Device and method for continuous preparation of particulate polyamide resin
A polyamide resin, particle-like technology, applied in chemical instruments and methods, chemical/physical/physical chemical processes, chemical/physical processes, etc., can solve the problem of limited particle size control, continuous preparation difficulties, and difficulty in ring-opening. Aggregation etc.
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[0053] As an example of the present invention, a continuous preparation method of particulate polyamide resin is provided, the continuous preparation method of the above-mentioned particulate polyamide resin comprises: a step of first polymerizing monomers containing 2-pyrrolidone in a continuous reactor ; and after carrying out the above-mentioned first polymerization, the step of carrying out the second polymerization in the extrusion reactor.
[0054] The continuous production method of the above-mentioned particulate polyamide resin may further include the step of reacting the above-mentioned monomer containing 2-pyrrolidone with a catalyst in advance.
[0055] The above-mentioned 2-pyrrolidone-containing monomers can be obtained from biomass.
[0056] The above-mentioned monomer containing 2-pyrrolidone is preferably a single form of 2-pyrrolidone monomer or a mixed form of 2-pyrrolidone monomer and a lactam monomer having 5 to 7 carbon atoms, but is not limited thereto. ...
Embodiment 1
[0077] Put 4250g of 2-pyrrolidone as a monomer, put 420g of potassium hydroxide as a basic catalyst, and remove water while reacting with the catalyst for 1 hour and 30 minutes under reduced pressure at a temperature of 85°C. . Afterwards, the activated reactant was sent to a continuous stirring reactor, and 88 g of carbon dioxide initiator and 15.8 g of 1,6-hexamethylene diisocyanate were added as isocyanate compounds, and the temperature was reduced at 100° C. Under pressure conditions, the first polymerization was carried out for 1 hour. After the first polymerization, the first polymer was conveyed to a kneading extruder, and a second polymerization was performed at a temperature of 100° C. under reduced pressure for 5 hours to prepare a nylon 4 resin.
Embodiment 2
[0079] It was the same as Example 1 except that 1275 g of 2-pyrrolidone and 3955 g of ε-caprolactam were used as monomers to prepare nylon 4,6 resin.
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