Preparation method of polyorganosiloxane-polycarbonate and its application

Abstract

The invention relates to the technical field of polymer materials, in particular to a preparation method of polyorganosiloxane-polycarbonate and its application. The preparation method includes the following steps: A: The preparation of polycarbonate terminated by acyl chloride. B: Preparation of polyorganosiloxane-polycarbonate. In the invention, the polyorganosiloxane-polycarbonate has excellent mechanical properties due to the introduction of polydimethylsiloxane terminated by eugenol in the main chain. In particular, the polysiloxane-polycarbonate has high low temperature impact strength, low ductility/brittleness transition temperature and good flame retardancy. In the invention, the polycarbonate modified by the Polyorganosiloxane-polycarbonate has good flexural strength, tensile strength and flame retardancy.

Claims

1. Preparation method of polyorganosiloxane-polycarbonate includes the following steps: A: Preparation of polycarbonate terminated by acyl chloride: A1: Using transesterification method by adding bisphenol A to diphenyl carbonate and under the action of composite catalyst. Low molecular weight polycarbonate is created. The molar ratio of diphenyl carbonate to bisphenol A is 1:1.3-1.6. A2: Before adding an acyl chloride capping agent to the reaction product of step A1, inert gas is used for protection, temperature is controlled at 160-180 C. First, constant temperature for 30-45 min, then, Vacuum extraction is operated, then, Constant temperature for 15-20 min, and then, cooling to 40 C.-60 C., the polycarbonate with end-capped acyl chloride is acquired. B: Preparation of polyorganosiloxane-polycarbonate: B1: Inert gas is used for protection, and then adding polyorganosiloxane to the mixture of diphenyl carbonate and magnesium chloride, transesterification reaction is carried out under the state of stirring and molten condition. The mass ratio of diphenyl carbonate, magnesium chloride and polydimethylsiloxane is 50-70:15-30:1. B2: Adding the acyl chloride-terminated polycarbonate obtained from step A2 wherein said into the reaction product of step B1, then, under the conditions of inert gas protection, stirring and heating to cause the polycondensation reaction to take place. After the reaction is finished, cooling to normal temperature, the crude product of polyorganosilicone-polycarbonate is obtained. B3: The crude product of polycarbonate obtained by step B2 wherein said is dissolved into organic solution, washed by alcohol solvent and filtered, and then the polyorganosiloxane-polycarbonate is obtained after it's dried.

2. According to claim 1 wherein said, the preparation method of polyorganosiloxane-polycarbonate is described, its characteristic includes: in the step A1 wherein said, the non-phosgene synthesis comprises a transesterification phase and a polycondensation stage, and the specific steps in the transesterification phase are as follows: The first step is that the temperature of diphenyl carbonate is rised to 100 C.-120 C. under inert gas protection. The second step is that bisphenol A is added and then the time of keeping temperature is 30-45 min. The third step is that the prepolymer is prepared by heating up to 150 C.-180 C. and the time of keeping temperature is 1-2 H. The specific steps of the condensation phase are as follows: The first step is that the temperature of the prepolymer is rised to 200 C.-220 C. under inert gas protection and then the time of keeping temperature is 45-60 min. The second step is that causing the temperature to rise to 240-270 C. and the time of keeping temperature is 1-2 H. The third step is that the reaction is kept 15-30 min under the condition of vacuum. Low molecular weight polycarbonate is acquired.

3. According to claim 1 wherein said, the preparation method of polyorganosiloxane-polycarbonate is described, its characteristic includes: in the step A1, the additive amount of the composite catalyst said is 0.4%-3% of the mass of the bisphenol A. The composite catalyst said is composed of catalyst A and catalyst B, the molar ratio of A:B is 1:0.8-1.5. The catalyst A said is one or more of the tetraphenyl phosphonium benzene oxide, tetraphenyl phosphonium acetate and phenol tetraphenyl phosphonium salts. The catalyst B said is one or more of t-butyllithium, t-butylpotassium, cesium tert-butyl, tert-butyl, n-butyllithium, n-butyl, n-butyl, and n-butylcaesium.

