CN102702715A - 一种高流动性玻纤增强无卤阻燃pc树脂及其制备方法 - Google Patents

一种高流动性玻纤增强无卤阻燃pc树脂及其制备方法 Download PDF

Info

Publication number
CN102702715A
CN102702715A CN2012102211559A CN201210221155A CN102702715A CN 102702715 A CN102702715 A CN 102702715A CN 2012102211559 A CN2012102211559 A CN 2012102211559A CN 201210221155 A CN201210221155 A CN 201210221155A CN 102702715 A CN102702715 A CN 102702715A
Authority
CN
China
Prior art keywords
resin
flame retardant
free flame
district
temperature
Prior art date
Legal status (The legal status 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 status listed.)
Pending
Application number
CN2012102211559A
Other languages
English (en)
Inventor
刘福军
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
DONGGUAN SONG SHEN PLASTICS TECHNOLOGY Co Ltd
Original Assignee
DONGGUAN SONG SHEN PLASTICS TECHNOLOGY Co Ltd
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 DONGGUAN SONG SHEN PLASTICS TECHNOLOGY Co Ltd filed Critical DONGGUAN SONG SHEN PLASTICS TECHNOLOGY Co Ltd
Priority to CN2012102211559A priority Critical patent/CN102702715A/zh
Publication of CN102702715A publication Critical patent/CN102702715A/zh
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/12Making granules characterised by structure or composition
    • B29B9/14Making granules characterised by structure or composition fibre-reinforced
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58Component parts, details or accessories; Auxiliary operations
    • B29B7/72Measuring, controlling or regulating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/7461Combinations of dissimilar mixers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/88Adding charges, i.e. additives
    • B29B7/90Fillers or reinforcements, e.g. fibres
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/12Making granules characterised by structure or composition
    • 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
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/04Particle-shaped
    • 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
    • B29C48/36Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
    • B29C48/395Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
    • B29C48/40Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
    • 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
    • C08K5/00Use of organic ingredients
    • C08K5/49Phosphorus-containing compounds
    • C08K5/51Phosphorus bound to oxygen
    • C08K5/52Phosphorus bound to oxygen only
    • C08K5/521Esters of phosphoric acids, e.g. of H3PO4
    • C08K5/523Esters of phosphoric acids, e.g. of H3PO4 with hydroxyaryl compounds
    • 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
    • C08K7/00Use of ingredients characterised by shape
    • C08K7/02Fibres or whiskers
    • C08K7/04Fibres or whiskers inorganic
    • C08K7/14Glass
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L25/00Compositions of, homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Compositions of derivatives of such polymers
    • C08L25/02Homopolymers or copolymers of hydrocarbons
    • C08L25/04Homopolymers or copolymers of styrene
    • C08L25/08Copolymers of styrene
    • C08L25/12Copolymers of styrene with unsaturated nitriles
    • 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
    • C08L69/00Compositions of polycarbonates; Compositions of derivatives of polycarbonates
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K21/00Fireproofing materials
    • C09K21/06Organic materials
    • C09K21/12Organic materials containing phosphorus
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/34Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
    • B29B7/38Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
    • B29B7/46Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/02Making granules by dividing preformed material
    • B29B9/06Making granules by dividing preformed material in the form of filamentary material, e.g. combined with extrusion
    • 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
    • B29C2948/92561Time, e.g. start, termination, duration or interruption
    • 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
    • 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
    • B29C2948/92819Location or phase of control
    • B29C2948/92857Extrusion unit
    • B29C2948/92876Feeding, melting, plasticising or pumping zones, e.g. the melt itself
    • B29C2948/92895Barrel or housing

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Materials Engineering (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

本发明涉及PC树脂改性技术领域,特别是涉及一种高流动性玻纤增强无卤阻燃PC树脂及其制备方法,该种高流动性玻纤增强无卤阻燃PC树脂,它由以下重量百分比的原料组成:PC树脂30-70%、玻璃纤维10-35%、AS树脂5-30%、阻燃剂8-15%、增韧剂5-10%、抗氧剂0.2-1.5%,以上原料经共混挤出造粒制得,本发明制得的种高流动性玻纤增强无卤阻燃PC在满足材料UL94V0阻燃的基础上,耐热性、加工流动性、抗冲击性能优异;本发明的制备方法工艺简单、成本低。

