CN101092501A - PA6 / ABS alloy material, and preparation method - Google Patents

PA6 / ABS alloy material, and preparation method Download PDF

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Publication number
CN101092501A
CN101092501A CNA2007100746873A CN200710074687A CN101092501A CN 101092501 A CN101092501 A CN 101092501A CN A2007100746873 A CNA2007100746873 A CN A2007100746873A CN 200710074687 A CN200710074687 A CN 200710074687A CN 101092501 A CN101092501 A CN 101092501A
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China
Prior art keywords
abs
district
alloy material
abs alloy
brominated
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Chinese (zh)
Inventor
徐东
贺永
李茂林
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Polymer Science Shenzhen New Materials Co Ltd
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Polymer Science Shenzhen New Materials Co Ltd
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Priority to CNA2007100746873A priority Critical patent/CN101092501A/en
Publication of CN101092501A publication Critical patent/CN101092501A/en
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    • 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
    • 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
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/918Thermal treatment of the stream of extruded material, e.g. cooling characterized by differential heating or cooling
    • B29C48/9185Thermal treatment of the stream of extruded material, e.g. cooling characterized by differential heating or cooling in the direction of the stream of the material
    • 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
    • B29C48/94Lubricating
    • B29C48/95Lubricating by adding lubricant to the moulding material
    • 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
    • B29C2948/9258Velocity
    • B29C2948/9259Angular velocity
    • 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
    • B29C2948/92885Screw or gear
    • 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

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)

Abstract

This invention discloses a method for preparing PA6/ABS alloy material, which comprises: PA6 20-65%, ABS 10-70%, compatibilizer, 0.1-20%, composite flame retardant 5-30%, lubricant 0.1-0.6%, and antioxidant 0.1-1.2%. The PA6/ABS alloy material has such advantages as high flame retardancy, no toxicity, good physical properties, simple preparation, high dimensional stability, high strength, good appearance, high fluidity and high chemical resistance, and is environmentally friendly.

