Embodiment
In order to make the technical problem to be solved in the present invention, technical scheme and beneficial effect clearer, below in conjunction with embodiment, the present invention is further elaborated.Should be appreciated that specific embodiment described herein, only in order to explain the present invention, is not intended to limit the present invention.
The embodiment of the present invention provides the alloy material of a kind of PC and ASA, comprises following component (in parts by weight):
Wherein, described polycarbonate is that weight-average molecular weight is 3-5 ten thousand, and density is 1.18-1.20g/cm
3Polycarbonate, described acrylonitrile-styrene-acrylic ester is acrylate rubber like body and vinyl cyanide, cinnamic graft copolymer, density is 1.04-1.07g/cm
3, and wherein acrylate rubber like body content is 30%-60%.
Particularly, in PC/ASA alloy material of the present invention, described compatilizer can be Zelan 338 (SMA), wherein maleic anhydride content is 15%-30%, also can be one or more in the graft copolymer (PS-g-MAH) of graft copolymer (ASA-g-MAH), vinylbenzene and maleic anhydride of ABS grafted maleic anhydride (ABS-g-MAH), ASA and maleic anhydride, wherein the content of the content of maleic anhydride in compatilizer is 3-30wt%.
It should be noted that the degree (%) used in specification sheets of the present invention, unless specified otherwise is arranged, otherwise all in weight percentage.
Particularly, in PC/ASA alloy material of the present invention, described toughner is that organosilicon/vinylformic acid is core, and methyl methacrylate is the nucleocapsid structure body of shell, and wherein silicone content is 10%-30%.
In the embodiment of the present invention, toughness reinforcing dose of organosilicon has nucleocapsid structure toughner, can significantly improve the weather resistance of alloy, and element silicon wherein can effectively be put forward heavy alloyed flame retardant properties.
Particularly, in PC/ASA alloy material of the present invention, described fire retardant can or have halogen fire retardant for halogen-free flame retardants.Wherein halogen-free flame retardants is the composition of phosphoric acid ester fire retardant and silicone flame retardant or Sulfonates fire retardant, and in the phosphoric acid ester fire retardant of halogen-free flame retardants, phosphorus content is greater than 9.0% by weight percentage; There is halogen fire retardant to can be bromide fire retardant, comprise brominated triazine based flame retardant, ten bromine class (TDE) fire retardants etc.
In the embodiment of the present invention, if use halogen-free flame-retardant system, can greatly reduce the consumption of halogen-free flame retardants by adding silicone flame retardant or Sulfonates fire retardant, significantly improve simultaneously the flame retarding efficiency of gained alloy material.If use when the halogen fire retardant system is arranged, can reach high heat-resisting effect.
Particularly, in PC/ASA alloy material of the present invention, described fire retarding synergist is the SAN(styrene-acrylonitrile) tetrafluoroethylene that coats, wherein, in this fire retarding synergist in SAN the mass ratio of vinylbenzene and vinyl cyanide be 4:1-2:1, and the mass ratio of tetrafluoroethylene and SAN is 1:1-1:3, thereby tetrafluoroethylene fibrosis under the effect of the shearing force that is subject to screw rod forms reticulated structure, plays the effect of anti-drippage.
Particularly, in PC/ASA alloy material of the present invention, described photostabilizer is the benzotriazole category light absorber, as UV-5411 (2 (the tertiary octyl phenyl of 2-hydroxyl-5-) benzotriazole), utilize this kind photostabilizer can shielding, uv reflectance or absorb ultraviolet ray and be translated into harmless heat energy.
In the embodiment of the present invention, the PC/ASA alloy material also can contain the component that lubricant and oxidation inhibitor etc. are conducive to improve the alloy material performance.Use therein lubricant can be ethene stearylamide or ethylene bis stearamide, as: EBS etc.
The oxidation inhibitor used in PC/ASA alloy material of the present invention can-3-(3-tertiary butyl-4-hydroxy-5-aminomethyl phenyl two as triglycol) vinyl cyanide or tricresyl phosphite (2, the 4-di-tert-butyl-phenyl) a kind of in ester, or by four [3-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester and tricresyl phosphite (2,4-di-tert-butyl-phenyl) ester mix by the weight ratio of 1:1-1:3.
