CN103937271A - Matte spraying-free polycarbonate/acrylonitrile-butadiene-styrene alloy and preparation method thereof - Google Patents

Matte spraying-free polycarbonate/acrylonitrile-butadiene-styrene alloy and preparation method thereof Download PDF

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CN103937271A
CN103937271A CN201410177444.2A CN201410177444A CN103937271A CN 103937271 A CN103937271 A CN 103937271A CN 201410177444 A CN201410177444 A CN 201410177444A CN 103937271 A CN103937271 A CN 103937271A
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eva
parts
alloy
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CN103937271B (en
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刘春艳
王正有
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SHANGHAI ZHONGLEI NEW MATERIAL TECHNOLOGY Co Ltd
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SHANGHAI ZHONGLEI NEW MATERIAL TECHNOLOGY Co Ltd
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    • 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
    • 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
    • B29C48/25Component 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
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L69/00Compositions of polycarbonates; Compositions of derivatives of polycarbonates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • 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
    • B29C2948/9258Velocity
    • 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
    • B29C2948/92609Dimensions
    • B29C2948/92657Volume or quantity
    • 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
    • B29C2948/92504Controlled parameter
    • B29C2948/92761Mechanical properties
    • 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
    • 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
    • B29C2948/9298Start-up, shut-down or parameter setting phase; Emergency shut-down; Material change; Test or laboratory equipment or studies

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

Abstract

The invention provides a matte spraying-free polycarbonate/acrylonitrile-butadiene-styrene alloy and a preparation method thereof in the technical field of the high polymer materials. The matte spraying-free polycarbonate/acrylonitrile-butadiene-styrene alloy is composed of the following components: 40-80 parts of PC-g-EVA (Ethylene-Vinyl acetate), 20-60 parts of ABS (Acrylonitrile Butadiene Styrene), 5-30 parts of ACS (Acrylonitrile Chlorinated-Polyethylene Styrene), 1-10 parts of silicon dioxide, 0.1-2 parts of antioxidant, and 0.05-1 part of thermal stability; the luster of the polycarbonate/acrylonitrile-butadiene-styrene alloy reaches 4-25Gu at 60 DEG C. The PC/ABS alloy achieves the matte effect by use of the characteristic that ACS and PC-g-EVA are incompatible; meanwhile, the inorganic powder silicon dioxide is added so that the PC/ABS alloy has the matte effect; ACS and silicon dioxide are used for achieving the synergetic matte effect. Meanwhile, as the alloy prepared by the preparation method contains EVA, the problem of low impact property of the inorganic powder modified matte PC/ABS is solved. Moreover, as ACS is added, the alloy materials has flame-retarding, anti-aging and weather-resisting characteristics.