4. According to claim 1 wherein said, the preparation method of polyorganosiloxane-polycarbonate is described, its characteristic includes: The molar ratio of total diphenyl carbonate in steps A1 and B1 wherein said to bisphenol A in step A1 is 1:1.1-1.2. In the step A2 wherein said, the molar ratio of acyl chloride capping agent to bisphenol A is 5-10:1.

5. According to claim 1 wherein said, the preparation method of polyorganosiloxane-polycarbonate is described, its characteristic includes: In the step A2 wherein said, the acyl chloride capping agent said is vinyl benzenesulfonyl chloride and/or methyl propionyl chloride. In the step B1 wherein said, the polysiloxane said is a polydimethylsiloxane terminated by eugenol. The weight-average molecular weight of the polysiloxane said is 2500-3200, and the polydispersity index is less than 3.5.

6. According to claim 1 wherein said, the preparation method of polyorganosiloxane-Polycarbonate is described, its characteristic includes In the step B1 wherein said, the reaction temperature is 100 C.-120 C., at the end of the reaction, the product is cooled to 40 C.-60 C. In the step B2, the reaction temperature is 120 C.-150 C., and the time of keeping temperature is 45-60 min, and then vacuum extraction is operated, and then the time of keeping temperature is 15-20 min, the last the polyorganosiloxane-polycarbonate crude product is acquired by cooling down to normal atmospheric temperature.

7. According to claim 1 wherein said, the preparation method of polyorganosiloxane-polycarbonate is described, its characteristic includes: In the step B3 wherein said, organic solvents are one or more of dichloromethane, trichloromethane, dichloroethane, trichloroethane, tetrachloroethane, toluene, and chlorobenzene. Alcohol solvents are one or more of methanol, ethyl alcohol, propanol and butanol.

8. According to claim 1 wherein said, the preparation method of polyorganosiloxane-polycarbonate is described, its characteristic includes: In the step B3 wherein said, the weight-average molecular weight of the Polyorganosiloxane-polycarbonate is 40000-60000, and the polydispersity index is 1.5-2.2. The weight percentage of the polycarbonate block said is 70%-85%, and the polysiloxane block said is 15%-30%.

9. The characterized of modified polycarbonate includes raw materials weights as follow: Polycarbonate: 100 PHR Polyorganosiloxane-polycarbonate: 20-40 PHR Hyperbranched polymer: 1-5 PHR Halogen-free flame retardant: 0.1-0.6 PHR Toughening agent: 0.5-4 PHR Anti-drop agent: 0.3-0.5 PHR Antioxidant: 0.16-0.3 PHR Light stabilizer: 0.2-0.4 PHR Dispersant: 0.4-0.5 PHR The polyorganosiloxane-polycarbonate said is prepared by means of the preparation method described in claim 1.

10. Preparation method of modified polycarbonate is described in claim 9 wherein said, its characteristic includes the following steps: (1) The polycarbonate and polyorganosiloxane-polycarbonate are dried at 100 C.-120 C. for 2-4 h. (2) Hyperbranched polymers, flame retardants and partially polysiloxane-polycarbonate are mixed homogeneously, the mixing speed is 1000-1200 r/min, and the mixing time is 5-8 min, the flame retardant plastic masterbatch is prepared by extrusion granulation. (3) The Homogeneous mixture contains the flame retardant masterbatch prepared in step (2), polycarbonate, antioxidant and the remaining polyorganosiloxane-polycarbonate and extruded to form plastic masterbatch. (4) The toughening agent, anti-dropping agent, light stabilizer and dispersant are predispersed to obtain the pre-dispersed mixture. (5) The product of step (3) is added to the pre-dispersed mixture of the step (4) wherein said, and the mixture is evenly mixed. Modified polycarbonate is acquired by extrusion granulation. Wherein, the step (2), the step (3) and the step (5) wherein said are all extruded by a twin screw extruder. In the step (2) wherein said, the temperature of each area of twin screw extruder is: the first area: 210-230 C., the second area: 250-260 C., the third area: 270-280 C., the fourth area: 270-280 C., the fifth area: 270-280 C., the sixth area: 270-280 C., the seventh area: 250-260 C., the eighth area: 250-260 C., the ninth area: 270-280 C., extruder head temperature: 270-280 C. In the step (3) wherein said, the temperature of each area of twin screw extruder is: the first area: 180-200 C., the second area: 210-230 C., the third area: 220-240 C., the fourth area: 220-240 C., the fifth area: 220-240 C., the sixth area: 220-240 C., the seventh area: 210-230 C., the eighth area: 210-230 C., the ninth area: 220-240 C., extruder head temperature: 160-180 C. In the step (5) wherein said, the temperature of each area of twin screw extruder is: the first area: 180-200 C., the second area: 210-230 C., the third area: 220-240 C., the fourth area: 220-240 C., the fifth area: 220-240 C., the sixth area: 220-240 C., the seventh area: 210-230 C., the eighth area: 210-230 C., the ninth area: 220-240 C., extruder head temperature: 160-180 C., The rotating speed of twin screw extruder is 350-400 r/min, the feed quantity is 170-180 kg/h, the vacuum degree is 600 mm Hg, and the temperature of water cooling is 40-65 C.

