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 a kind of polycarbonate composite material of cold and corrosion resistant, comprises following component (in parts by weight):
The melting index (MI) of wherein said polycarbonate (PC) under 300 ℃ and 1.2kg condition be 3-15g/10min, described organosilicon-polycarbonate block copolymer 300 ℃ with the 1.2kg condition under melting index be 1-10g/10min.
Preferably, the melting index MI of the polycarbonate used in the embodiment of the present invention under 300 ℃ and 1.2kg condition is 4-8g/10min.Polycarbonate component under this condition can improve the toughness of gained PC matrix material effectively.
Organosilicon-the polycarbonate block copolymer used in the embodiment of the present invention, claim again polydimethylsiloxane-polycarbonate block copolymer, be by α, ω-dichloro-polydimethylsiloxane and dihydroxyphenyl propane condensation, obtain the polydimethylsiloxane that two ends are the dihydroxyphenyl propane group; And then add the dihydroxyphenyl propane photoreactive gas to carry out copolycondensation, finally obtain organosilicon-polycarbonate block copolymer.Contain polydimethylsiloxane and polycarbonate structure in this copolymer molecule chain, because of the introducing of dimethyl siloxane chain link, reduced softening temperature and the melting viscosity of pure polycarbonate (PC), improved impelling strength and pyrolysis temperature range.Preferably, the melting index MI of the organosilicon-polycarbonate block copolymer used in the embodiment of the present invention under 300 ℃ and 1.2kg condition is 2-6g/10min.
Use organosilicon-polycarbonate block copolymer in the embodiment of the present invention, effectively reduce the internal stress of resin matrix, increase toughness and the erosion resistance of PC matrix material, increase the shock strength of gained PC matrix material and the performance under cold condition simultaneously.
Particularly, the toughner used in the embodiment of the present invention contains organosilicon/vinylformic acid and methyl methacrylate, and wherein organosilicon/vinylformic acid is core, and methyl methacrylate is that hull shape becomes nucleocapsid structure, and wherein silicone content is 10wt%-30wt%.This kind of toughner is the anti-impact modifier of a kind of efficient, low-temperature impact-resistant, weathering resistance; As the S-2001 of the beautiful sun of Mitsubishi, S-2030 etc.
The UV light absorber of using in the embodiment of the present invention is preferably benzotriazole compound or benzophenone, as one or more of UV531 (Octabenzone), UV944, UV5411 (2 (the tertiary octyl phenyl of 2-hydroxyl-5-) benzotriazole).The existence of this UV light absorber component, make gained PC matrix material except having above-mentioned good characteristic, also has weathering resistance, the ageing resistance of enhancing.
The lubricant used in the embodiment of the present invention is: ethene stearylamide or ethylene bis stearamide, as: EBS etc.
The antioxidant component used in the embodiment of the present invention preferably includes main anti-oxidant and auxiliary antioxidant, and wherein the mass ratio of main anti-oxidant and auxiliary antioxidant is preferably 1:1-1:3.Wherein, this main anti-oxidant is preferably β-(3,5-di-tert-butyl-hydroxy phenyl) propionic acid octadecanol ester, and its molecular weight is 530.86g/mol; Auxiliary antioxidant is preferably three (2,4-di-tert-butyl-phenyl) phosphorous acid ester, and molecular weight is 646.9g/mol.By the acting in conjunction of primary antioxidant and auxiliary antioxidant and other components, effectively improve the antioxidant property of this PC matrix material in PC matrix material of the present invention, further strengthened the stability of PC matrix material.
The polycarbonate composite material that the embodiment of the present invention provides also can comprise stablizer, this stablizer is can be Pb stabilizer, as lead sulfate tribasic, dibasic lead stearate, or metal soap stablizer, as Zinic stearas (ZnSt), lead stearate (PbSt) etc., certainly, can use the stablizer of the other types of this area to substitute.The existence of stabilizer component, be conducive to reduce PC composite material surface tension force, prevents the effects such as light, thermolysis or oxygenolysis.
The polycarbonate composite material that the embodiment of the present invention provides also can comprise white mineral oil, and this white mineral oil can be this area white mineral oil commonly used, and this white mineral oil accounts for the 0.6-1wt% of this matrix material gross weight.
White mineral oil plays the powder auxiliary agents such as organosilicon-polycarbonate block copolymer, toughner is bonded on the PC particle, plays good dispersion effect and lubrication, has optimized the process engineering of material.
PC matrix material of the present invention, by adding organosilicon toughner, further effectively reduce the internal stress of resin matrix, increased toughness and the weather resistance of PC matrix material; This PC composite material and preparation method thereof operation is simple, easily control, and cost is low, is applicable to suitability for industrialized production.
