Preparation method of in-situ polymerized type halogen-free flame retardant nylon material for selective laser sintering
A flame retardant nylon and laser sintering technology, applied in the field of additive manufacturing, can solve problems such as inability to form and process, poor flame retardant effect, and difficulty in preparing workpieces, and achieve the effects of reducing impact, saving reaction time, and protecting the environment
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[0022] The invention provides a method for preparing an in-situ polymerization type halogen-free flame-retardant nylon material for selective laser sintering, comprising the following steps:
[0023] In-situ polymerization of nylon monomer, melamine, cyanuric acid, light absorber, molecular weight regulator, and primary antioxidant to obtain a halogen-free flame-retardant nylon material;
[0024] The halogen-free flame-retardant nylon material obtained above is pulverized to obtain halogen-free flame-retardant nylon powder for selective laser sintering.
[0025] In order to make the halogen-free flame-retardant nylon powder obtained above be better applied to selective laser sintering, that is, it has better light absorption effect and flame-retardant effect, and the mechanical properties of sintered parts are better. Preferably, the above-mentioned nylon Monomer, melamine, cyanuric acid, light absorber, molecular weight regulator, and first antioxidant are also added with wat...
Embodiment 1
[0033] (1) Add the raw materials caprolactam, melamine, cyanuric acid, benzoxazine, molecular weight regulator, antioxidant and deionized water into the reaction kettle. Wherein each component and its percentage by weight are as follows: the content of caprolactam is 88%, the content of melamine is 5%, the content of cyanuric acid is 5%, the content of benzoxazine is 0.1%, and the content of molecular weight regulator is 0.3%. The antioxidant content is 1%, and the deionized water content accounts for 20% of the total mass of the above raw materials; the reaction kettle is sealed and the gas in the kettle is removed, and then carbon dioxide gas is introduced to protect the pressure in the kettle to 0.15Mpa, and the temperature in the kettle is controlled to rise to 245°C , pressure to 1.6MPa, keep the pressure for 1 hour, then slowly release the air to normal pressure, raise the temperature in the kettle to 280°C and keep the reaction for 1 hour, stop heating, water-cool the st...
Embodiment 2
[0037] (1) Add raw materials PA66 salt, melamine, cyanuric acid, benzotriazole, molecular weight modifier, antioxidant and deionized water into the reaction kettle. Wherein each component and its percentage by weight are: PA66 salt content is 82%, melamine content is 8%, cyanuric acid content is 8%, benzotriazole content is 0.2%, molecular weight regulator is 0.6%, The antioxidant is 1.2%, and the deionized water content accounts for 30% of the total mass of the above-mentioned raw materials. Close the reaction kettle and remove the gas in the kettle, and then pass in carbon dioxide gas protection until the pressure in the kettle is 0.1MPa. Control the temperature in the kettle to 210°C, the air pressure to 1.5MPa, keep the pressure for 1.5 hours, then slowly release the gas to normal pressure, raise the temperature in the kettle to 270°C and keep the reaction for 1.5 hours, stop heating, water-cool the strips to discharge, cut pellets to obtain in-situ polymerized halogen-fr...
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