Description

DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0061] In order to facilitate the understanding of the technical personnel in the field, the present invention is further explained in the light of embodiments below, and the contents referred to in the embodiment are not limited to the present invention.

The Implementation Example 1

[0062] Preparation method of polyorganosiloxane-polycarbonate includes the following steps:

[0063] A: Preparation of polycarbonate terminated by acyl chloride:

[0064] A1: Using transesterification method by adding bisphenol A to diphenyl carbonate and under the action of composite catalyst. Low molecular weight polycarbonate is created. The molar ratio of diphenyl carbonate to bisphenol A is 1:1.3.

[0065] A2: Before adding an acyl chloride capping agent to the reaction product of step A1, inert gas is used for protection, temperature is controlled at 160 C. First, constant temperature for 45 min, then, Vacuum extraction is operated, then, Constant temperature for 20 min, and then, cooling to 40 C., the polycarbonate with end-capped acyl chloride is acquired.

[0066] B: Preparation of polyorganosiloxane-polycarbonate:

[0067] B1: Inert gas is used for protection, and then adding polyorganosiloxane to the mixture of diphenyl carbonate and magnesium chloride, transesterification reaction is carried out under the state of stirring and molten condition. The mass ratio of diphenyl carbonate, magnesium chloride and polydimethylsiloxane is 50:15:1.

[0068] B2: Adding the acyl chloride-terminated polycarbonate obtained from step A2 wherein said into the reaction product of step B1, then, under the conditions of inert gas protection, stirring and heating to cause the polycondensation reaction to take place. After the reaction is finished, cooling to normal temperature, the crude product of polyorganosilicone-polycarbonate is obtained.

[0069] B3: The crude product of polycarbonate obtained by step B2 wherein said is dissolved into organic solution, washed by alcohol solvent and filtered, and then the polyorganosiloxane-polycarbonate is obtained after it's dried.

[0070] In the step A1 wherein said, the non-phosgene synthesis comprises a transesterification phase and a polycondensation stage, and the specific steps in the transesterification phase are as follows: The first step is that the temperature of diphenyl carbonate is rised to 100 C. under inert gas protection. The second step is that bisphenol A is added and then the time of keeping temperature is 45 min. The third step is that the prepolymer is prepared by heating up to 150 C. and the time of keeping temperature is 2 H. The specific steps of the condensation phase are as follows: The first step is that the temperature of the prepolymer is rised to 200 C. under inert gas protection and then the time of keeping temperature is 60 min. The second step is that causing the temperature to rise to 240 C. and the time of keeping temperature is 2 H. The third step is that the reaction is kept 30 min under the condition of vacuum. Low molecular weight polycarbonate is acquired.

[0071] In the step A1, the additive amount of the composite catalyst said is 0.4% of the mass of the bisphenol A. The composite catalyst said is composed of catalyst A and catalyst B, the molar ratio of A:B is 1:0.8. The catalyst A said is tetraphenyl phosphonium benzene oxide and tetraphenyl phosphonium acetate, the mass ratio of them is 1:0.8. The catalyst B said is t-butyllithium.

[0072] The molar ratio of total diphenyl carbonate in steps A1 and B1 wherein said to bisphenol A in step A1 is 1:1.1. In the step A2 wherein said, the molar ratio of acyl chloride capping agent to bisphenol A is 5:1.