Description

一种高流动性玻纤增强无卤阻燃PC树脂及其制备方法
技术领域
本发明涉及PC树脂改性技术领域,特别是涉及一种高流动性玻纤增强无卤阻燃PC树脂及其制备方法。
背景技术
聚碳酸酯PC具有冲击强度高,透明,无毒,介电性能优良抗蠕变性和尺寸稳定性等优点,在电气,汽车工业,医疗器械,建筑和照明用具等领域已广泛应用。虽然聚碳酸酯PC的阻燃等级为UL94-V-2。但是仍可燃烧,且燃烧时有热熔体滴下,容易引起附近材料着火,难以满足阻燃防火要求。因此,在实际应用中要对PC进行阻燃处理。
如专利号为ZL200810038154.4的中国发明公开了一种低发烟量无卤阻燃PC/ABS合金及其制备方法,按重量百分比称取聚碳酸酯(PC)40-75%,丙烯晴-丁二烯-苯乙烯共聚物(ABS)10-40%,复合阻燃剂10-15%,复合降烟剂0.2-2%,相容剂2-16%,低发烟促进剂1-6%,稳定剂0.1-0.5%,润滑剂0.1-0.6%,以上专利和其它现有技术要使PC树脂达到V0级别阻燃,都添加了很大量的阻燃剂和其它助剂,导致改性PC树脂的耐热性急剧下降,加工流动性较差。
发明内容
本发明的目的在于针对现有技术的不足,提供了一种高流动性玻纤增强无卤阻燃PC树脂及其制备方法,该种高流动性玻纤增强无卤阻燃PC树脂耐热性好、加工流动性强,该种高流动性玻纤增强无卤阻燃PC树脂的制备方法工艺简单、成本低。
本发明的目的是这样实现的:一种高流动性玻纤增强无卤阻燃PC树脂,它由以下重量百分比的原料组成:
PC树脂              30-70%
玻璃纤维             10-35%
AS树脂              5-30%
阻燃剂               8-15%
增韧剂              5-10%
抗氧剂              0.2-1.5%。
优选的,它由以下重量百分比的原料组成:
PC树脂              30-64%
玻璃纤维             15-35%
AS树脂              5-30%
阻燃剂               10-15%
增韧剂               5-10%
抗氧剂              1-1.5%。
更为优选的,它由以下重量百分比的原料组成:
PC树脂              45%
玻璃纤维             15%
AS树脂              19%
阻燃剂               15%
增韧剂               5%
抗氧剂              1%。
其中,所述PC树脂为一种通用型号芳香族聚碳酸酯,密度为1.1-1.6g/cm3
其中,所述玻璃纤维的直径为10μm-13μm。
其中,所述AS树脂中苯乙烯含量为30%-50%。
其中,所述阻燃剂为双酚A双(磷酸二苯酯)(BDP)。
其中,所述增韧剂为甲基丙烯酸甲酯、丁二烯、及苯乙烯的三元共聚物(MBS)。
其中,所述抗氧剂为四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯,三[2.4-二叔丁基苯基]亚磷酸酯,2-叔丁基-6-(3-叔丁基-5-甲基-2-羟苯基)-4-甲基苯基丙烯酸酯中的一种或任意几种。
本发明通过调节玻璃纤维的含量来有效改善材料的耐热性能,通过调节AS树脂的含量来有效改善材料的加工流动性。
上述高流动性玻纤增强无卤阻燃PC树脂的制备方法,它包括以下制备步骤:
步骤A、将PC 树脂和AS树脂在80℃烘烤1小时,备用;
