Polyamides and polyamide compositions
A technology of polyamide and diamine, which is applied in the field of polyamide and polyamide composition, can solve the problems such as difficulty in obtaining molded products, and achieve the effects of excellent heat reflow soldering resistance and excellent fogging property
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Embodiment 1
[0417] The polyamide polymerization reaction is carried out by the "prepolymer-solid-phase polymerization method".
[0418] (a) 896 g (5.20 mol) of CHDA and (b) 604 g (5.20 mol) of 2MPD were dissolved in 1500 g of distilled water to prepare a 50% by mass aqueous solution containing equimolar raw material monomers.
[0419] The resulting aqueous solution and 2MPD 18g (0.16 mol) as an additive during polymerization were put into an autoclave with an internal volume of 5.4L (Nitto High Pressure), and kept warm until the liquid temperature (internal temperature) reached 50°C, and then the inside of the autoclave was Replace with nitrogen.
[0420] Continue heating from the liquid temperature of about 50°C until the pressure in the tank of the autoclave reaches about 2.5kg / cm2 in terms of gauge pressure (hereinafter, the pressure in the tank is all expressed in gauge pressure) 2 .
[0421] In order to keep the pressure in the tank at about 2.5kg / cm 2 , remove water to the outsid...
Embodiment 2
[0427] Using the polyamide obtained in [Example 1] above, "solid phase polymerization" was further implemented.
[0428] 10 kg of polyamide pellets obtained by the prepolymer-solid-state polymerization method were charged into a conical belt vacuum dryer (manufactured by Okawara Seisakusho Co., Ltd., trade name リボコーン RM-10V) and fully replaced with nitrogen.
[0429] Heating was performed at 260° C. for 6 hours while stirring while blowing nitrogen gas at 1 L / min. Then, the temperature was lowered while flowing nitrogen gas, and when it reached about 50° C., the pellets were taken out from the apparatus as they were to obtain a polyamide.
[0430] The measurements of (1) to (10) above were performed on the obtained polyamide.
[0431] The measurement results are shown in Table 2.
[0432] [Reference Example 3 and Examples 4 to 6]
[0433] As (a) dicarboxylic acid, (b) diamine, and additives during polymerization, the compounds and amounts described in Table 1 below were use...
Embodiment 7
[0469] The polyamide obtained in Example 1 was dried in a nitrogen stream, and used after adjusting the water content to about 0.2% by mass.
[0470] Using a twin-screw extruder (TEM35 manufactured by Toshiba Machine Co., Ltd., L / D=47.6 (D=37mmφ), set temperature Tm2+20°C (at this time, 327+20=347°C), screw speed 300rpm), The polyamide (100 parts by mass) was supplied from the top feeder installed at the most upstream part of the extruder, and the side feeder on the downstream side of the extruder (in a state where the resin supplied from the top feeder was fully melted) was expressed as Glass fiber as an inorganic filler was supplied at a ratio (parts by mass) shown in 3, and the melt-kneaded product extruded from a die was cooled in a strand form and pelletized to obtain a polyamide composition.
[0471] The measurement results of the above (7), (11) and (12) of the obtained polyamide composition are shown in Table 3 below.
[0472] In addition, the tensile test was implement...
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