[0073] In the step A2 wherein said, the acyl chloride capping agent said is vinyl benzenesulfonyl chloride. In the step B1 wherein said, the polysiloxane said is a polydimethylsiloxane terminated by eugenol. The weight-average molecular weight of the polysiloxane said is 2500, and the polydispersity index is 3.5.

[0074] In the step B1 wherein said, the reaction temperature is 100 C., at the end of the reaction, the product is cooled to 40 C. In the step B2, the reaction temperature is 120 C., and the time of keeping temperature is 60 min, and then vacuum extraction is operated, and then the time of keeping temperature is 20 min, the last the polyorganosiloxane-polycarbonate crude product is acquired by cooling down to normal atmospheric temperature.

[0075] In the step B3 wherein said, organic solvents is dichloromethane. Alcohol solvents is methanol.

[0076] In the step B3 wherein said, the weight-average molecular weight of the polyorganosiloxane-polycarbonate is 40000, and the polydispersity index is 1.5. The weight percentage of the polycarbonate block said is 70%, and the polysiloxane block said is 30%.

The Implementation Example 2

[0077] Preparation method of polyorganosiloxane-polycarbonate includes the following steps:

[0078] A: Preparation of polycarbonate terminated by acyl chloride:

[0079] A1: Using transesterification method by adding bisphenol A to diphenyl carbonate and under the action of composite catalyst. Low molecular weight polycarbonate is created. The molar ratio of diphenyl carbonate to bisphenol A is 1:1.6.

[0080] A2: Before adding an acyl chloride capping agent to the reaction product of step A1, inert gas is used for protection, temperature is controlled at 180 C. First, constant temperature for 30 min, then, Vacuum extraction is operated, then, Constant temperature for 15 min, and then, cooling to 60 C., the polycarbonate with end-capped acyl chloride is acquired.

[0081] B: Preparation of polyorganosiloxane-polycarbonate:

[0082] B1: Inert gas is used for protection, and then adding polyorganosiloxane to the mixture of diphenyl carbonate and magnesium chloride, transesterification reaction is carried out under the state of stirring and molten condition. The mass ratio of diphenyl carbonate, magnesium chloride and polydimethylsiloxane is 70:30:1.

[0083] B2: Adding the acyl chloride-terminated polycarbonate obtained from step A2 wherein said into the reaction product of step B1, then, under the conditions of inert gas protection, stirring and heating to cause the polycondensation reaction to take place. After the reaction is finished, cooling to normal temperature, the crude product of polyorganosilicone-polycarbonate is obtained.

[0084] B3: The crude product of polycarbonate obtained by step B2 wherein said is dissolved into organic solution, washed by alcohol solvent and filtered, and then the polyorganosiloxane-polycarbonate is obtained after it's dried.

[0085] In the step A1 wherein said, the non-phosgene synthesis comprises a transesterification phase and a polycondensation stage, and the specific steps in the transesterification phase are as follows: The first step is that the temperature of diphenyl carbonate is rised to 120 C. under inert gas protection. The second step is that bisphenol A is added and then the time of keeping temperature is 30 min. The third step is that the prepolymer is prepared by heating up to 180 C. and the time of keeping temperature is 1 H. The specific steps of the condensation phase are as follows: The first step is that the temperature of the prepolymer is rised to 220 C. under inert gas protection and then the time of keeping temperature is 45 min. The second step is that causing the temperature to rise to 270 C. and the time of keeping temperature is 1 H. The third step is that the reaction is kept 15 min under the condition of vacuum. Low molecular weight polycarbonate is acquired.

[0086] In the step A1 wherein said, the additive amount of the composite catalyst said is 3% of the mass of the bisphenol A. The composite catalyst said is composed of catalyst A and catalyst B, the molar ratio of A:B is 1:1.5. The catalyst A said is phenol tetraphenyl phosphonium salts. The catalyst B said is n-butyllithium.