Description

A kind of PA6/ABS alloy material and preparation method thereof
Technical field
The present invention relates to technical field of polymer materials, relate in particular to a kind of PA6/ABS alloy material and preparation method thereof.
Background technology
Nylon/ABS alloy is to be released by the Borg.Warner Chemical company of the U.S. and Monsanto company the earliest, has heat-drawn wire than nylon 6 (PA6) height, and the higher characteristics of vicat softening temperature, thereby become the ideal material of making trolley parts such as vehicle body plate shell at first.Because nylon/ABS alloy material remedied PA material water-absorbent, the unsettled characteristics of size, and have the characteristics of high impulse strength, thereby be fit to be applied to make electronic apparatus, household appliance shell.
But for electronic apparatus, household appliance shell material require fire-retardant characteristics are arranged, and existing nylon/ABS alloy material do not possess the performance of this respect.
Summary of the invention
The technical problem to be solved in the present invention provides a kind of PA6/ABS alloy material with flame retardant resistance, and corresponding, the present invention also provides a kind of preparation method of PA6/ABS alloy material.
For solving the problems of the technologies described above, the objective of the invention is to be achieved through the following technical solutions.
A kind of PA6/ABS alloy material, its composition is (%) by weight ratio:
PA6 20-65%;
ABS 10-70%;
Compatilizer 0.1-20%;
Composite flame-retardant agent 5-30%;
Lubricant 0.1-0.6%;
Oxidation inhibitor 0.1-1.2%.
Wherein, the relative viscosity of described PA6 is 2.4-3.8PS.
Wherein, ABS is an acrylonitrile-butadiene-styrene terpolymer, and its rubber content is 15-70%.
Wherein, compatilizer is ABS-g-MAH, acrylonitrile-styrene-copolymer-maleic anhydride or SEBS-g-MAH.
Wherein, described composite flame-retardant agent is a brominated flame-retardant and antimonous oxide is composite forms.
Wherein, described brominated flame-retardant is one or more the mixture in Poly Brominated Diphenyl Ethers, TDE, brominated Polystyrene, brominated polystyrene, brominated epoxy resin, the brominated polycarbonate.
Wherein, described lubricant is the ultra-high molecular weight polysiloxane.
Wherein, described oxidation inhibitor is the composite of four [3-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester primary antioxidants and tricresyl phosphite (2,4-di-t-butyl phenyl ester) auxiliary anti-oxidant.
A kind of preparation method of PA6/ABS alloy material comprises step:
A: take by weighing PA6 and ABS by weight ratio, mix;
B: take by weighing compatilizer and composite flame-retardant agent by weight ratio, mix;
C: take by weighing lubricant and oxidation inhibitor by weight ratio, mix, the above-mentioned material that mixes is joined in the mixing tank together continue to mix until evenly;
D: mixed raw materials is put into the loading hopper of twin screw extruder, through melt extruding, granulation, fully plasticizing, fusion, compound, again through extrude, tie rod, cooling, pelletizing, oven dry and packing; Complete processing is as follows: twin screw extruder one district 215-240 ℃, two district 215-240 ℃, three district 215-240 ℃, four district 215-240 ℃, five district 215-240 ℃, six district 215-240 ℃, seven district 215-240 ℃, eight district 215-240 ℃; The screw rod revolution is controlled at 350 rev/mins; The residence time 2~10min.
Above technical scheme as can be seen, the present invention has following beneficial effect:
1: the present invention fuses together PA6 system and ABS system by selecting suitable fire retardant, and prepared material has fire-retardant characteristic, and environment-protecting asepsis;
2: guaranteed alloy material when having anti-flaming function, its every physical and mechanical property excellence;
3: the preparation technology of this fire retardant alloy material is simple, and has characteristics such as dimensional stabilizing, high strength, outward appearance are good, high workability, resistance to chemical reagents.
Embodiment
Technical scheme of the present invention provides a kind of fire-retardant nylon and ABS alloy material, and it is made up of a mixture, and its weight proportion consists of:
PA6 20-65%, ABS 10-70%, compatilizer 0.1-20%, composite flame-retardant agent 5-30%, lubricant 0.1-0.6%, oxidation inhibitor 0.1-1.2%;