The PC/ASA alloy material of the embodiment of the present invention be take PC and ASA and is resin matrix, by adding organosilicon toughner, effectively reduces the internal stress of resin matrix, has increased the toughness (comprising low-temperature flexibility) of PC/ASA alloy material; Use phenylethylene-maleic anhydride (maleic anhydride) as compatilizer, wherein contain can with maleic anhydride and the vinylbenzene of PC and the effective combination of ASA, make the intermolecular also combination of having an effect of each component, thereby form constitutionally stable PC/ASA alloy material, make prepared alloy material have good mechanical property; Select efficient halogen-free silicon-type or sulfonate fire retardant and the effective combination of phosphoric acid ester fire retardant, make the flame retardant properties of gained alloy material reach the requirement of U.S. UL945VA level, simultaneously, greatly reduce the consumption of phosphoric acid ester fire retardant, and effectively improved the resistance toheat of this alloy.
The embodiment of the present invention also provides the preparation method of the alloy material of a kind of PC and ASA, and the method comprises the following steps:
S01. take each component of the alloy material that forms PC of the present invention and ASA, for example take each component of following parts by weight:
Above-mentioned each component that S02. will take is poured in agitation vat and is stirred 8-20min, and mixing speed is 400-500r/min, obtains mixture;
S03. the said mixture material is adopted to the twin screw extruder extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 140~160 ℃, a district, two 210~230 ℃, 190~210 190~210 ℃, 4th district, ℃, 3rd district, districts, five 210~230 ℃, districts, six 210~230 ℃, 220~240 220~240 ℃, 8th district, ℃, 7th district, districts, 230~240 ℃ of heads, the rotating speed of described double-screw extruder screw are 250~300 rev/mins.
The method that the embodiment of the present invention provides is easy and simple to handle.
Below the present invention will be described in detail by specific embodiment.
Embodiment 1
1. in following ratio, take each component, total mass is 5Kg:
Wherein above-mentioned polycarbonate is that weight-average molecular weight is 40,000, and density is 1.20g/cm
3Polycarbonate, described acrylonitrile-styrene-acrylic ester is acrylate rubber like body and vinyl cyanide, cinnamic graft copolymer, density is 1.07g/cm
3, and wherein acrylate rubber like body content is 50%;
Wherein above-mentioned fire retarding synergist is the tetrafluoroethylene that SAN coats, and wherein the mass ratio of tetrafluoroethylene and SAN is 1:1, and in SAN, the mass ratio of vinylbenzene and vinyl cyanide is 4:1.
2. above-mentioned each component that will take is poured in agitation vat and is stirred 20min, and mixing speed is 500r/min, obtains mixture;
3. the said mixture material is adopted to the twin screw extruder extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 150 ℃, a district, two 220 ℃, 200 200 ℃, 4th district, ℃, 3rd district, districts, five 220 ℃, districts, six 220 ℃, 230 230 ℃, 8th district, ℃, 7th district, districts, 240 ℃ of heads, the rotating speed of described double-screw extruder screw are 300 rev/mins.
Embodiment 2
1. in following ratio, take each component, total mass is 5Kg:
Wherein above-mentioned polycarbonate is that weight-average molecular weight is 40,000, and density is 1.20g/cm
3Polycarbonate, described acrylonitrile-styrene-acrylic ester is acrylate rubber like body and vinyl cyanide, cinnamic graft copolymer, density is 1.07g/cm
3, and wherein acrylate rubber like body content is 50%;
In above-mentioned SMA, maleic anhydride content is 20%;
Above-mentioned fire retarding synergist is the SAN(styrene-acrylonitrile) tetrafluoroethylene that coats, and the mass ratio of tetrafluoroethylene and SAN is 1: 2, and in this SAN, the mass ratio of vinylbenzene and vinyl cyanide is 3: 1.
2. above-mentioned each component that will take is poured in agitation vat and is stirred 15min, and mixing speed is 450r/min, obtains mixture;
3. the said mixture material is adopted to the twin screw extruder extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 160 ℃, a district, two 230 ℃, 210 210 ℃, 4th district, ℃, 3rd district, districts, five 230 ℃, districts, six 210 ℃, 240 230 ℃, 8th district, ℃, 7th district, districts, 230 ℃ of heads, the rotating speed of described double-screw extruder screw are 280 rev/mins.
Embodiment 3
1. in following ratio, take each component, total mass is 5Kg:
Wherein above-mentioned polycarbonate is that weight-average molecular weight is 40,000, and density is 1.20g/cm
3Polycarbonate, described acrylonitrile-styrene-acrylic ester is acrylate rubber like body and vinyl cyanide, cinnamic graft copolymer, density is 1.07g/cm
3, and wherein acrylate rubber like body content is 50%;
In above-mentioned SMA, maleic anhydride content is 30%;
Above-mentioned toughner B take organosilicon/vinylformic acid to be core, and methyl methacrylate is that hull shape becomes nucleocapsid structure, and wherein silicone content is 10%-30%.