[0087] The molar ratio of total diphenyl carbonate in steps A1 and B1 wherein said to bisphenol A in step A1 is 1:1.2. In the step A2 wherein said, the molar ratio of acyl chloride capping agent to bisphenol A is 10:1. Preferably, n the step A2 wherein said, the acyl chloride capping agent said is vinyl benzenesulfonyl chloride or methyl propionyl chloride. In the step B1 wherein said, the polysiloxane said is a polydimethylsiloxane terminated by eugenol. The weight-average molecular weight of the polysiloxane said is 3200, and the polydispersity index is 1.5.

[0088] In the step B1 wherein said, the reaction temperature is 120 C., at the end of the reaction, the product is cooled to 60 C. In the step B2, the reaction temperature is 150 C., and the time of keeping temperature is 45 min, and then vacuum extraction is operated, and then the time of keeping temperature is 15 min, the last the polyorganosiloxane-polycarbonate crude product is acquired by cooling down to normal atmospheric temperature.

[0089] In the step B3 wherein said, organic solvents is chloroform. Alcohol solvents is alcohol.

[0090] In the step B3 wherein said, the weight-average molecular weight of the Polyorganosiloxane-polycarbonate is 50000, and the polydispersity index is 2.2. The weight percentage of the polycarbonate block said is 85%, and the polysiloxane block said is 15%.

The Implementation Example 3

[0091] Preparation method of polyorganosiloxane-polycarbonate includes the following steps:

[0092] A: Preparation of polycarbonate terminated by acyl chloride:

[0093] A1: Using transesterification method by adding bisphenol A to diphenyl carbonate and under the action of composite catalyst. Low molecular weight polycarbonate is created. The molar ratio of diphenyl carbonate to bisphenol A is 1:1.5.

[0094] A2: Before adding an acyl chloride capping agent to the reaction product of step A1, inert gas is used for protection, temperature is controlled at 170 C. First, constant temperature for 40 min, then, vacuum extraction is operated, then, Constant temperature for 18 min, and then, cooling to 50 C., the polycarbonate with end-capped acyl chloride is acquired.

[0095] B: Preparation of polyorganosiloxane-polycarbonate:

[0096] B1: Inert gas is used for protection, and then adding polyorganosiloxane to the mixture of diphenyl carbonate and magnesium chloride, transesterification reaction is carried out under the state of stirring and molten condition. The mass ratio of diphenyl carbonate, magnesium chloride and polydimethylsiloxane is 60:25:1.

[0097] B2: Adding the acyl chloride-terminated polycarbonate obtained from step A2 wherein said into the reaction product of step B1, then, under the conditions of inert gas protection, stirring and heating to cause the polycondensation reaction to take place. After the reaction is finished, cooling to normal temperature, the crude product of polyorganosilicone-polycarbonate is obtained.

[0098] B3: The crude product of polycarbonate obtained by step B2 wherein said is dissolved into organic solution, washed by alcohol solvent and filtered, and then the polyorganosiloxane-polycarbonate is obtained after it's dried.

[0099] In the step A1 wherein said, the non-phosgene synthesis comprises a transesterification phase and a polycondensation stage, and the specific steps in the transesterification phase are as follows: The first step is that the temperature of diphenyl carbonate is rised to 110 C. under inert gas protection. The second step is that bisphenol A is added and then the time of keeping temperature is 35 min. The third step is that the prepolymer is prepared by heating up to 165 C. and the time of keeping temperature is 1-2 H. The specific steps of the condensation phase are as follows: The first step is that the temperature of the prepolymer is rised to 210 C. under inert gas protection and then the time of keeping temperature is 50 min. The second step is that causing the temperature to rise to 260 C. and the time of keeping temperature is 1.5 H. The third step is that the reaction is kept 20 min under the condition of vacuum. Low molecular weight polycarbonate is acquired.

[0100] In the step A1 wherein said, the additive amount of the composite catalyst said is 2% of the mass of the bisphenol A. The composite catalyst said is composed of catalyst A and catalyst B, the molar ratio of A:B is 1:1.2. The catalyst A said is tetraphenyl phosphonium benzene oxide and phenol tetraphenyl phosphonium salts, the mass ratio of them is 1:2. The catalyst B said is t-butyllithium and n-butyllithium, the mass ratio of them is 1:2-3.