步骤B、将烘烤后的PC树脂、将烘烤后的AS树脂、阻燃剂、增韧剂、抗氧剂按比例加入高速混合机中高速共混5-10min,得到共混物;
步骤C、将玻璃纤维和步骤B得到的共混物经双螺杆挤出机挤出造粒;
步骤D、将步骤C得到的粒子在100℃ 烘烤1-2小时,即得成品。
其中,所述步骤C双螺杆挤出机的具体工艺参数为:一区温度 210-200℃,二区温度210-200℃,三区温度210-200℃,四区温度210-200℃,五区温度210-200℃,六区温度 190-200℃,七区温度190-200℃,八区温度190-200℃,九区温度190-200℃,模头温度190-195℃ ,停留时间2-3min,压力12-18MPa,螺杆转速 280-350R/min。
本发明的有益效果为:本发明制备的高流动性玻纤增强无卤阻燃PC树脂,在满足材料UL94 V0阻燃的基础上,耐热性、加工流动性、抗冲击性能优异;本发明的制备方法工艺简单、成本低。
具体实施方式
下面通过实施例对本发明作进一步说明,但本发明的实施范围并不限于此。
实施例1。
将PC 树脂和AS树脂在80℃烘烤1小时,然后将30㎏烘烤后的PC树脂、将30㎏烘烤后的AS树脂、15㎏BDP、5㎏MBS、0.2㎏四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯加入高速混合机中高速共混10min,得到共混物,再将19.8㎏玻璃纤维和上述共混物经双螺杆挤出机挤出造粒,得到的粒子在100℃ 烘烤2小时,即得成品。双螺杆挤出机的具体工艺参数为:一区温度 210℃,二区温度200℃,三区温度205℃,四区温度210℃,五区温度200℃,六区温度 195℃,七区温度200℃,八区温度190℃,九区温度200℃,模头温度195℃ ,停留时间2min,压力12MPa,螺杆转速 280R/min。
实施例2。
将PC 树脂和AS树脂在80℃烘烤1小时,然后将70㎏烘烤后的PC树脂、将5㎏烘烤后的AS树脂、8.5㎏BDP、5㎏MBS、0.5㎏四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯、0.5㎏三[2.4-二叔丁基苯基]亚磷酸酯、0.5㎏2-叔丁基-6-(3-叔丁基-5-甲基-2-羟苯基)-4-甲基苯基丙烯酸酯加入高速混合机中高速共混8min,得到共混物,再将10㎏玻璃纤维和上述共混物经双螺杆挤出机挤出造粒,得到的粒子在100℃ 烘烤1小时,即得成品。双螺杆挤出机的具体工艺参数为:一区温度200℃,二区温度210℃,三区温度200℃,四区温度210℃,五区温度200℃,六区温度 190℃,七区温度200℃,八区温度190℃,九区温度200℃,模头温度195℃ ,停留时间3min,压力18MPa,螺杆转速350R/min。
实施例3。
将PC 树脂和AS树脂在80℃烘烤1小时,然后将50㎏烘烤后的PC树脂、将20㎏烘烤后的AS树脂、10㎏BDP、5.8㎏MBS、0.2㎏三[2.4-二叔丁基苯基]亚磷酸酯加入高速混合机中高速共混8min,得到共混物,再将14㎏玻璃纤维和上述共混物经双螺杆挤出机挤出造粒,得到的粒子在100℃ 烘烤2小时,即得成品。双螺杆挤出机的具体工艺参数为:一区温度 205℃,二区温度200℃,三区温度205℃,四区温度210℃,五区温度205℃,六区温度 195℃,七区温度200℃,八区温度195℃,九区温度195℃,模头温度190℃ ,停留时间2min,压力15MPa,螺杆转速 320R/min。
实施例4。