Description

Dumb light exempts to spray PC/Abs Alloy And Preparation Method
Technical field
What the present invention relates to is a kind of method of technical field of polymer materials, specifically a kind of dumb light exempt to spray polycarbonate (PC)/Bing Xi Jing ?Ding bis-Xi ?vinylbenzene (ABS) Alloy And Preparation Method.
Background technology
For the plastics for automotive trim and office electronic apparatus case material, require surface luster soft, i.e. so-called delustring or dumb light effect.Automotive trim plastic part in selection and design, need to reduce dazzle by surperficial diffuse-reflectance method conventionally, in order to avoid disturb motorist vision; Office electronic apparatus shell, in selection, requires dumb light effect too, reduces dazzle, in order to avoid clerical workforce is felt tired.So automotive upholstery, office electronic apparatus shell are carried out to delustring or matte management, to obtain comfortable driving sensation or office sensation.Automotive upholstery is as inside gadgets such as dashboards, and office electronic apparatus all shows to have similar demand to product as housings such as computer casing, keyboard, duplicating machine.
In PC/ABS, can add dumb light filler or high polymer carries out dumb light modification, but mixture mechanical property can reduce as shock strength, ductility retain, flame retardant resistance and weathering resistance are bad simultaneously.
Through the retrieval of prior art is found, Chinese patent literature CN103194033A open (bulletin) day 2013.07.10, a kind of blending and modifying resin that can be applicable to lead-acid storage battery outer case is disclosed, raw material by following weight proportion is made: ABS resin 60 ?80%, PC resin 20 ?30%, EVA multipolymer 5 ?10%, compatilizer 2 ?10%.It is compatilizer that the present invention adopts the graft copolymer of ABS and maleic anhydride, and ABS, PC and the strong tri-kinds of polymkeric substance of EVA of toughness are carried out to blend, high strength and the flame retardant resistance of the existing PC of hybrid resin obtaining.But the blending resin that this technology obtains does not reduce the effect of gloss.
Summary of the invention
The present invention is directed to prior art above shortcomings, propose a kind of dumb light exempt to spray polycarbonate/Bing Xi Jing ?Ding bis-Xi ?styrene alloy and preparation method thereof, utilize Bing Xi Jing ?Lvization Ju Yi Xi ?styrol copolymer (ACS) and PC ?g ?the incompatible PC/ABS of the making alloy of EVA there is dumb light effect, add inorganic powder silicon-dioxide simultaneously and make PC/ABS alloy have dumb light effect, ACS and silicon-dioxide play the effect of collaborative dumb light effect.Simultaneously the present invention is prepared in gained alloy owing to containing EVA, has solved the not high problem of inorganic powder modification dumb light PC/ABS impact property.Further, owing to having increased ACS composition, make alloy material there is fire-retardant, ageing-resistant and weathering characteristics.
The present invention is achieved by the following technical solutions: the present invention by the reaction of PC and EVA melt blending is extruded pelletizing obtain PC ?g ?EVA graft copolymer, with ABS, ACS, silicon-dioxide and auxiliary agent blending extrusion, obtain polycarbonate/Bing Xi Jing ?Ding bis-Xi ?styrene alloy.
Described PC and the weight ratio of EVA are (60~90): (40~10), are preferably 80:20.
In described PC and EVA melt blending, adopt dibutyltin oxide (DBTO) as catalyzer, the temperature of extruding after melt blending is 230~255 DEG C, and screw speed is 100~200r/min; Percentage of grafting is 5~10%.
Described PC ?g ?the weight ratio (50~70) of EVA graft copolymer, ABS, ACS, silicon-dioxide and auxiliary agent: (10~30): (0~40): (2~5): 0.3.
Described Bing Xi Jing ?Lvization Ju Yi Xi ?the terpolymer of styrol copolymer (ACS) for adopting mass polymerization to be prepared by vinyl cyanide (AN), chlorinatedpolyethylene (CPE) and vinylbenzene (St), and chlorinated polyethylene rubber part by weight be 25 ?35%, in CPE cl content be 40 ?70%, cl content preferably 45% in CPE.
Described Yi Xi ?in vinyl acetate copolymer (EVA) VA content be 20 ?40%, preferably 25%.
Described auxiliary agent includes but not limited to: Hinered phenols antioxidant, phosphite ester kind antioxidant, thermo-stabilizer etc.
Described oxidation inhibitor is the one or more combination in Hinered phenols antioxidant and phosphite ester kind antioxidant, be preferably antioxidant 1010 and irgasfos 168, i.e. four [methyl-β-(3,5-di-tert-butyl-hydroxy phenyl) propionic ester] tetramethylolmethane or three [2,4-di-tert-butyl-phenyl] phosphorous acid ester.
The present invention relates to polycarbonate/Bing Xi Jing that aforesaid method prepares ?Ding bis-Xi ?styrene alloy, its 60 ° of lower gloss reach 4~25 gloss unit (Gu).
Described polycarbonate/Bing Xi Jing ?Ding bis-Xi ?the flame retardant resistance of styrene alloy reach V ?2 grades even V ?1 grade.