[0101] The molar ratio of total diphenyl carbonate in steps A1 and B1 wherein said to bisphenol A in step A1 is 1:1.1. In the step A2 wherein said, the molar ratio of acyl chloride capping agent to bisphenol A is 8:1.

[0102] In the step A2 wherein said, the acyl chloride capping agent said is vinyl benzenesulfonyl chloride or methyl propionyl chloride. In the step B1 wherein said, the polysiloxane said is a polydimethylsiloxane terminated by eugenol. The weight-average molecular weight of the polysiloxane said is 3000, and the polydispersity index is 2.

[0103] In the step B1 wherein said, the reaction temperature is 110 C., at the end of the reaction, the product is cooled to 50 C. In the step B2, the reaction temperature is 135 C., and the time of keeping temperature is 50 min, and then vacuum extraction is operated, and then the time of keeping temperature is 18 min, the last the polyorganosiloxane-polycarbonate crude product is acquired by cooling down to normal atmospheric temperature.

[0104] In the step B3 wherein said, organic solvents is dichloromethane, chloroform and dichloroethane, mixed according to the volume ratio of 2-3:1:1. Alcohol solvents is methanol and alcohol, mixed according to the volume ratio of 2:1.

[0105] In the step B3 wherein said, the weight-average molecular weight of the Polyorganosiloxane-polycarbonate is 60000, and the polydispersity index is 1.5. The weight percentage of the polycarbonate block said is 80%, and the polysiloxane block said is 20%.

The Implementation Example 4

[0106] A modified polycarbonate includes raw materials weights as follow: [0107] Polycarbonate: 100 PHR [0108] Polyorganosiloxane-polycarbonate: 20 PHR [0109] Hyperbranched polymer: 1 PHR [0110] Halogen-free flame retardant: 0.1 PHR [0111] Toughening agent: 0.5 PHR [0112] Anti-drop agent: 0.3 PHR [0113] Antioxidant: 0.16 PHR [0114] Light stabilizer: 0.2 PHR [0115] Dispersant: 0.4 PHR

[0116] The polyorganosiloxane-polycarbonate said is prepared in the implementation example 1.

[0117] Preparation method of modified polycarbonate is described wherein said, the following steps is included: [0118] (1) The polycarbonate and polyorganosiloxane-polycarbonate are dried at 100 C. for 4 h. [0119] (2) Hyperbranched polymers, flame retardants and partially polysiloxane-polycarbonate are mixed homogeneously, the mixing speed is 1000 r/min, and the mixing time is 8 min, the flame retardant plastic masterbatch is prepared by extrusion granulation. [0120] (3) The Homogeneous mixture contains the flame retardant masterbatch prepared in step (2), polycarbonate, antioxidant and the remaining polyorganosiloxane-polycarbonate and extruded to form plastic masterbatch. [0121] (4) The toughening agent, anti-dropping agent, light stabilizer and dispersant are predispersed to obtain the pre-dispersed mixture. [0122] (5) The product of step (3) is added to the pre-dispersed mixture of the step (4) wherein said, and the mixture is evenly mixed. Modified polycarbonate is acquired by extrusion granulation.

[0123] Wherein, the step (2), the step (3) and the step (5) wherein said are all extruded by a twin screw extruder.

[0124] In the step (2) wherein said, the temperature of each area of twin screw extruder is: the first area: 210 C., the second area: 250 C., the third area: 270 C., the fourth area: 270 C., the fifth area: 270 C., the sixth area: 270 C., the seventh area: 250 C., the eighth area: 250 C., the ninth area: 270 C., extruder head temperature: 270 C.

[0125] In the step (3) wherein said, the temperature of each area of twin screw extruder is: the first area: 180 C., the second area: 210 C., the third area: 220 C., the fourth area: 220 C., the fifth area: 220 C., the sixth area: 220 C., the seventh area: 210 C., the eighth area: 210 C., the ninth area: 220 C., extruder head temperature: 160 C.

[0126] In the step (5) wherein said, the temperature of each area of twin screw extruder is: the first area: 180 C., the second area: 210 C., the third area: 220 C., the fourth area: 220 C., the fifth area: 220 C., the sixth area: 220 C., the seventh area: 210 C., the eighth area: 210 C., the ninth area: 220 C., extruder head temperature: 160 C., The rotating speed of twin screw extruder is 350 r/min, the feed quantity is 170 kg/h, the vacuum degree is 600 mm Hg, and the temperature of water cooling is 40 C.

