension tolerance: 0.2 ~ 0.7%.
上面对本发明的较佳实施方式作了详细说明,但是本发明并不限于上述实施方式,在本领域的普通技术人员所具备的知识范围内,还可以在不脱离本发明宗旨的前提下作出各种变化。The preferred embodiments of the present invention have been described in detail above, but the present invention is not limited to the above embodiments, and within the scope of knowledge possessed by a person of ordinary skill in the art, various embodiments can be made without departing from the spirit of the present invention. Kind of change.

Claims (8)

  1. 一种改性聚苯醚发泡珠粒的配方,其特征在于,由包含以下重量份的组分制成:聚苯醚30-90份、改性聚合物30-90份、相容剂5-30份、增韧剂5-30份、阻燃剂5-20份、抗氧剂1-5份、助抗氧剂1-5份、润滑剂1-3份、偶联剂1--3份、分散剂1--10份、无机纳米成核剂材料2-6份。A formula of modified polyphenylene ether foamed beads, which is characterized by being composed of the following components by weight: 30-90 parts of polyphenylene ether, 30-90 parts of modified polymer, and compatibilizer 5 -30 parts, toughener 5-30 parts, flame retardant 5-20 parts, antioxidants 1-5 parts, auxiliary antioxidants 1-5 parts, lubricants 1-3 parts, coupling agent 1-- 3 parts, dispersant 1--10 parts, inorganic nano-nucleating agent material 2-6 parts.
  2. 根据权利要求1所述的一种改性聚苯醚发泡珠粒的配方,其特征在于,所述改性聚合物是由ABS、PE、PPS、PA、HIPS、PP、BS以及GPPS按照等重量混合制造而成。The formulation of a modified polyphenylene ether foamed bead according to claim 1, wherein the modified polymer is made of ABS, PE, PPS, PA, HIPS, PP, BS, and GPPS according to Made by mixing weights.
  3. 所述相容剂是由PP-g-MAH、SEBS-g-MAH、PE-g-MAH、EPDM以及POE-g-GMA按照等重量混合制造而成。The compatibilizer is made by mixing PP-g-MAH, SEBS-g-MAH, PE-g-MAH, EPDM and POE-g-GMA according to equal weight.
  4. 所述增韧剂是由SBS、SEBS、聚丁烯、LCP、EPDM以及聚烯烃弹性体按照等重量混合制造而成。The toughening agent is made by mixing SBS, SEBS, polybutene, LCP, EPDM, and polyolefin elastomer according to equal weight.
  5. 所述阻燃剂是由磷酸酯类的阻燃剂和无机纳米阻燃剂复配按照等重量混合制造而成;所述无机纳米阻燃剂:纳米氢氧化铝、纳米氢氧化镁、红磷、硼酸锌、纳米氧化锑、纳米钼化合物、层状硅酸盐和无水碳酸镁按照等重量混合制造而成。The flame retardant is prepared by mixing a phosphate ester flame retardant and an inorganic nano flame retardant in an equal weight; the inorganic nano flame retardant: nano aluminum hydroxide, nano magnesium hydroxide, and red phosphorus , Zinc borate, nano antimony oxide, nano molybdenum compound, layered silicate and anhydrous magnesium carbonate are mixed and produced according to equal weight.
  6. 所述抗氧剂为抗氧剂1010;助抗氧剂为助抗氧剂168,润滑剂为液体石蜡,偶联剂是由硅烷偶联剂、钛酸酯偶联剂和铝酸偶联剂按照等重量混合制造而成,分散剂是由聚烯烃类超分散剂、聚醚型超分散剂以及聚丙烯酸酯型超分散剂按照等重量混合制造而成。The antioxidant is antioxidant 1010; the auxiliary antioxidant is auxiliary antioxidant 168; the lubricant is liquid paraffin; and the coupling agent is a silane coupling agent, a titanate coupling agent, and an aluminate coupling agent. The dispersant is made by mixing the same weight, and the dispersant is made by mixing the polyolefin type super dispersant, the polyether type super dispersant and the polyacrylate type super dispersant according to the same weight.
  7. 一种如权利要求1-6任一所述的一种改性聚苯醚发泡珠粒的制备方法,其特征在于,包括如下步骤:A method for preparing a modified polyphenylene ether foamed bead according to any one of claims 1-6, comprising the following steps:
    步骤一:材料改性,以聚苯醚材料为基料,加入改性聚合物,相容剂,无机纳米材料和有关助剂,混合加热,挤出得到发泡改性聚苯醚材料;Step 1: material modification, using polyphenylene ether material as the base material, adding modified polymer, compatibilizer, inorganic nano material and related auxiliary agents, mixing and heating, and extruding to obtain foamed modified polyphenylene ether material;
    步骤二:水下切粒:物料按配方加入在高速混合机混合均匀,投入双、三螺杆挤出混合设备,高温熔融挤出物料,与水下切粒设备配合进行水下切 粒,使得切出的颗粒粒径大小均匀,粒径0.3~6mm,颗粒形状圆度高,表面光滑;Step 2: Underwater pelletizing: Add the materials according to the formula and mix them evenly in a high-speed mixer. Put in twin or three-screw extrusion mixing equipment to melt the materials at high temperature. Use the underwater pelletizing equipment to perform underwater pelletization to make the pellets cut out. Uniform particle size, particle size 0.3 ~ 6mm, high roundness of particle shape, smooth surface;
    步骤三:预发泡粒子:在预发泡珠粒成型设备中加入超临界流体(二氧化碳,氮气),将水下切出的粒子,以高频加热方式,在120~250℃的温度下,高压喷入到预发泡珠粒成型设备中,通过气体渗透溶解,压力释放,冷却降温等过程,用高效节能的预发泡加工设备和工艺来完成改性聚苯醚材料发泡珠粒的生产,发泡倍率3-30倍,制造出适合发泡均匀,倍率大,闭孔率高,泡孔均匀细密,不容易收缩塌陷的发泡珠粒;使其达到要求发泡倍率的发泡粒子。Step 3: Pre-expanded particles: Add supercritical fluid (carbon dioxide, nitrogen) to the pre-expanded bead molding equipment, and cut the particles that are cut out underwater under high-frequency heating at a temperature of 120-250 ° C under high pressure. Sprayed into the pre-expanded bead molding equipment, through the processes of gas infiltration and dissolution, pressure release, cooling and cooling, etc., the production of modified polyphenylene ether foamed beads is completed with high-efficiency and energy-saving pre-expanded processing equipment and processes. , Foaming ratio of 3-30 times, making foaming beads suitable for uniform foaming, large magnification, high closed cell ratio, uniform and fine cells, and not easy to shrink and collapse; make it reach the required foaming ratio of foamed particles .
  8. 一种如权利要求7所述的一种改性聚苯醚发泡珠粒在轻量化动力电池箱的应用,其特征在于,利用高效加热的高频技术成型设备,预发泡好的一定发泡倍率的发泡粒子风送进入模具,发泡粒子充满模具后,通过高频加热,加热温度高,发泡珠粒从里到外加热温度均匀,保证发泡制品质量;发泡粒子经加热熔接后,迅速冷却成型脱模,得到电动汽车塑料泡沫珠粒模压锂电电池箱制品;成型温度为150℃,压力为0.25MPa。The use of a modified polyphenylene ether foamed bead as claimed in claim 7 in a lightweight power battery box, characterized in that high-frequency heating molding equipment using efficient heating is used to pre-foam a certain amount of hair. The foaming rate of the foamed particles is sent into the mold by wind. After the foamed particles are filled in the mold, the heating temperature is high and the foamed beads are heated uniformly from the inside to the outside to ensure the quality of the foamed products; the foamed particles are heated After welding, the product was quickly cooled and molded to obtain an electric vehicle plastic foam bead molded lithium battery box product. The molding temperature was 150 ° C and the pressure was 0.25 MPa.
PCT/CN2018/111453 2018-06-06 2018-10-23 Modified polyphenylene ether foam bead, preparation method and application thereof WO2019233017A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201810573216.5A CN109054337A (en) 2018-06-06 2018-06-06 A kind of formula of Noryl expanded bead, preparation method and applications
CN201810573216.5 2018-06-06