The present invention relates to above-mentioned polycarbonate/Bing Xi Jing ?Ding bis-Xi ?the application of styrene alloy, use it for the automotive upholstery of the weather-proof dumb light of preparation.Because will effectively prevent the impact of reflection on driver, increase traffic safety, all at present treatment processs that most of automotive upholsteries adopt are on the market coated matte paint.If adopt dulling material to be made into inside gadget, can remove the operation of spraying from.Not only can be cost-saving, can reduce the environmental pollution causing because of spraying simultaneously.
Embodiment
Below embodiments of the invention are elaborated, the present embodiment is implemented under taking technical solution of the present invention as prerequisite, provided detailed embodiment and concrete operating process, but protection scope of the present invention is not limited to following embodiment.
Embodiment 1
Below in conjunction with embodiment, the present invention is described in further detail, but the present invention is not limited to following examples.The polycarbonate that following examples the are used bisphenol A polycarbonate PC lexan141R that is GE company, molecular weight be 25000 ?28000g/mol.Bing Xi Jing ?Ding bis-Xi ?styrol copolymer use the ABS747S of the strange U.S. industry in Taiwan, butadiene content be 20 ?40wt%.Oxidation inhibitor use four [β ?(3,5 ?Er Te Ding Ji ?4 ?hydroxy phenyl) propionic acid] pentaerythritol ester, commodity are called Irganox1010, Ciba fine chemicals produces, and three (2,4 ?di-tert-butylphenols) phosphorous acid ester, commodity are called Irganox168, and Ciba fine chemicals produces.The present invention use ZE that German Berstorff company produces ?25 twin screw extruders.
The present embodiment comprises the following steps:
Grafting PC ?g ?the making of EVA: 80 parts of PC, 20 points of EVA, 2 parts of DBTO, 0.1 part of Hinered phenols antioxidant, 0.1 part of phosphite ester kind antioxidant are joined after evenly mixing with high-speed mixer and in twin screw extruder, carry out melt blending, one district's temperature is 190 DEG C, two district's temperature are 210 DEG C, three district's temperature are 220 DEG C, four district's temperature are 230 DEG C, five district's temperature are 240 DEG C, six district's temperature are 250 DEG C, seven district's temperature are 255 DEG C, eight district's temperature are 255 DEG C, nine district's temperature are 250 DEG C, and screw speed is 250 revs/min, and the residence time is 2 minutes.Cooling after extruding, dry, pelletizing, obtain PC ?g ?EVA.
By PC ?g ?EVA, ABS, ACS, silicon-dioxide and Hinered phenols antioxidant, phosphite ester kind antioxidant, thermo-stabilizer after evenly mixing with high-speed mixer according to the proportioning of embodiment, join and in twin screw extruder, carry out melt blending, one district's temperature is 190 DEG C, two district's temperature are 220 DEG C, three district's temperature are 230 DEG C, four district's temperature are 240 DEG C, five district's temperature are 250 DEG C, six district's temperature are 260 DEG C, seven district's temperature are 260 DEG C, eight district's temperature are 260 DEG C, nine district's temperature are 255 DEG C, and screw speed is 250 revs/min, and the residence time is 2 minutes.Cooling after extruding, dry, pelletizing, obtain dumb light PC/ABS alloy.
Notched Izod impact strength is tested by ASTM D256, and specimen size is 64mm*12.7mm*3.2mm, and notch depth is 2.2mm, testing apparatus be Britain Ray ?the shock-testing machine of Ran company.
ASTM D2457 is pressed in surface luster test, adopts Gardner's glossmeter to test in the thick model of smooth 3mm surface, records 60 ° of gloss numbers, and gloss unit is GU, and standard black sheet glass gloss level is wherein 100GU.
Flame retardant rating test press UL ?94, testing apparatus be U.S. ATLAS HVUL ?2 vertical combustion instrument.
Each weight percent and test physical property result are as following table:
PC ?g ?the PC:EVA ratio of EVA be 60~90:40~10, in following comparative example and embodiment, PC:EVA ratio is 80:20.
Table 1
In table 1, the alloy material impact physical property that does not add inorganic silicon dioxide powder is higher, and the alloy material that is added with inorganic silicon dioxide impacts and declines obviously.
By PC be replaced with PC ?g ?after EVA, PC/ABS alloy material impacts higher, add PC ?g ?alloy material is owing to containing EVA composition after EVA graft copolymer, impelling strength increases, and has improved inorganic powder modification dumb light PC/ABS and has impacted low problem.
The interpolation of inorganic silicon dioxide powder and ACS multipolymer, in PC/ABS alloy, gloss reducing is obvious, and alloy gloss the interpolation content with the two increase and reduce gradually, and the two plays collaborative dumb light modifying function.The gloss of embodiment 7 interalloy materials reaches 3.5 best gloss unit Gu.
In above comparative example and embodiment, not adding the alloy material UL94 of ACS fire-retardant is HB level, add after ACS alloy material flame retardant properties arrive V ?2 with V ?1 grade.