The Implementation Example 5

[0127] A modified polycarbonate includes raw materials weights as follow: [0128] Polycarbonate: 100 PHR [0129] Polyorganosiloxane-polycarbonate: 40 PHR [0130] Hyperbranched polymer: 5 PHR [0131] Halogen-free flame retardant: 0.6 PHR [0132] Toughening agent: 4 PHR [0133] Anti-drop agent: 0.5 PHR [0134] Antioxidant: 0.3 PHR [0135] Light stabilizer: 0.4 PHR [0136] Dispersant: 0.5 PHR

[0137] The polyorganosiloxane-polycarbonate said is prepared in the implementation example 2.

[0138] Preparation method of modified polycarbonate is described wherein said, the following steps is included: [0139] (1) The polycarbonate and polyorganosiloxane-polycarbonate are dried at 120 C. for 2 h. [0140] (2) Hyperbranched polymers, flame retardants and partially polysiloxane-polycarbonate are mixed homogeneously, the mixing speed is 1200 r/min, and the mixing time is 5 min, the flame retardant plastic masterbatch is prepared by extrusion granulation. [0141] (3) The Homogeneous mixture contains the flame retardant masterbatch prepared in step (2), polycarbonate, antioxidant and the remaining polyorganosiloxane-polycarbonate and extruded to form plastic masterbatch. [0142] (4) The toughening agent, anti-dropping agent, light stabilizer and dispersant are predispersed to obtain the pre-dispersed mixture. [0143] (5) The product of step (3) is added to the pre-dispersed mixture of the step (4) wherein said, and the mixture is evenly mixed. Modified polycarbonate is acquired by extrusion granulation.

[0144] Wherein, the step (2), the step (3) and the step (5) wherein said are all extruded by a twin screw extruder.

[0145] In the step (2) wherein said, the temperature of each area of twin screw extruder is: the first area: 230 C., the second area: 260 C., the third area: 280 C., the fourth area: 280 C., the fifth area: 280 C., the sixth area: 280 C., the seventh area: 260 C., the eighth area: 260 C., the ninth area: 280 C., extruder head temperature: 280 C.

[0146] In the step (3) wherein said, the temperature of each area of twin screw extruder is: the first area: 200 C., the second area: 230 C., the third area: 240 C., the fourth area: 240 C., the fifth area: 240 C., the sixth area: 240 C., the seventh area: 230 C., the eighth area: 230 C., the ninth area: 240 C., extruder head temperature: 180 C.

[0147] In the step (5) wherein said, the temperature of each area of twin screw extruder is: the first area: 200 C., the second area: 230 C., the third area: 240 C., the fourth area: 240 C., the fifth area: 240 C., the sixth area: 240 C., the seventh area: 230 C., the eighth area: 230 C., the ninth area: 240 C., extruder head temperature: 180 C., The rotating speed of twin screw extruder is 400 r/min, the feed quantity is 180 kg/h, the vacuum degree is 600 mm Hg, and the temperature of water cooling is 65 C.

The Implementation Example 6

[0148] A modified polycarbonate includes raw materials weights as follow: [0149] Polycarbonate: 100 PHR [0150] Polyorganosiloxane-polycarbonate: 30 PHR [0151] Hyperbranched polymer: 3 PHR [0152] Halogen-free flame retardant: 0.3 PHR [0153] Toughening agent: 2 PHR [0154] Anti-drop agent: 0.4 PHR [0155] Antioxidant: 0.22 PHR [0156] Light stabilizer: 0.3 PHR [0157] Dispersant: 0.45 PHR

[0158] The polyorganosiloxane-polycarbonate said is prepared in the implementation example 3.