Wherein, the relative viscosity of PA6 is 2.4-3.8PS; ABS is an acrylonitrile-butadiene-styrene terpolymer, and its rubber content is 15-70%; Compatilizer can be the polymer graft maleic anhydride, as ABS-g-MAH, acrylonitrile-styrene-copolymer-maleic anhydride, SEBS-g-MAH; Fire retardant is a brominated flame-retardant and antimonous oxide is composite forms; Wherein brominated flame-retardant can be one or more mixture of Poly Brominated Diphenyl Ethers, TDE, brominated Polystyrene, brominated polystyrene, brominated epoxy resin, brominated polycarbonate; Lubricant is the ultra-high molecular weight polysiloxane; Oxidation inhibitor is composite 1010/168 (1: 1) of four [3-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester primary antioxidants and tricresyl phosphite (2,4-di-t-butyl phenyl ester) auxiliary anti-oxidant.
In the present invention, take by weighing PA6 and ABS by weight ratio, mix; Take by weighing compatilizer and composite flame-retardant agent by weight ratio, mix; Take by weighing lubricant and oxidation inhibitor by weight ratio, mix; The above-mentioned material that mixes joined in the mixing tank together continue to mix until evenly; Mixed raw materials is put into the loading hopper of twin screw extruder, through melt extruding, granulation, fully plasticizing, fusion, compound, again through extrude, tie rod, cooling, pelletizing, oven dry and packing; Complete processing is as follows: twin screw extruder one district 215-240 ℃, two district 215-240 ℃, three district 215-240 ℃, four district 215-240 ℃, five district 215-240 ℃, six district 215-240 ℃, seven district 215-240 ℃, eight district 215-240 ℃; The screw rod revolution is controlled at 350 rev/mins; The residence time 2~10min.
Wherein, advantage such as PA6 has wear-resisting, anti-solvent, oil resistant, use temperature are wide is the engineering plastics of current production rate maximum.
ABS combines glossiness that vinylbenzene has and formability, vinyl cyanide and has rigidity and resistance to chemical reagents and excellent mechanical property, the shock-resistance that divinyl has, and can improve dimensional stability, shock strength, chemical resistant properties and the processing characteristics of nylon with nylon blending.
Because belonging to the adding of thermodynamics incompatible material acrylonitrile-styrene-copolymer-maleic anhydride, nylon and ABS can greatly improve both consistencies, improve the shock strength and the elongation at break of material, but because the fragility of acrylonitrile-styrene-copolymer-maleic anhydride self, add excessive acrylonitrile-styrene-copolymer-maleic anhydride and can reduce the impact of material on the contrary, therefore the relatively more suitable addition of compatilizer is 1-20%, and better addition is 3-15%.
Composite flame-retardant agent is by brominated flame-retardant with antimonous oxide is composite forms in the fire-retardant PA6/ABS mixture of the present invention, the interpolation of fire retardant has certain influence to the impact property of whole material system, but because brominated flame-retardant and antimonous oxide have good synergistic, the flame retarding efficiency height, do not need excessive interpolation, comparatively Shi Yi addition is 5-30%, and better addition is 13-25%.
For ease of the present invention is further understood, now describe the present invention in conjunction with specific embodiments:
Embodiment 1:
Weight ratio PA6 51%, ABS 20%, compatilizer 6.4%, composite flame-retardant agent (TDE 15%, antimonous oxide 7%), lubricant 0.3%, 1,010 0.15%, 168 0.15% are mixed in plastic containers; Mixed raw materials is put into the loading hopper of twin screw extruder, through melt extruding, granulation, fully plasticizing, fusion, compound, again through extrude, tie rod, cooling, pelletizing, oven dry and packing; Complete processing is as follows: 230 ℃ in twin screw extruder one district, 235 ℃ in two districts, 235 ℃ in three districts, 235 ℃ in four districts, 235 ℃ in five districts, 230 ℃ in six districts, 230 ℃ in seven districts, 230 ℃ in eight districts; The screw rod revolution is controlled at 350 rev/mins; The residence time 2~10min.
Embodiment 2
Weight ratio PA6 35.5%, ABS 35.5%, compatilizer 6.4%, composite flame-retardant agent (TDE 15%, antimonous oxide 7%), lubricant 0.3%, 1,010 0.15%, 168 0.15% are mixed in plastic containers; Mixed raw materials is put into the loading hopper of twin screw extruder, through melt extruding, granulation, fully plasticizing, fusion, compound, again through extrude, tie rod, cooling, pelletizing, oven dry and packing; Complete processing is as follows: 230 ℃ in twin screw extruder one district, 235 ℃ in two districts, 235 ℃ in three districts, 235 ℃ in four districts, 235 ℃ in five districts, 230 ℃ in six districts, 230 ℃ in seven districts, 230 ℃ in eight districts; The screw rod revolution is controlled at 350 rev/mins; The residence time 2~10min.