2. above-mentioned each component that will take is poured in agitation vat and is stirred 10min, and mixing speed is 400r/min, obtains mixture;
3. the said mixture material is adopted to the twin screw extruder extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 140 ℃, a district, two 220 ℃, 200 200 ℃, 4th district, ℃, 3rd district, districts, five 220 ℃, districts, six 210 ℃, 230 230 ℃, 8th district, ℃, 7th district, districts, 230 ℃ of heads, the rotating speed of described double-screw extruder screw are 260 rev/mins.
Embodiment 4
1. in following ratio, take each component, total mass is 5Kg:
Wherein above-mentioned polycarbonate is that weight-average molecular weight is 40,000, and density is 1.20g/cm
3Polycarbonate, described acrylonitrile-styrene-acrylic ester is acrylate rubber like body and vinyl cyanide, cinnamic graft copolymer, density is 1.07g/cm
3, and wherein acrylate rubber like body content is 50%;
In above-mentioned compatilizer ABS grafted maleic anhydride, maleic anhydride content is 20%;
Above-mentioned fire retarding synergist is the SAN(styrene-acrylonitrile) tetrafluoroethylene that coats, and the mass ratio of tetrafluoroethylene and SAN is 1: 2, and in this SAN, the mass ratio of vinylbenzene and vinyl cyanide is 3: 1.
2. above-mentioned each component that will take is poured in agitation vat and is stirred 20min, and mixing speed is 500r/min, obtains mixture;
3. the said mixture material is adopted to the twin screw extruder extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 150 ℃, a district, two 220 ℃, 200 200 ℃, 4th district, ℃, 3rd district, districts, five 220 ℃, districts, six 220 ℃, 230 230 ℃, 8th district, ℃, 7th district, districts, 240 ℃ of heads, the rotating speed of described double-screw extruder screw are 300 rev/mins.
Embodiment 5
1. in following ratio, take each component, total mass is 5Kg:
Wherein above-mentioned polycarbonate is that weight-average molecular weight is 40,000, and density is 1.20g/cm
3Polycarbonate, described acrylonitrile-styrene-acrylic ester is acrylate rubber like body and vinyl cyanide, cinnamic graft copolymer, density is 1.07g/cm
3, and wherein acrylate rubber like body content is 50%;
In above-mentioned compatilizer ABS grafted maleic anhydride, maleic anhydride content is 15%;
Above-mentioned fire retarding synergist is the SAN(styrene-acrylonitrile) tetrafluoroethylene that coats, and the mass ratio of tetrafluoroethylene and SAN is 1: 2, and in this SAN, the mass ratio of vinylbenzene and vinyl cyanide is 3: 1.
2. above-mentioned each component that will take is poured in agitation vat and is stirred 20min, and mixing speed is 500r/min, obtains mixture;
3. the said mixture material is adopted to the twin screw extruder extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 150 ℃, a district, two 220 ℃, 200 200 ℃, 4th district, ℃, 3rd district, districts, five 220 ℃, districts, six 220 ℃, 230 230 ℃, 8th district, ℃, 7th district, districts, 240 ℃ of heads, the rotating speed of described double-screw extruder screw are 300 rev/mins.
The comparative example 1
1. in following ratio, take each component, total mass is 5Kg:
Wherein above-mentioned polycarbonate is that weight-average molecular weight is 40,000, and density is 1.20g/cm
3Polycarbonate, described acrylonitrile-styrene-acrylic ester is acrylate rubber like body and vinyl cyanide, cinnamic graft copolymer, density is 1.07g/cm
3, and wherein acrylate rubber like body content is 50%;
Above-mentioned toughner B take organosilicon/vinylformic acid to be core, and methyl methacrylate is that hull shape becomes nucleocapsid structure, and wherein silicone content is 10%-30%;
Above-mentioned fire retarding synergist is the SAN(styrene-acrylonitrile) tetrafluoroethylene that coats, and the mass ratio of tetrafluoroethylene and SAN is 1: 2, and in this SAN, the mass ratio of vinylbenzene and vinyl cyanide is 3: 1.
2. above-mentioned each component that will take is poured in agitation vat and is stirred 15min, and mixing speed is 450r/min, obtains mixture;
3. the said mixture material is adopted to the twin screw extruder extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 160 ℃, a district, two 230 ℃, 210 210 ℃, 4th district, ℃, 3rd district, districts, five 230 ℃, districts, six 210 ℃, 240 230 ℃, 8th district, ℃, 7th district, districts, 230 ℃ of heads, the rotating speed of described double-screw extruder screw are 280 rev/mins.