Claims (10)

1. a dumb light exempts to spray polycarbonate/the third alkene nitrile ?fourth two alkene ?styrene alloys and preparation method thereof, it is characterized in that, by the reaction of PC and EVA melt blending is extruded pelletizing obtain PC ?g ?EVA graft copolymer, with ABS, ACS, silicon-dioxide and auxiliary agent blending extrusion, obtain polycarbonate/Bing Xi Jing ?Ding bis-Xi ?styrene alloy;
Described PC and the weight ratio of EVA are (60~90): (40~10);
In described PC and EVA melt blending, adopt dibutyltin oxide as catalyzer, the temperature of extruding after melt blending is 230~255 DEG C, and screw speed is 100~200r/min; Percentage of grafting is 5~10%;
Described PC ?g ?the weight ratio (50~70) of EVA graft copolymer, ABS, ACS, silicon-dioxide and auxiliary agent: (10~30): (0~40): (2~5): 0.3.
2. method according to claim 1, is characterized in that, described auxiliary agent comprises: Hinered phenols antioxidant, phosphite ester kind antioxidant and thermo-stabilizer.
3. method according to claim 1, is characterized in that, described PC and the weight ratio of EVA are 80:20.
4. method according to claim 1, it is characterized in that, described ACS adopts the terpolymer that prepared by vinyl cyanide, chlorinatedpolyethylene and vinylbenzene of mass polymerization, and chlorinated polyethylene rubber part by weight be 25 ?35%, in CPE cl content be 40 ?70%.
5. method according to claim 1, is characterized in that, in described EVA VA content be 20 ?40%.
6. method according to claim 1, it is characterized in that, described PC and EVA melt blending refer to: after with high-speed mixer, PC and EVA evenly being mixed, join and in twin screw extruder, carry out melt blending, wherein: district's temperature is 190 DEG C, two district's temperature are 210 DEG C, three district's temperature are 220 DEG C, four district's temperature are 230 DEG C, five district's temperature are 240 DEG C, and six district's temperature are 250 DEG C, and seven district's temperature are 255 DEG C, eight district's temperature are 255 DEG C, nine district's temperature are 250 DEG C, and screw speed is 250 revs/min, and the residence time is 2 minutes.
7. method according to claim 1, it is characterized in that, described PC ?g ?EVA graft copolymer and ABS, ACS, silicon-dioxide and auxiliary agent blending extrusion refer to: after evenly mixing by high-speed mixer, join and in twin screw extruder, carry out melt blending, one district's temperature is 190 DEG C, two district's temperature are 220 DEG C, three district's temperature are 230 DEG C, four district's temperature are 240 DEG C, five district's temperature are 250 DEG C, six district's temperature are 260 DEG C, seven district's temperature are 260 DEG C, eight district's temperature are 260 DEG C, nine district's temperature are 255 DEG C, screw speed is 250 revs/min, the residence time is 2 minutes, rear cooling finally by extruding, dry, pelletizing, obtain dumb light PC/ABS alloy.
8. polycarbonate/Bing Xi the Jing preparing according to method described in claim 1 or 2 ?Ding bis-Xi ?styrene alloy, it is characterized in that, its component is: PC ?g ?EVA40 ?80 parts, ABS20 ?60 parts, ACS5 ?30 parts, silicon-dioxide 1 ?10 parts, oxidation inhibitor 0.1 ?2 parts, thermo-stabilizer 0.05 ?1 part, this polycarbonate/Bing Xi Jing ?Ding bis-Xi ?60 ° of lower gloss of styrene alloy reach 4~25Gu.
Polycarbonate/Bing Xi Jing according to claim 8 ?Ding bis-Xi ?styrene alloy, it is characterized in that, its component is: PC ?g ?EVA70 ?90 parts, ABS10 ?30 parts, ACS5 ?30 parts, silicon-dioxide 2 ?5 parts, 0.2 part, oxidation inhibitor, 0.1 part of thermo-stabilizer.
10. relate to an application for the polycarbonate/the third alkene nitrile ?fourth two alkene ?styrene alloys described in above-mentioned arbitrary claim, it is characterized in that, use it for the automotive upholstery of the weather-proof dumb light of preparation.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106589778A (en) * 2016-12-21 2017-04-26 深圳市捷创新材料有限公司 High-molecular polymer applicable to blow molding and blow molding process of high-molecular polymer
CN107459756A (en) * 2017-08-25 2017-12-12 广东壹豪新材料科技股份有限公司 A kind of PC/AS/UHMWPE composites for exempting from spraying and preparation method thereof

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Publication number Priority date Publication date Assignee Title
CA2025377A1 (en) * 1989-11-16 1991-05-17 James L. Derudder Low gloss flame retardant thermoplastic blends
CN101787192A (en) * 2009-10-15 2010-07-28 上海锦湖日丽塑料有限公司 Low-gloss polycarbonate styreneresin composite and preparation method thereof
CN102115583A (en) * 2009-12-30 2011-07-06 上海金发科技发展有限公司 Weather-resistant low-gloss high-fluidity polycarbonate composition

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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