将PC 树脂和AS树脂在80℃烘烤1小时,然后将45㎏烘烤后的PC树脂、将19㎏烘烤后的AS树脂、15㎏BDP、5㎏MBS、1㎏2-叔丁基-6-(3-叔丁基-5-甲基-2-羟苯基)-4-甲基苯基丙烯酸酯加入高速混合机中高速共混8min,得到共混物,再将15㎏玻璃纤维和上述共混物经双螺杆挤出机挤出造粒,得到的粒子在100℃ 烘烤2小时,即得成品。双螺杆挤出机的具体工艺参数为:一区温度 210℃,二区温度200℃,三区温度210℃,四区温度208℃,五区温度210℃,六区温度 198℃,七区温度195℃,八区温度200℃,九区温度190℃,模头温度193℃ ,停留时间3min,压力18MPa,螺杆转速 330R/min。
实施例5。
将PC 树脂和AS树脂在80℃烘烤1小时,然后将40㎏烘烤后的PC树脂、将10㎏烘烤后的AS树脂、10㎏BDP、10㎏MBS、0.5㎏四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯、0.5㎏三[2.4-二叔丁基苯基]亚磷酸酯加入高速混合机中高速共混10min,得到共混物,再将29㎏玻璃纤维和上述共混物经双螺杆挤出机挤出造粒,得到的粒子在100℃ 烘烤1小时,即得成品。双螺杆挤出机的具体工艺参数为::一区温度 205℃,二区温度200℃,三区温度205℃,四区温度210℃,五区温度205℃,六区温度 195℃,七区温度200℃,八区温度195℃,九区温度195℃,模头温度190℃ ,停留时间2min,压力15MPa,螺杆转速 320R/min。
实施例6。
将PC 树脂和AS树脂在80℃烘烤1小时,然后将40㎏烘烤后的PC树脂、将15㎏烘烤后的AS树脂、13.5㎏BDP、5㎏MBS、1㎏四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯、0.5㎏2-叔丁基-6-(3-叔丁基-5-甲基-2-羟苯基)-4-甲基苯基丙烯酸酯加入高速混合机中高速共混5min,得到共混物,再将25㎏玻璃纤维和上述共混物经双螺杆挤出机挤出造粒,得到的粒子在100℃ 烘烤2小时,即得成品。双螺杆挤出机的具体工艺参数为:一区温度200℃,二区温度210℃,三区温度200℃,四区温度210℃,五区温度200℃,六区温度 190℃,七区温度200℃,八区温度190℃,九区温度200℃,模头温度195℃ ,停留时间3min,压力17MPa,螺杆转速340R/min。
说明:实施例1-6所用的PC树脂为一种通用型号芳香族聚碳酸酯,密度为1.1-1.6g/cm3;玻璃纤维的直径为10μm-13μm;AS树脂中苯乙烯含量为30%-50%;阻燃剂为双酚A双(磷酸二苯酯)(BDP);增韧剂为甲基丙烯酸甲酯、丁二烯、及苯乙烯的三元共聚物(MBS)。
本发明产品的性能评价方式及实行标准:
按照上述方法完成造粒的粒子放入80℃的鼓风烘箱中干燥1-2小时,然后再将干燥好的粒子在注射成型机上进行注射成型制样。
拉伸性能测试按ISO-527-2进行,试样尺寸150*10*4mm ,拉伸速度为50mm/min;弯曲强度按ISO 178进行,试样尺寸80*10*4mm ,弯曲速度为2mm/min,跨距为64mm;
简支梁冲击强度按ISO 179进行,试样尺寸80*6*4mm,缺口深度为试样厚度的三分之一;
热变形温度按ISO 75进行,试样尺寸120*10*3mm,载荷为1.8MPa; 
熔融指数按照ISO1133,试样为粒子状,加工流动性通过熔融指数进行评价。
实施例1-6产品性能参数见表1。
                                                
