Patent ID: 8759476

Claim:
A process for preparing a polyamide based on dicarboxylic acids and diamines, comprising the following stages: 1) providing an aqueous monomer mixture consisting of a dicarboxylic acid mixture of from 60 to 88% by weight of terephthalic acid and from 12 to 40% by weight of isophthalic acid, in which up to 20% by weight of the dicarboxylic acid mixture may be replaced by other dicarboxylic acids, and hexamethylenediamine which may be up to 20% by weight replaced by other C 2-30 − diamines, the molar ratio of dicarboxylic acids to diamines being adjusted such that a molar deficiency of diamines of from 1 to 10 mol % is present at the outlet of stage 3), based on the other component in each case, 2) transferring the aqueous mixture from stage 1) to a continuous evaporator reactor which is a vertical tubular reactor flowed through from the top downward in which diamines and dicarboxylic acids are reacted at a temperature in the range from 100 to 370° C. and a pressure in the range from 1 to 50 bar, 3) transferring the mixture from stage 2) to a separator which is operated at a temperature in the range from 100 to 370° C. with removal of gaseous components, wherein said separator is under a pressure of 16-17 bar, 4) transferring the mixture from stage 3) together with diamine in an amount suitable to balance out the molar deficiency and to increase the amino end group content by at least 20 mmol/kg into an extruder which is operated at a temperature in the range from 150 to 400° C. for a residence time in the range from 10 seconds to 30 minutes to remove gaseous components through devolatilizing orifices; wherein, in the monomer mixture, equimolar amounts of dicarboxylic acids and diamines are present, from 0.5 to 15% by weight of the hexamethylenediamine used in stage 1) is removed in gaseous form in the separator in stage 3), and sufficient hexamethylenediamine is added in stage 4) that the content of amino end groups in the resulting polyamide at the end of the extruder is from 70 to 220 mmol/kg; and wherein steam and volatile dicarboxylic acids or diamines are removed in stage 3) and are subsequently separated by distillation, and an aqueous condensate enriched in dicarboxylic acid or diamine is recycled into one or both of stages 1) and 2).