The comparative example 2
1. in following ratio, take each component, total mass is 5Kg:
Wherein above-mentioned polycarbonate is that weight-average molecular weight is 40,000, and density is 1.20g/cm
3Polycarbonate, described acrylonitrile-styrene-acrylic ester is acrylate rubber like body and vinyl cyanide, cinnamic graft copolymer, density is 1.07g/cm
3, and wherein acrylate rubber like body content is 50%.
Above-mentioned fire retarding synergist is the SAN(styrene-acrylonitrile) tetrafluoroethylene that coats, and the mass ratio of tetrafluoroethylene and SAN is 1: 2, and in this SAN, the mass ratio of vinylbenzene and vinyl cyanide is 3: 1.
2. above-mentioned each component that will take is poured in agitation vat and is stirred 10min, and mixing speed is 400r/min, obtains mixture;
3. the said mixture material is adopted to the twin screw extruder extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 140 ℃, a district, two 220 ℃, 200 200 ℃, 4th district, ℃, 3rd district, districts, five 220 ℃, districts, six 210 ℃, 230 230 ℃, 8th district, ℃, 7th district, districts, 230 ℃ of heads, the rotating speed of described double-screw extruder screw are 260 rev/mins.
The comparative example 3
1. in following ratio, take each component, total mass is 5Kg:
Wherein above-mentioned polycarbonate is that weight-average molecular weight is 40,000, and density is 1.20g/cm
3Polycarbonate, described acrylonitrile-styrene-acrylic ester is acrylate rubber like body and vinyl cyanide, cinnamic graft copolymer, density is 1.07g/cm
3, and wherein acrylate rubber like body content is 50%.
2. above-mentioned each component that will take is poured in agitation vat and is stirred 20min, and mixing speed is 500r/min, obtains mixture;
3. the said mixture material is adopted to the twin screw extruder extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 150 ℃, a district, two 220 ℃, 200 200 ℃, 4th district, ℃, 3rd district, districts, five 220 ℃, districts, six 220 ℃, 230 230 ℃, 8th district, ℃, 7th district, districts, 240 ℃ of heads, the rotating speed of described double-screw extruder screw are 300 rev/mins.
Performance test and evaluation:
Particle prepared by above-described embodiment 1-5 and comparative example 1-3 first in convection oven under the condition of 80-100 ℃ dry 2 hours, then will dried particle material make the standard testing batten with injection moulding machine and test.
(1) aging (weather-proof) test: use Xenon lamp weather resistance test box to test, its yield of radiation is 1.12kw/m
2, 24h is a cycle, and duration of test runs is 10 cycles (they being 240h), and in each cycle, 8h irradiates, and 16h does not irradiate, and the radiation amount in each cycle is 8.96kwh/m
2.Temperature during the proofing box internal radiation is 75 ℃, and the light source of employing is relatively that approach and the xenon arc lamp that install infrared filter glass additional of spectral distribution and sunlight, and irradiation finishes laggard circumstances in which people get things ready for a trip difference analysis and shock test.Wherein, notched Izod impact strength is tested by the ASTMD-256 standard.Specimen types is the I type, specimen size (mm): (63 ± 2) * (12.45 ± 0.2) * (3.1 ± 0.2); The breach type is category-A, and the breach residual thickness is 1.9mm; HDT(Heat deflectiontemperature, heat-drawn wire, reflection material thermal resistance) to test and use computermatic heat-drawn wire trier to carry out, condition is carried out according to ASTMD648, and test condition is 1.8MPa, unannealed, 6.4mm; Other performances are all tested according to ASTM standard batten.
(2) flame retardant test usage level testing vertical flammability instrument, test according to the UL94 standard.
Shown in the material properties test data following table 1 of embodiment 1-5 and comparative example (Comparative Examples) 1-3:
Table 1 material properties test data results
We can find out from upper table data, use toughness reinforcing dose of organosilicon, and the material at low temperature impact resistance is better, simultaneously toughness reinforcing dose of weather resistance that also affects material of organosilicon; SMA can be good at compatible PC/ASA, has higher impact property.
The foregoing is only preferred embodiment of the present invention, not in order to limit the present invention, all any modifications of doing within the spirit and principles in the present invention, be equal to and replace and improvement etc., within all should being included in protection scope of the present invention.