Figure 365093DEST_PATH_IMAGE001
通过表1可以看出本发明制备的高流动性玻纤增强无卤阻燃PC树脂耐热性、加工流动性、抗冲击性能优异。
最后应当说明的是,以上实施例仅用以说明本发明的技术方案,而非对本发明保护范围的限制,尽管参照较佳实施例对本发明作了详细地说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的实质和范围。

Claims (10)

1.一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于: 它由以下重量百分比的原料组成:
PC树脂              30-70%
玻璃纤维             10-35%
AS树脂              5-30%
阻燃剂               8-15%
增韧剂              5-10%
抗氧剂              0.2-1.5%。
2.根据权利要求1所述的一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于:它由以下重量百分比的原料组成:
PC树脂              30-64%
玻璃纤维             15-35%
AS树脂              5-30%
阻燃剂               10-15%
增韧剂               5-10%
抗氧剂              1-1.5%。
3.根据权利要求2所述的一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于:它由以下重量百分比的原料组成:
PC树脂              45%
玻璃纤维             15%
AS树脂              19%
阻燃剂               15%
增韧剂               5%
抗氧剂              1%。
4.根据权利要求1-3任一项所述的一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于:所述玻璃纤维的直径为10μm-13μm。
5.根据权利要求1-3任一项所述的一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于:所述AS树脂中苯乙烯含量为30%-50%。
6.根据权利要求1-3任一项所述的一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于:所述阻燃剂为双酚A双(磷酸二苯酯)。
7.根据权利要求1-3任一项所述的一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于:所述增韧剂为甲基丙烯酸甲酯、丁二烯及苯乙烯的三元共聚物。
8.根据权利要求1-3任一项所述的一种高流动性玻纤增强无卤阻燃PC树脂,其特征在于:所述抗氧剂为四[β-(3,5-二叔丁基-4-羟基苯基)丙酸]季戊四醇酯,三[2.4-二叔丁基苯基]亚磷酸酯,2-叔丁基-6-(3-叔丁基-5-甲基-2-羟苯基)-4-甲基苯基丙烯酸酯中的一种或任意几种。
9.权利要求1-8任一项所述的高流动性玻纤增强无卤阻燃PC树脂的制备方法,其特征在于:它包括以下制备步骤:
步骤A、将PC 树脂和AS树脂在80℃烘烤1小时,备用;
步骤B、将烘烤后的PC树脂、将烘烤后的AS树脂、阻燃剂、增韧剂、抗氧剂按比例加入高速混合机中高速共混5-10min,得到共混物;
步骤C、将玻璃纤维和步骤B得到的共混物经双螺杆挤出机挤出造粒;
步骤D、将步骤C得到的粒子在100℃ 烘烤1-2小时,即得成品。
10.根据权利要求9所述的一种高流动性玻纤增强无卤阻燃PC的制备方法,其特征在于:所述步骤C双螺杆挤出机的具体工艺参数为:一区温度 210-200℃,二区温度210-200℃,三区温度210-200℃,四区温度210-200℃,五区温度210-200℃,六区温度 190-200℃,七区温度190-200℃,八区温度190-200℃,九区温度190-200℃,模头温度190-195℃ ,停留时间2-3min,压力12-18MPa,螺杆转速 280-350R/min。
CN2012102211559A 2012-06-29 2012-06-29 一种高流动性玻纤增强无卤阻燃pc树脂及其制备方法 Pending CN102702715A (zh)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2012102211559A CN102702715A (zh) 2012-06-29 2012-06-29 一种高流动性玻纤增强无卤阻燃pc树脂及其制备方法

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2012102211559A CN102702715A (zh) 2012-06-29 2012-06-29 一种高流动性玻纤增强无卤阻燃pc树脂及其制备方法

Publications (1)

Publication Number Publication Date
CN102702715A true CN102702715A (zh) 2012-10-03

Family

ID=46895788

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2012102211559A Pending CN102702715A (zh) 2012-06-29 2012-06-29 一种高流动性玻纤增强无卤阻燃pc树脂及其制备方法

Country Status (1)

Country Link
CN (1) CN102702715A (zh)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103351596A (zh) * 2013-08-08 2013-10-16 深圳市兴盛迪新材料有限公司 一种改进的玻纤增强pc/asa组合物
CN103709708A (zh) * 2013-12-19 2014-04-09 上海日之升新技术发展有限公司 高流动性的玻纤增强无卤阻燃pc材料及其制备方法
CN104419190A (zh) * 2013-09-11 2015-03-18 安徽科聚新材料有限公司 一种透明增强无卤阻燃pc材料及其制备方法
CN105086410A (zh) * 2015-08-28 2015-11-25 合肥会通新材料有限公司 一种玻璃纤维增强高光无卤阻燃pc及其制备方法
EP2964701A4 (en) * 2013-03-08 2016-10-19 Covestro Llc FLAME RETARDANT POLYCARBONATE WITHOUT HALOGEN
CN107383825A (zh) * 2017-07-19 2017-11-24 上海仕天工程塑料有限公司 高光泽、免喷涂、薄壁化聚碳酸酯阻燃增强材料与应用
CN111087778A (zh) * 2018-10-23 2020-05-01 中国石油化工股份有限公司 流动性能改善的导热聚碳酸酯组合物及制备方法和应用

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101134839A (zh) * 2007-09-30 2008-03-05 深圳市科聚新材料有限公司 一种阻燃玻纤增强聚碳酸酯材料及其制备方法
CN101525481A (zh) * 2008-02-26 2009-09-09 帝人化成株式会社 阻燃性芳香族聚碳酸酯树脂组合物
CN101787190A (zh) * 2009-09-21 2010-07-28 深圳市科聚新材料有限公司 一种阻燃环保高强度pc-as复合材料及其制备方法

