Method for producing polyamide
A process for the manufacture of polyamide is described. Also described, is a process comprising a stage of initial polymerization under pressure starting from monomers and a stage of finishing in the liquid phase at atmospheric pressure. The finishing stage can employ an injection of inert gas along a direction essentially parallel to that of the flow of the liquid reaction stream.
1. A process for the continuous manufacture of a polyamide, the process comprising initial polymerization under pressure starting from monomers and finishing in a liquid phase at a pressure in a vicinity of atmospheric pressure, wherein the finishing is carried out in a horizontal-axis reactor, in the lower part of which a liquid reaction stream flows and in the upper part of which, the upper part being composed of a gaseous headspace above a liquid reaction stream, injecting an inert gas, wherein the inert gas is injected at the end of the finishing reactor, according to a direction essentially parallel to that of the flow of the liquid reaction stream and in the direction of this flow.
2. The method as defined by claim 1 , wherein the monomers are a dicarboxylic acid and a diamine.
3. The method as defined by claim 1 , wherein the polyamide is a polyamide 66 or a copolyamide, the majority of the repeat units of which are polyamide 66 units, the dicarboxylic acid being adipic acid and the diamine being hexamethylenediamine.
4. The method of as defined by claim 1 , wherein the monomers are a lactam and/or an amino acid.
5. A method as defined by claim 4 , wherein the polyamide is a polyamide 6 or a copolyamide, the majority of the repeat units of which are polyamide 6 units, the lactam being caprolactam and/or the amino acid being aminohexanoic acid.
6. The method as defined by claim 1 , wherein a degree of progression of polycondensation at an outlet of the initial polymerization is greater than 90% for a polyamide 66.
7. The method as defined by claim 1 , wherein the dilution factor for steam in the headspace of a finishing reactor, when the inert gas is introduced, is greater than 2.
8. The method as defined by claim 1 , wherein residence time of a gas phase in a finishing reactor is less than or equal to 30 min.
9. The method as defined by claim 1 , wherein a residence time of a liquid phase in a finishing reactor is greater than 5 minutes.
10. The method as defined by claim 1 , wherein an initial polymerization reactor and a finishing reactor are placed in an enclosure or jacket comprising a heat-exchange fluid.
11. The method as defined by claim 8 , wherein the residence time of the gas phase in the finishing reactor is less than or equal to 20 min.