[0159] Preparation method of modified polycarbonate is described wherein said, the following steps is included: [0160] (1) The polycarbonate and polyorganosiloxane-polycarbonate are dried at 110 C. for 3 h. [0161] (2) Hyperbranched polymers, flame retardants and partially polysiloxane-polycarbonate are mixed homogeneously, the mixing speed is 1100 r/min, and the mixing time is 6 min, the flame retardant plastic masterbatch is prepared by extrusion granulation. [0162] (3) The Homogeneous mixture contains the flame retardant masterbatch prepared in step (2), polycarbonate, antioxidant and the remaining polyorganosiloxane-polycarbonate and extruded to form plastic masterbatch. [0163] (4) The toughening agent, anti-dropping agent, light stabilizer and dispersant are predispersed to obtain the pre-dispersed mixture. [0164] (5) The product of step (3) is added to the pre-dispersed mixture of the step (4) wherein said, and the mixture is evenly mixed. Modified polycarbonate is acquired by extrusion granulation.

[0165] Wherein, the step (2), the step (3) and the step (5) wherein said are all extruded by a twin screw extruder.

[0166] In the step (2) wherein said, the temperature of each area of twin screw extruder is: the first area: 220 C., the second area: 255 C., the third area: 275 C., the fourth area: 275 C., the fifth area: 275 C., the sixth area: 275 C., the seventh area: 255 C., the eighth area: 255 C., the ninth area: 275 C., extruder head temperature: 275 C.

[0167] In the step (3) wherein said, the temperature of each area of twin screw extruder is: the first area: 190 C., the second area: 220 C., the third area: 230 C., the fourth area: 230 C., the fifth area: 230 C., the sixth area: 230 C., the seventh area: 220 C., the eighth area: 220 C., the ninth area: 230 C., extruder head temperature: 170 C.

[0168] In the step (5) wherein said, the temperature of each area of twin screw extruder is: the first area: 190 C., the second area: 220 C., the third area: 230 C., the fourth area: 230 C., the fifth area: 230 C., the sixth area: 230 C., the seventh area: 220 C., the eighth area: 220 C., the ninth area: 230 C., extruder head temperature: 170 C., The rotating speed of twin screw extruder is 380 r/min, the feed quantity is 175 kg/h, the vacuum degree is 600 mm Hg, and the temperature of water cooling is 50 C.

Contrast Example

[0169] A modified polycarbonate includes raw materials weights as follow: [0170] Polycarbonate: 100 PHR [0171] Hyperbranched polymer: 3 PHR [0172] Halogen-free flame retardant: 2 PHR [0173] Toughening agent: 1 PHR [0174] Anti-drop agent: 0.4 PHR [0175] Antioxidant: 0.22 PHR [0176] Light stabilizer: 0.3 PHR [0177] Dispersant: 0.45 PHR

[0178] The test properties of modified polycarbonate about the implementation example 4-6 and contrast example 1 are as follows:

TABLE-US-00001 Imple- Imple- Imple- mentation mentation mentation Contrast Example Example Example Example ITEMS 4 5 6 1 Bending Strength (MPa) 88 89 90 85 Tensile Strength(MPa) 60 61 63 55 Notched Impact Strength 71 71 70 57 of Cantilever Beam at Room Temp.(KJ/M2) Notched Impact Strength 56 57 61 39 Cantilever Beam At Low Temp.(40 C.) (KJ/M2) UL94 Flame Retardant V0 V0 V0 HB Grade (2.0 mm) UL94 Flame Retardant V1 V1 V1 HB Grade (1.6 mm) Electric Indentation 2 2 2 3 Index(CTI) Long-term Thermal 70 70 70 30 Aging Test Performance Retention Rate (%) Weathering Test f1 f1 f1 /
From the table above, we can see, polycarbonate modified by polyorganosiloxane-polycarbonate was prepared by the invention. The physical properties of modified polycarbonate are obviously better than contrast example 1, for example, flexural strength, tensile strength, notched impact strength of cantilever beam at room temperature, notched impact strength of cantilever beam at low temperature, inflaming retarding, CTI, ageing resistance and weather fastness and so on. Polycarbonate modified by polyorganosiloxane-polycarbonate in the present invention has good flexural strength, tensile strength and flame retardant property up to UL94 V0 (0.8 mm).

[0179] The implementation example are better implementation schemes of the invention. In addition, the invention can also be realized in other ways. Any obvious replacement is within the protection scope of the invention without being separated from the conception of the invention.