The embodiment of the present invention also provides the preparation method of a kind of polycarbonate (PC) matrix material, comprises the following steps:
S01. obtain each component that forms polycarbonate composite material of the present invention, be mixed to get mixture;
S02. utilize twin screw extruder by described mixture extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 200~220 ℃, a district, two 230~250 ℃, 230~240 230~240 ℃, 4th district, ℃, 3rd district, districts, five 230~250 ℃, districts, six 220~240 ℃, 200~220 200~220 ℃, 8th district, ℃, 7th district, districts, 230~260 ℃ of heads, the rotating speed of described double-screw extruder screw is 280~350 rev/mins.Under these processing condition, can make to interact between each component, thereby form the PC matrix material of stable performance.
Exemplarily, above-mentioned matrix material can consist of the following composition:
Particularly, in step S01, above-mentioned each component can fully be mixed in mixing machine, and mixing time is preferably 20~30min, so that each component mixes.
Particularly, in above-mentioned steps S02, above-mentioned twin screw extruder can be this area twin screw extruder commonly used, the twin screw extruder that the model of producing as Nanjing Ke Ya company is CTE-35 (L/D=36).
In the PC composite material and preparation method thereof that the embodiment of the present invention provides, each component is mixed in proportion, through extruding pelletization, processes and can obtain product, this preparation method's technique is simple, easily control, and cost is low, is applicable to suitability for industrialized production.
The embodiment of the present invention also provides a kind of cable junction box of being made by polycarbonate composite material, and described cable junction box is for connecting subterranean cable and submarine optical fiber cable.Simultaneously, the polycarbonate composite material that the embodiment of the present invention provides can be used for military Material Field and the erosion resistance fields such as Material Field for low-temperature cold store, navigation flight, as navigation instrument, military interphone, aircraft communication receiving box etc.
Below by specific embodiment, describe the present invention.
Embodiment 1
1. take following each component by following weight ratio:
Wherein the MI of above-mentioned polycarbonate is 9~12g/10min, the MI of above-mentioned organosilicon-polycarbonate block copolymer is 7~10g/10min, above-mentioned oxidation inhibitor is by β-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid octadecanol ester and three (2, the 4-di-tert-butyl-phenyl) phosphorous acid ester forms with the 1:1 mass ratio, and the total mass of all components is 5Kg.
2. above-mentioned each component is mixed to 30min in mixing machine, obtain mixture;
In twin screw extruder by the mixture extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 210 ℃, a district, two 250 ℃, 240 240 ℃, 4th district, ℃, 3rd district, districts, five 250 ℃, districts, six 230 ℃, 220 210 ℃, 8th district, ℃, 7th district, districts, 250 ℃ of heads, the rotating speed of described double-screw extruder screw is 320 rev/mins.
Embodiment 2
1. take following each component by following weight ratio:
Wherein the MI of above-mentioned polycarbonate is 9~12g/10min, the MI of above-mentioned organosilicon-polycarbonate block copolymer is 2~6g/10min, above-mentioned oxidation inhibitor is by β-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid octadecanol ester and three (2, the 4-di-tert-butyl-phenyl) phosphorous acid ester forms with the 1:2 mass ratio, and the total mass of all components is 5Kg.
2. above-mentioned each component is mixed to 20min in mixing machine, obtain mixture;
In twin screw extruder by the mixture extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 200 ℃, a district, two 240 ℃, 230 240 ℃, 4th district, ℃, 3rd district, districts, five 250 ℃, districts, six 220 ℃, 210 210 ℃, 8th district, ℃, 7th district, districts, 230 ℃ of heads, the rotating speed of described double-screw extruder screw is 340 rev/mins.
Embodiment 3
1. take following each component by following weight ratio:
Wherein the MI of above-mentioned polycarbonate is 4~8g/10min, the MI of above-mentioned organosilicon-polycarbonate block copolymer is 2~6g/10min, the MI of above-mentioned organosilicon-polycarbonate block copolymer is 7~10g/10min, above-mentioned oxidation inhibitor is by β-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid octadecanol ester and three (2, the 4-di-tert-butyl-phenyl) phosphorous acid ester forms with the 1:3 mass ratio, and the total mass of all components is 5Kg.
2. above-mentioned each component is mixed to 25min in mixing machine, obtain mixture;
In twin screw extruder by the mixture extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 210 ℃, a district, two 240 ℃, 230 230 ℃, 4th district, ℃, 3rd district, districts, five 230 ℃, districts, six 230 ℃, 200 210 ℃, 8th district, ℃, 7th district, districts, 250 ℃ of heads, the rotating speed of described double-screw extruder screw is 330 rev/mins.
Embodiment 4
1. take following each component by following weight ratio:
Wherein the MI of above-mentioned polycarbonate is 4~8g/10min, and the MI of above-mentioned organosilicon-polycarbonate block copolymer is 7~10g/10min, and the total mass of all components is 5Kg.
2. above-mentioned each component is mixed to 25min in mixing machine, obtain mixture;
In twin screw extruder by the mixture extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 210 ℃, a district, two 240 ℃, 230 230 ℃, 4th district, ℃, 3rd district, districts, five 230 ℃, districts, six 230 ℃, 200 210 ℃, 8th district, ℃, 7th district, districts, 250 ℃ of heads, the rotating speed of described double-screw extruder screw is 330 rev/mins.