Embodiment 3
Weight ratio PA6 34.5%, ABS 34.5%, compatilizer 6.4%, composite flame-retardant agent (brominated polystyrene 18%, antimonous oxide 6%), lubricant 0.3%, 1,010 0.15%, 168 0.15% are mixed in plastic containers; Mixed raw materials is put into the loading hopper of twin screw extruder, through melt extruding, granulation, fully plasticizing, fusion, compound, again through extrude, tie rod, cooling, pelletizing, oven dry and packing; Complete processing is as follows: 230 ℃ in twin screw extruder one district, 235 ℃ in two districts, 235 ℃ in three districts, 235 ℃ in four districts, 235 ℃ in five districts, 230 ℃ in six districts, 230 ℃ in seven districts, 230 ℃ in eight districts; The screw rod revolution is controlled at 350 rev/mins; The residence time 2~10min.
Embodiment 4:
Weight ratio PA6 20%, ABS 51%, compatilizer 6.4%, composite flame-retardant agent (TDE 15%, antimonous oxide 7%), lubricant 0.3%, 1,010 0.15%, 168 0.15% are mixed in plastic containers; Mixed raw materials is put into the loading hopper of twin screw extruder, through melt extruding, granulation, fully plasticizing, fusion, compound, again through extrude, tie rod, cooling, pelletizing, oven dry and packing; Complete processing is as follows: 225 ℃ in twin screw extruder one district, 230 ℃ in two districts, 235 ℃ in three districts, 235 ℃ in four districts, 235 ℃ in five districts, 230 ℃ in six districts, 230 ℃ in seven districts, 225 ℃ in eight districts; The screw rod revolution is controlled at 330 rev/mins; The residence time 2~10min.
Embodiment 5:
Weight ratio PA6 61%, ABS 12%, compatilizer 4.4%, composite flame-retardant agent (TDE 15%, antimonous oxide 7%), lubricant 0.3%, 1,010 0.15%, 168 0.15% are mixed in plastic containers; Mixed raw materials is put into the loading hopper of twin screw extruder, through melt extruding, granulation, fully plasticizing, fusion, compound, again through extrude, tie rod, cooling, pelletizing, oven dry and packing; Complete processing is as follows: 230 ℃ in twin screw extruder one district, 235 ℃ in two districts, 235 ℃ in three districts, 235 ℃ in four districts, 235 ℃ in five districts, 230 ℃ in six districts, 230 ℃ in seven districts, 230 ℃ in eight districts; The screw rod revolution is controlled at 350 rev/mins; The residence time 2~10min.
Performance test:
Tensile strength is tested by the GB/T1040 standard.Specimen types is the I type, batten size (mm): 170 (length) * (20 ± 0.2) (end width) * (4 ± 0.2) (thickness), and draw speed is 50mm/min;
Flexural strength and modulus in flexure are tested by the GB9341/T standard.Specimen types is specimen size (mm): (80 ± 2) * (10 ± 0.2) * (4 ± 0.2), rate of bending are 20mm/min;
Notched Izod impact strength is tested by the GB/T1043 standard.Specimen types is the I type, specimen size (mm): (80 ± 2) * (10 ± 0.2) * (4 ± 0.2); The breach type is a category-A, and the breach residual thickness is 3.2mm.
Embodiment 1~5 prescription and material property see Table 1:
Table 1
Project Testing method Unit Index
Embodiment 1 Embodiment 2 Embodiment 3 Embodiment 4 Embodiment 5
Tensile strength GB/T1040 MPa 46.0 41.5 40.6 35.8 48.0
Elongation at break GB/T1040 38.0 45.0 43.5 48.6 39
Flexural strength GB9341/T MPa 65 48.5 50.0 42.0 70
Modulus in flexure GB9341/T MPa 2150 1650 1700 1500 2430
Notched Izod impact strength GB/T1043 KJ/M2 9.6 14.5 11.5 15.0 7.8
Flame retardant properties UL-94 0.8mm V0 V0 V0 V0 V0
From embodiment 1, the adding of fire retardant increases the anti-flaming function of material, and is very little to the influence of the physical and mechanical property of material.
From embodiment 2~5, the adding of fire retardant is very little to the physical and mechanical property influence of material.The consideration of comprehensive flame retardant effect and cost, the optimum addition of fire retardant is 13-25%.
More than a kind of PA6/ABS alloy material provided by the present invention and preparation method thereof is described in detail, used specific case herein principle of the present invention and embodiment are set forth, the explanation of above embodiment just is used for helping to understand method of the present invention and core concept thereof; Simultaneously, for one of ordinary skill in the art, according to thought of the present invention, the part that all can change in specific embodiments and applications, in sum, this description should not be construed as limitation of the present invention.

