Polyamide production method
The polyamide production method of the present invention comprises the steps of: producing a low-order condensate by effecting a polycondensation reaction between a dicarboxylic acid component containing between about 5 and about 40 mol. % of terephthalic acid, and a diamine component containing between about 70 and about 100 mol. % of a xylylenediamine in which the content of paraxylylenediamine is between about 50 and about 100 mol. %, under conditions of a reaction temperature of at least about 200° C. and less than about 230° C.; discharging and cooling the low-order condensate at a pressure at or below atmospheric pressure, in an inert gas atmosphere; and subjecting the discharged and cooled low-order condensate to solid state polymerization. The production method makes it possible to obtain a polyamide having outstanding mechanical strength, heat resistance, color tone and the like without problems such as gelling.
1. A polyamide production method comprising:
preparing a low-order condensate through polycondensation of a dicarboxylic acid component containing about 5 mol % to about 40 mol % of terephthalic acid and a diamine component comprising about 50 mol % to about 70 mol % of p-xylylenediamine and about 30 mol % to about 50 mol % of m-xylylenediamine at a reaction temperature of about 200° C. to less than about 230° C. after adding both the dicarboxylic acid component and the diamine component to a reactor;
discharging and cooling the low-order condensate at atmospheric pressure or less under an inert gas atmosphere; and
solid-polymerizing the discharged and cooled low-order condensate,
wherein the polycondensation is performed in the presence of an end-capping agent.
2. The polyamide production method according to claim 1 , wherein preparing the low-order condensate is performed under conditions of a reaction pressure of about 0.5 MPa to about 3 MPa, a reaction time of about 0.5 hours to about 4 hours, and a moisture content of about 15 wt % to about 35 wt % in a reaction system upon completion of reaction, and the discharged and cooled low-order condensate has an inherent viscosity of about 0.07 dL/g to about 0.40 dL/g, as measured at a concentration of about 0.5 g/dL and at a temperature of about 25° C. in concentrated sulfuric acid.
3. The polyamide production method according to claim 1 , wherein the solid polymerization is performed at a maximum reaction temperature of about 170° C. to about 210° C.
4. The polyamide production method according to claim 1 , wherein the polyamide has a melting point of about 280° C. or more and a glass transition temperature of about 100° C. or more.
5. The polyamide production method according to claim 1 , further comprising:
an enrichment process before preparation of the low-order condensate.
6. The polyamide production method according to claim 1 , wherein the step of preparing a low-order condensate takes place in an aqueous solution.