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101134839A (zh) * 2007-09-30 2008-03-05 深圳市科聚新材料有限公司 一种阻燃玻纤增强聚碳酸酯材料及其制备方法
CN101525481A (zh) * 2008-02-26 2009-09-09 帝人化成株式会社 阻燃性芳香族聚碳酸酯树脂组合物
CN101787190A (zh) * 2009-09-21 2010-07-28 深圳市科聚新材料有限公司 一种阻燃环保高强度pc-as复合材料及其制备方法

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2964701A4 (en) * 2013-03-08 2016-10-19 Covestro Llc FLAME RETARDANT POLYCARBONATE WITHOUT HALOGEN
US10017640B2 (en) 2013-03-08 2018-07-10 Covestro Llc Halogen free flame retarded polycarbonate
CN103351596A (zh) * 2013-08-08 2013-10-16 深圳市兴盛迪新材料有限公司 一种改进的玻纤增强pc/asa组合物
CN104419190A (zh) * 2013-09-11 2015-03-18 安徽科聚新材料有限公司 一种透明增强无卤阻燃pc材料及其制备方法
CN103709708A (zh) * 2013-12-19 2014-04-09 上海日之升新技术发展有限公司 高流动性的玻纤增强无卤阻燃pc材料及其制备方法
CN105086410A (zh) * 2015-08-28 2015-11-25 合肥会通新材料有限公司 一种玻璃纤维增强高光无卤阻燃pc及其制备方法
CN107383825A (zh) * 2017-07-19 2017-11-24 上海仕天工程塑料有限公司 高光泽、免喷涂、薄壁化聚碳酸酯阻燃增强材料与应用
CN111087778A (zh) * 2018-10-23 2020-05-01 中国石油化工股份有限公司 流动性能改善的导热聚碳酸酯组合物及制备方法和应用

Similar Documents

Publication Publication Date Title
CN102702715A (zh) 一种高流动性玻纤增强无卤阻燃pc树脂及其制备方法
CN101885881B (zh) 一种耐热阻燃聚氯乙烯电缆料及其制作方法
CN104327467B (zh) 一种膨胀型高灼热丝点燃温度pbt复合材料及其制备方法
CN102040775A (zh) 一种阻燃聚丙烯材料
CN102174247A (zh) 一种无卤阻燃玻璃纤维增强聚酯复合材料及其制备方法
CN102516732A (zh) 聚碳酸酯树脂/ abs合金及其制备方法
CN103724968A (zh) 一种高耐热高刚无卤阻燃耐刮擦pc-abs合金材料及其制备方法
CN104231575A (zh) 一种无卤无膦pbt增强复合材料及其制备方法
CN102093688A (zh) 一种高性能无卤阻燃pc/abs合金及其制备方法
CN105440628A (zh) 一种增强阻燃pc/ppo复合材料及其制备方法
CN104693701A (zh) 低翘曲无卤阻燃玻纤增强pbt/as合金及其制备方法
CN102924895A (zh) 一种无卤阻燃高光泽pc/abs合金及其制备方法
CN102504412A (zh) 一种低烟无卤阻燃聚丙烯电缆料及其制备方法
CN108129825B (zh) 一种高cti、高耐热无卤阻燃pc/abs组合物及其制备方法
CN104292827A (zh) 一种玻纤增强pa66专用无卤阻燃剂及其制备方法
CN101851405B (zh) 无人看管电器用高cti、高gwit环保阻燃增强pbt工程塑料及其制备方法
CN104817838A (zh) 一种高韧性无卤阻燃pc/abs合金反光材料及其制备方法
CN102731955A (zh) 无卤阻燃耐高温弹性体插头料及其制备方法
CN102942738A (zh) 一种高cti值、高gwit值环保阻燃玻纤增强pp/ppo合金材料及其制备方法
CN103073855A (zh) 一种聚酯组合物、制备方法及其应用
CN104725797A (zh) 一种阻燃塑料复合材料的制备方法
CN104725821A (zh) 磷氮系无卤阻燃聚碳酸酯及其制备方法
CN101851408B (zh) 一种无卤阻燃聚碳酸酯组合物及其制备方法
CN102604236A (zh) 一种暖风机外壳用高灼热丝阻燃聚丙烯材料及其制备方法
CN103881346A (zh) 加纤增强阻燃无卤化pc/pbt合金材料及其制备方法

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C12 Rejection of a patent application after its publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20121003