The comparative example 1
1. take following each component by following weight ratio:
Wherein the MI of above-mentioned polycarbonate is 4~8g/10min, and the MI of above-mentioned organosilicon-polycarbonate block copolymer is 2~6g/10min, and the total mass of all components is 5Kg.
2. above-mentioned each component is mixed to 30min in mixing machine, obtain mixture;
In twin screw extruder by the mixture extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 210 ℃, a district, two 250 ℃, 240 240 ℃, 4th district, ℃, 3rd district, districts, five 250 ℃, districts, six 230 ℃, 220 210 ℃, 8th district, ℃, 7th district, districts, 250 ℃ of heads, the rotating speed of described double-screw extruder screw is 320 rev/mins.
The comparative example 2
1. take following each component by following weight ratio:
Wherein the MI of above-mentioned polycarbonate is 4~8g/10min, and the total mass of all components is 5Kg.
2. above-mentioned each component is mixed to 20min in mixing machine, obtain mixture;
In twin screw extruder by the mixture extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 200 ℃, a district, two 240 ℃, 230 240 ℃, 4th district, ℃, 3rd district, districts, five 250 ℃, districts, six 220 ℃, 210 210 ℃, 8th district, ℃, 7th district, districts, 230 ℃ of heads, the rotating speed of described double-screw extruder screw is 340 rev/mins.
The comparative example 3
1. take following each component by following weight ratio:
Wherein the MI of above-mentioned polycarbonate is 4~8g/10min, and the total mass of all components is 5Kg.
2. above-mentioned each component is mixed to 25min in mixing machine, obtain mixture;
In twin screw extruder by the mixture extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 210 ℃, a district, two 240 ℃, 230 230 ℃, 4th district, ℃, 3rd district, districts, five 230 ℃, districts, six 230 ℃, 200 210 ℃, 8th district, ℃, 7th district, districts, 250 ℃ of heads, the rotating speed of described double-screw extruder screw is 330 rev/mins.
The comparative example 4
1. take polycarbonate 5Kg, its MI is 4~8g/10min.
By above-mentioned polycarbonate in twin screw extruder by the mixture extruding pelletization, the spout of wherein said twin screw extruder is respectively to the temperature of each section of die head: 210 ℃, a district, two 240 ℃, 230 230 ℃, 4th district, ℃, 3rd district, districts, five 230 ℃, districts, six 230 ℃, 200 210 ℃, 8th district, ℃, 7th district, districts, 250 ℃ of heads, the rotating speed of described double-screw extruder screw is 330 rev/mins.
Performance test and evaluation:
Particle material prepared by above-described embodiment 1-4 and comparative example 1-4 first in convection oven under the condition of 100-120 ℃ dry 2 hours, then utilize dried particle material injection moulding machine to make the standard testing batten and test.
Wherein, tensile strength is tested by the ASTMD-638 standard.Specimen types is the I type, batten size (mm): (176 ± 2) (length) * (12.6 ± 0.2) (end width) * (3.05 ± 0.2) (thickness), and draw speed is 50mm/min;
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;
The erosion resistance test is to continue to soak respectively 24h in 5% hydrochloric acid, 5% sodium hydroxide, 5% sodium chloride solution, observes whether obvious swelling and corrosion phenomenon are arranged;
The temperature cycling test condition is :-40 ℃~+ 85 ℃, cycle index 10 times, do Impact Test;
Insulation resistance test: after product is sunk in the water that 1.5m is dark and to soak 24h, detect insulation resistance whether>=2 * 10
4M Ω.
Burn-in test (weather-proof test) utilizes Xenon lamp weather resistance test box to carry out, and this proofing box yield of radiation is 1.12kw/ ㎡, and 24h is a cycle, and in each cycle, 8h irradiates, and 16h does not irradiate, and the radiation amount in each cycle is 8.96kwh/ ㎡.Temperature during the proofing box internal radiation is 75 ℃, duration of test runs is 10 cycles (being 240h), the light source adopted be spectral distribution with sunlight relatively more approaching and xenon arc lamp that install infrared filter glass additional, 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(Heatdeflectiontemperature, heat-drawn wire, the impact that reflection silicon copolymerization polycarbonate and toughner are heat-resisting on material and reduction injection temperature), test is used computermatic heat-drawn wire trier to carry out, condition is carried out according to ASTMD648, test condition is 1.8MPa, unannealed, 6.4mm; Other performances are all tested according to ASTM standard batten.
The detected result of above-mentioned test is as shown in table 1 below
Table 1 embodiment and comparative example's (Comparative Examples) material properties test data
By upper table data relatively, we are not difficult to find polycarbonate and the toughness reinforcing dose of effect that can play the increase low temperature impact properties of organosilicon of organosilicon copolymerization, simultaneously, also can increase weather resistance and the corrosion resistance nature of material, but the polycarbonate effect of organosilicon copolymerization is more obvious, plays best effect when both carry out composite use; Can see the organosilyl heat-drawn wire that is conducive to reduce material that adds from the data of HDT, can suitably reduce the temperature of injection moulding, play the effect that improves material flowability.
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.