Polyamide composition, and preparation method and application thereof
A technology of polyamide composition and polyamide, which is applied in the field of low-corrosion polyamide composition and low precipitation, and can solve problems such as easy precipitation, corrosion of extruder and other equipment, and affecting the performance of polyamide composition
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Embodiment 1
[0064] Add nylon 6, aluminum tris(diethylphosphinate), melamine polyphosphate, epoxy resin and zeolite into the twin-screw extruder through the main feed port of the twin-screw extruder according to the weight parts in Table 1 The polyamide composition is obtained after extrusion granulation, cooling, and drying; wherein, the process conditions of the extruder are: the temperature of the first and second stages of the twin-screw extruder is 230~250°C, and the temperature of the third and fourth stages is 250~270°C, the temperature of the fifth and sixth stages is 260~280°C, the temperature of the seventh and eighth stages is 240~270°C, the temperature of the head is 230~270°C, and the screw speed is 150~350 rpm.
[0065] The properties of the prepared polyamide composition were tested and listed in Table 1.
Embodiment 2
[0067] Nylon 66, tris(diethylphosphinate)aluminum, zinc borate, ethylene-maleic anhydride copolymer and zinc oxide were added to the double-screw extruder through the main feed port of the twin-screw extruder according to the weight parts in Table 1. The polyamide composition is obtained after extruding, granulating, cooling, and drying in a screw extruder; wherein, the process conditions of the extruder are: the temperature of the first and second stages of the twin-screw extruder is 230~250°C, and the temperature of the third stage , The temperature of the fourth stage is 250~270°C, the temperature of the fifth and sixth stage is 260~280°C, the temperature of the seventh and eighth stage is 240~270°C, the temperature of the head is 230~270°C, and the screw speed is 150~350 rpm .
[0068] The properties of the prepared polyamide composition were tested and listed in Table 1.
Embodiment 3
[0070] Nylon 6 / 6T, bis(diethylphosphinate) zinc, melamine cyanurate, styrene-maleic anhydride copolymer and sodium hydroxide are passed through a twin-screw extruder according to the weight parts in Table 1 The main feed port of the twin-screw extruder is added into a twin-screw extruder to extrude, granulate, cool, and dry to obtain a polyamide composition; wherein, the process conditions of the extruder are: the temperature of the first and second sections of the twin-screw extruder is 230~250°C, the temperature of the third and fourth stages is 250~270°C, the temperature of the fifth and sixth stages is 260~280°C, the temperature of the seventh and eighth stages is 240~270°C, the temperature of the head is 230~270°C, the screw speed 150~350 rpm.
[0071] The properties of the prepared polyamide composition were tested and listed in Table 1.
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