A kind of copolymerized high temperature resistant nylon and its preparation method and application
A high temperature-resistant and copolymerization technology, applied in the field of high molecular polymers, can solve the problems of weak succinate activity, complex polymerization process, and difficult industrial scale-up, and achieve outstanding photostability, excellent flame retardant performance, and high molecular structure. Effect
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Embodiment 1
[0051] Salt the multifunctional dibasic acid whose R is p-phenylene and decanediamine at a molar ratio of 0.97:1 to obtain component A; and decanediamine and terephthalic acid to form a salt with a molar ratio of 1.03:1 to obtain nylon 10T salt; decanediamine and sebacic acid are salted at a molar ratio of 1.03:1 to obtain nylon 1010 salt. Then put 0.5kg of component A, 7kg of nylon 10T salt and 2.5kg of nylon 1010 salt into the reactor, add 1kg of water and 0.2kg of benzoic acid, replace the air in the reactor with nitrogen for 3 to 4 times, and heat up to 210°C. Keep the pressure in the kettle at 1.5-2.5MPa, continue to heat up to 310°C, keep the pressure in the kettle at 1.5-2.0MPa, keep the pressure for 1.5h, release the gas to normal pressure, drain the water in the system, and then gradually vacuumize the system to reduce the pressure. Press down to -0.03~-0.07MPa, keep it for 4 hours, then fill it with nitrogen to 0.4MPa, discharge the material to obtain copolymerized h...
Embodiment 2
[0054] Salt the multifunctional dibasic acid whose R is p-phenylene with decanediamine at a molar ratio of 0.97:1 to obtain component A; salt with decanedidiamine and terephthalic acid at a molar ratio of 1.03:1 to obtain nylon 10T Salt; Decanediamine and sebacic acid are salted at a molar ratio of 1.03:1 to obtain nylon 1010 salt. Then put 1 kg of component A, 7 kg of nylon 10T salt and 2 kg of nylon 1010 salt into the reactor, add 1 kg of water and 0.2 kg of benzoic acid, replace the air in the reactor with nitrogen for 3 to 4 times, raise the temperature to 210 ° C, and keep the reactor The internal pressure is 1.5-2.5MPa, continue to heat up to 310°C, keep the pressure in the kettle at 1.5-2.0MPa, keep the pressure for 1.5h, release the gas to normal pressure, discharge the water in the system, and then gradually vacuumize the system to decompress to -0.03~-0.07MPa, keep it for 4 hours, then fill it with nitrogen to 0.4MPa, and discharge the material to obtain the copolyme...
Embodiment 3
[0056] The multifunctional dibasic acid whose R is a p-phenyl group is salted with decanediamine at a molar ratio of 0.97:1 to obtain component A; the molar ratio of decanediamine and terephthalic acid is formed into a salt with a molar ratio of 1.03:1 to obtain nylon 10T salt; decanediamine and sebacic acid are salted at a molar ratio of 1.03:1 to obtain nylon 1010 salt. Then put 1.5kg of component A, 7kg of nylon 10T salt and 1.5kg of nylon 1010 salt into the reactor, add 1kg of water and 0.2kg of benzoic acid, replace the air in the reactor with nitrogen for 3 to 4 times, and heat up to 210°C. Keep the pressure in the kettle at 1.5-2.5MPa, continue to heat up to 310°C, keep the pressure in the kettle at 1.5-2.0MPa, keep the pressure for 1.5h, release the gas to normal pressure, drain the water in the system, and then gradually vacuumize the system to reduce the pressure. Press down to -0.03~-0.07MPa, keep it for 4 hours, then fill it with nitrogen to 0.4MPa, discharge the m...
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