Method for manufacturing polycarbonate resin, polycarbonate resin, polycarbonate-resin film, and methods for manufacturing polycarbonate-resin pellets and polycarbonate-resin films
A technology of polycarbonate resin and manufacturing method, which is applied in the field of polycarbonate resin, and can solve the problems of resin deterioration and high melt viscosity
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0417] In the raw material preparation tank fully subjected to nitrogen substitution (oxygen concentration 0.0005% to 0.001% by volume), a certain amount of raw material is continuously supplied to the first polymerization reactor, and at the same time, it is continuously fed through the catalyst supply pipe connected to the raw material supply pipe. Supply the magnesium acetate tetrahydrate that has been made into the aqueous solution so that it reaches 19×10 per 1 mol of all dihydroxy compounds. -6 mol (converted into magnesium metal atoms), the raw material is prepared in such a way that the molar ratio of BHEPF / ISB / PEG (average molecular weight 1000) / DPC is 43.2 / 55.6 / 1.2 / 99, and the first polymerization reactor has : Heat medium jacket with oil as heat medium, heat medium internal coil, stirring paddle, distillation tube connected with vacuum pump, and condenser.
[0418] After the raw material and the aqueous catalyst solution are mixed in the piping, two pleated cylindri...
Embodiment 2
[0433]The raw material is prepared in such a way that the molar ratio of BHEPF / ISB / PEG (average molecular weight is 1000) / DPC is 40.3 / 59.4 / 0.3 / 99, the inner temperature of the first polymerization reactor is 194°C, the pressure is 27.8kPa, and the second The internal temperature of the dipolymerization reactor is 208°C and the pressure is 25.8kPa, so that the internal temperature of the third polymerization reactor is 221°C and the pressure is 23.0kPa, so that the internal temperature near the entrance of the fourth polymerization reactor is 225°C and the outlet The nearby internal temperature is 239°C and the pressure is 1.3kPa, and the screw speed of the extruder, the polycarbonate resin extrusion amount / the cross-sectional area of the extruder barrel, the heater setting temperature of the filter, and the filter surface Except that the linear velocity of the molten resin above was changed as shown in Table 1, it was carried out in the same manner as in Example 1. The analy...
Embodiment 3
[0435] For the setting of the heater temperature of the barrel of the extruder, set the 4 upstream components to 240°C, set the 6 downstream components to 220°C, set the screw speed of the extruder, the heater of the filter Except having changed the preset temperature and the heater preset temperature of a die|dye as shown in Table 1, it carried out similarly to Example 2. The analytical values are shown in Table 1.
PUM
Property | Measurement | Unit |
---|---|---|
glass transition temperature | aaaaa | aaaaa |
thickness | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com