Publications (1)

Publication Number Publication Date
WO2019233017A1 true WO2019233017A1 (en) 2019-12-12

Family

ID=64820451

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2018/111453 WO2019233017A1 (en) 2018-06-06 2018-10-23 Modified polyphenylene ether foam bead, preparation method and application thereof

Country Status (2)

Country Link
CN (1) CN109054337A (en)
WO (1) WO2019233017A1 (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109943055A (en) * 2019-01-28 2019-06-28 广东国立科技股份有限公司 Low creep flame-proof glass fibre enhancing PPO/LCP composite alloy material of a kind of high-temperature resistant high rigidity and preparation method thereof
CN109867942B (en) * 2019-01-30 2021-06-29 中国科学院宁波材料技术与工程研究所 Preparation method of flame-retardant micro-foaming polyphenyl ether composite material and product thereof
CN110591331A (en) * 2019-08-16 2019-12-20 杭州博适特新材料科技有限公司 Modified polyphenylene sulfide or modified polyphenylene oxide foamed bead and preparation method thereof
CN112745653B (en) * 2019-10-30 2022-11-18 中国石油化工股份有限公司 Modified polyphenyl ether, halogen-free flame-retardant TPV, preparation methods and applications of modified polyphenyl ether and halogen-free flame-retardant TPV, and composition for preparing halogen-free flame-retardant TPV
CN113136098B (en) * 2021-04-16 2022-08-26 贵州凯科特材料有限公司 Modified polyphenyl ether micro-foaming material and preparation method thereof
CN114311484B (en) * 2021-12-31 2023-10-27 中山大学南昌研究院 Preparation method of modified polyphenyl ether foaming bead molding body
CN114374038A (en) * 2022-03-22 2022-04-19 浙江阿莱西澳智能装备科技有限公司 Carbon fiber composite material for new energy automobile chassis structure and battery pack tray
CN114736505B (en) * 2022-04-22 2024-01-23 无锡会通轻质材料股份有限公司 Foaming polyphenyl ether polypropylene composite bead and wafer packaging box
CN115181319B (en) * 2022-08-09 2023-03-21 北京化工大学 Preparation method of polyphenyl ether foamable particles
CN116496542B (en) * 2023-06-13 2023-10-03 山东联欣环保科技有限公司 Preparation method of carbon dioxide-based biodegradable foaming material