Claims (9)

1, a kind of PA6/ABS alloy material is characterized in that, its composition is (%) by weight ratio:
PA6 20-65%;
ABS 10-70%;
Compatilizer 0.1-20%;
Composite flame-retardant agent 5-30%;
Lubricant 0.1-0.6%;
Oxidation inhibitor 0.1-1.2%.
2, PA6/ABS alloy material as claimed in claim 1 is characterized in that: the relative viscosity of described PA6 is 2.4-3.8PS.
3, PA6/ABS alloy material as claimed in claim 1 or 2 is characterized in that: ABS is an acrylonitrile-butadiene-styrene terpolymer, and its rubber content is 15-70%.
4, claim 1 or 2 described PA6/ABS alloy materials, it is characterized in that: compatilizer is ABS-g-MAH, acrylonitrile-styrene-copolymer-maleic anhydride or SEBS-g-MAH.
5, PA6/ABS alloy material as claimed in claim 1 or 2 is characterized in that: described composite flame-retardant agent is a brominated flame-retardant and antimonous oxide is composite forms.
6, PA6/ABS alloy material as claimed in claim 5 is characterized in that: described brominated flame-retardant is one or more the mixture in Poly Brominated Diphenyl Ethers, TDE, brominated Polystyrene, brominated polystyrene, brominated epoxy resin, the brominated polycarbonate.
7, PA6/ABS alloy material as claimed in claim 6 is characterized in that: described lubricant is the ultra-high molecular weight polysiloxane.
8, PA6/ABS alloy material as claimed in claim 6 is characterized in that: described oxidation inhibitor is the composite of four [3-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester primary antioxidants and tricresyl phosphite (2,4-di-t-butyl phenyl ester) auxiliary anti-oxidant.
9, a kind of preparation method of PA6/ABS alloy material as claimed in claim 1 is characterized in that, comprises step:
A: take by weighing PA6 and ABS by weight ratio, mix;
B: take by weighing compatilizer and composite flame-retardant agent by weight ratio, mix;
C: take by weighing lubricant and oxidation inhibitor by weight ratio, mix, the above-mentioned material that mixes is joined in the mixing tank together continue to mix until evenly;
D: mixed raw materials is put into the loading hopper of twin screw extruder, through melt extruding, granulation, fully plasticizing, fusion, compound, again through extrude, tie rod, cooling, pelletizing, oven dry and packing; Complete processing is as follows: twin screw extruder one district 215-240 ℃, two district 215-240 ℃, three district 215-240 ℃, four district 215-240 ℃, five district 215-240 ℃, six district 215-240 ℃, seven district 215-240 ℃, eight district 215-240 ℃; The screw rod revolution is controlled at 350 rev/mins; The residence time 2~10min.
CNA2007100746873A 2007-06-01 2007-06-01 PA6 / ABS alloy material, and preparation method Pending CN101092501A (en)

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CN101875782A (en) * 2010-03-31 2010-11-03 深圳市科聚新材料有限公司 Bromine/stibium flame retardancy reinforced polyamide composite material and preparation method thereof
CN101899210A (en) * 2010-07-16 2010-12-01 深圳市科聚新材料有限公司 High glowing filament nylon and preparation method thereof
CN101942174A (en) * 2010-10-25 2011-01-12 江苏技术师范学院 Halogen-free flame-retardant ABS/PA6 alloy material and preparation method thereof
CN102199347A (en) * 2011-03-31 2011-09-28 上海金玺实验室有限公司 Modified PA/ABS composite material with boiling resistance, high intensity and superior toughness and preparation method thereof
CN102604374A (en) * 2012-02-29 2012-07-25 杨谢 Formula and preparing method of PA6 (Polyamide-6) and ABS (Acrylonitrile Butadiene Styrene) alloy material
CN102656232A (en) * 2009-12-16 2012-09-05 罗地亚经营管理公司 Polyamide composition with low thermal conductivity
CN102850782A (en) * 2011-06-29 2013-01-02 合肥杰事杰新材料股份有限公司 PA/ABS alloy material and preparation method thereof
CN102993699A (en) * 2012-10-19 2013-03-27 芜湖市鑫海橡塑制品有限责任公司 Polytetrafluoroethylene modified nylon polyamide 6 (PA6) material for automobile oil pipe and preparation method of polytetrafluoroethylene modified nylonPA6 material
CN103160110A (en) * 2011-12-14 2013-06-19 上海杰事杰新材料(集团)股份有限公司 Halogen-free flame retardant PA / ABS blend and preparation method thereof
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CN102993699A (en) * 2012-10-19 2013-03-27 芜湖市鑫海橡塑制品有限责任公司 Polytetrafluoroethylene modified nylon polyamide 6 (PA6) material for automobile oil pipe and preparation method of polytetrafluoroethylene modified nylonPA6 material
CN103254635A (en) * 2013-03-15 2013-08-21 东风(十堰)非金属部件有限公司 Rare earth modified toughening nylon material and its preparation method
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