Polycarbonate resin composition
A technology of polycarbonate resin and resin composition, applied in the field of resin composition containing polycarbonate resin, capable of solving problems such as insufficient heat resistance
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[0167] The following examples are given to further illustrate the present invention. However, the present invention is not limited to these Examples. Wherein, the parts in the examples are parts by weight, and % is % by weight. In addition, the following methods were used for evaluation.
[0168] (1) specific viscosity (η SP )
[0169] The pellets were dissolved in methylene chloride to a concentration of 0.7 g / dL, and measured using an Ostwald viscometer (device name: RIGO AUTO VISCOSIMETER TYPE VMR-0525·PC) at a temperature of 20°C. Among them, specific viscosity η SP It can be calculated|required from the following formula.
[0170] n sp =t / t o -1
[0171] t: flow time of the sample solution
[0172] t o : only the flow time of the solvent
[0173] (2) Content rate of biological origin substances
[0174] According to ASTM D686605, the biogenic substance content rate was measured by the biogenic substance content rate test using the radiocarbon concentration (pe...
reference example 1
[0200] Reference example 1 (production of polycarbonate resin)
[0201] 7307 parts by weight of isosorbide (50 moles) and 10709 parts by weight of diphenyl carbonate (50 moles) are put into the reactor, and 4.8 parts by weight of tetramethylammonium hydroxide are put into (with respect to 1 mole of diphenyl carbonate The composition is 1×10 -4 mol) and sodium hydroxide 5.0×10 -3 Parts by weight (relative to 1 mole of diphenyl carbonate component is 0.25 × 10 -6 mol) as a polymerization catalyst was heated to 180° C. under normal pressure in a nitrogen atmosphere to melt.
[0202] Slowly reduce the pressure in the reaction tank under stirring for 30 minutes, and distill off the generated phenol while reducing the pressure to 13.3×10 -3 MPa. After allowing it to react for 20 minutes in this state, the temperature was raised to 200° C., and then the pressure was reduced slowly over 20 minutes, while the phenol was distilled off, and at 4.00×10 -3 MPa was allowed to react for...
reference example 2
[0204] Reference example 2 (production of polycarbonate resin)
[0205] 7307 parts by weight of isosorbide (50 moles), 10923 parts by weight of diphenyl carbonate (51 moles) and 270 parts by weight of stearyl alcohol (1.0 moles) are put into the reactor, and tetramethylammonium hydroxide 4.7 Parts by weight (relative to 1 mole of diphenyl carbonate component is 1×10 -4 mol) and sodium hydroxide 4.0×10 -3 Parts by weight (relative to 1 mole of diphenyl carbonate component is 0.20×10 -6 mol) as a polymerization catalyst was heated to 180° C. under normal pressure in a nitrogen atmosphere to melt.
[0206] Slowly reduce the pressure in the reaction tank under stirring for 30 minutes, and distill off the generated phenol while reducing the pressure to 13.3×10 -3 MPa. After allowing it to react for 20 minutes in this state, the temperature was raised to 200° C., and then the pressure was reduced slowly over 20 minutes, while the phenol was distilled off, and at 4.00×10 -3 MPa ...
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