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05310986A (en) * 1992-05-13 1993-11-22 Sekisui Plastics Co Ltd Production of synthetic resin expansion molded body good in dimensional stability
US5389320A (en) * 1991-10-28 1995-02-14 General Electric Company Method of making expandable polyphenylene ether and polyolefin blend
CN1484675A (en) * 2000-12-28 2004-03-24 通用电气公司 Poly (arglene ether) polyolefin composition and articles derived therefrom
CN102471517A (en) * 2009-08-13 2012-05-23 旭化成化学株式会社 Expandable beads, molded body using the same, and production method for molded body

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6106420B2 (en) * 2012-12-13 2017-03-29 株式会社ジェイエスピー Method for producing thermoplastic resin foam blow molded article and thermoplastic resin foam blow molded article
CN103910966A (en) * 2013-01-05 2014-07-09 上海杰事杰新材料(集团)股份有限公司 Foamed polyphenyl ether/polystyrene blended alloy material and its preparation method

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5389320A (en) * 1991-10-28 1995-02-14 General Electric Company Method of making expandable polyphenylene ether and polyolefin blend
JPH05310986A (en) * 1992-05-13 1993-11-22 Sekisui Plastics Co Ltd Production of synthetic resin expansion molded body good in dimensional stability
CN1484675A (en) * 2000-12-28 2004-03-24 通用电气公司 Poly (arglene ether) polyolefin composition and articles derived therefrom
CN102471517A (en) * 2009-08-13 2012-05-23 旭化成化学株式会社 Expandable beads, molded body using the same, and production method for molded body

Also Published As

Publication number Publication date
CN109054337A (en) 2018-12-21

Similar Documents

Publication Publication Date Title
WO2019233017A1 (en) Modified polyphenylene ether foam bead, preparation method and application thereof
CN101250249B (en) Polypropylene resin with high flux intensity
CN102070841B (en) Polypropylene foam sheet prepared from composite foaming agent and production method thereof
CN103012832B (en) Preparation method of foamed polypropylene
CN103360682B (en) Heat-insulated degradable polypropylene foaming material and production method thereof
CN102218879B (en) Waste polypropylene-modified foaming plate and manufacturing method thereof
WO2017000923A1 (en) Low-temperature nylon powder material for selective laser sintering and preparation method therefor
CN103665583B (en) Propylene and ethylene high melt strength, propylene expanded bead and preparation method thereof
CN108000845B (en) Forming method of phase-change heat management component and formed phase-change heat management component
CN103788502B (en) A kind of polypropylene foaming beads formed body and preparation method thereof
CN109486473B (en) Multifunctional phase-change composite material and preparation method thereof
CN103756124A (en) Polypropylene foaming material, production and preparation method of product
CN109679227B (en) Method for shortening EPP bead forming period
CN103059416A (en) Anti-impact modified PP/HDPE (Polypropylene/High Density Polyethylene) plastics for automotive interior parts and preparation method thereof
CN110054835B (en) Preparation method of high-rate conductive polypropylene foamed beads
CN102746602A (en) Ultra-thin electron radiation crosslinked polyolefin foamed sheet and preparation method thereof
CN110229372A (en) Low molding energy consumption polypropylene foamed particles of one kind and preparation method thereof
CN110818990A (en) Preparation method of light slow-running shoe sole
CN102604205B (en) Novel environment-friendly composite reinforced polypropylene building template
CN105906945A (en) Battery box of oil-electric hybrid-power four-wheeler and application of battery box
JP2017186492A (en) Manufacturing method of foam molded body of carbon fiber reinforced modified polypropylene-based resin
CN110128741B (en) Polyolefin foam material and preparation method thereof
CN116162310A (en) Buffering flame-retardant crosslinked polypropylene foaming material for lithium battery pack and preparation method thereof
CN115418195A (en) Composite phase-change heat storage material for lithium battery pack heat management and preparation method thereof
CN103923382A (en) Foamed polypropylene bead with low melting point and high cementability and preparation method thereof

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 18922058

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 18922058

Country of ref document: EP

Kind code of ref document: A1