Semi-aromatic polyamide and preparation method thereof
A semi-aromatic and polyamide technology, which is applied in the field of semi-aromatic polyamide preparation, can solve the problems of uncontrollable molecular weight of semi-aromatic polyamide, difficulty in meeting the requirements of industrialized large-scale production, irregular distribution of molecular segments, etc. The process is green and environmentally friendly, the production cost is low, and the reaction is easy to control.
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Embodiment 1
[0058]30Kg of solid hexamethylenediamine with a content of more than 99.7% was completely dissolved in a water bath at 65°C and added to the stirring polymerization reactor, then the stirring was started, 15Kg deionized water was added to the reactor, and 24.50Kg was added to the reactor. of terephthalic acid, 14.38Kg of adipic acid, 590.7g of acetic acid, 130.3g of sodium hypophosphite, 194.4g of polydimethylsiloxane, and then added 2.5Kg of deionized water to the reactor, using After 3 times of nitrogen replacement, the temperature began to rise. When the temperature rose to 130 °C, the exhaust valve on the reactor was opened to exhaust for 2 minutes, and then the temperature continued to rise. The temperature was raised to 220°C within 1.5 hours, the temperature was maintained at 220°C for 10 min, and then the reaction temperature was continued to rise to 240°C. During the heating process, when the reaction pressure reached 2.0MPa, the exhaust valve was opened to discharge ...
Embodiment 2
[0062] The preparation steps of Example 1 were repeated, except that the tackifying method of the prepolymer was changed to solid-phase polymerization. Under the conditions of nitrogen atmosphere and 250°C, solid-phase polymerization was carried out for 8 hours to obtain light yellow semi-aromatic polyamide resin. Its intrinsic viscosity is 0.89dL / g, glass transition temperature is 94.76℃, melting point is 316.07℃, melting enthalpy is 52.53J / g, decomposition temperature is 424℃, and molecular weight distribution is 3.7.
Embodiment 3
[0064] 30Kg of solid hexamethylenediamine with a content of more than 99.7% was completely dissolved in a water bath at 65 ° C and added to the stirring polymerization reactor, then the stirring was started, 15Kg deionized water was added to the reactor, and 24.75Kg was then added to the reactor. terephthalic acid, 16.50Kg isophthalic acid, 606.5g benzoic acid, 157.9g sodium hypophosphite, 195.1g polydimethylsiloxane, then add 2.81Kg deionized water in the reactor After 3 times of nitrogen replacement, the temperature rises. When the temperature rises to 130 °C, open the exhaust valve on the reactor to exhaust for 2 minutes, and then continue to heat up. The temperature was raised to 230°C within 1.5 hours, the temperature was maintained at 230°C for 10 min, and then the reaction temperature was continued to rise to 250°C. During the heating process, when the reaction pressure reached 2.50MPa, the exhaust valve was opened to discharge the steam to keep the pressure constant at...
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