Polymerization process for polyesteramide
A technology of polyester amide and polymerization process, applied in the field of engineering plastics, can solve the problems of difficult continuous production of polyester amide and long reaction time, and achieve the effects of improving temperature resistance, high mixing efficiency and improving production efficiency
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Embodiment 1
[0040] A polyester amide polymerization process, the polymerization raw materials, by mass, include 5 parts of polymerized monomer dibasic acid, 5 parts of diamine and 90 parts of reactive dispersion medium polyester; uniformly disperse the polymerized monomer into the molten In a reactive dispersion medium, a polymerization reaction occurs to obtain a polyester amide with a suitable molecular weight.
Embodiment 2
[0042] A polyester amide polymerization process, the polymerization raw materials, by mass, include 60 parts of polymeric monomer dibasic acid esters, 30 parts of diamines and 10 parts of reactive dispersion medium polyester; the raw materials are added to the screw extruder by weight measurement out of the device for melting reaction and mixing evenly, and then enter the tank reaction device to complete continuous polymerization reaction and obtain polyester amide with suitable molecular weight.
[0043] The dibasic acid ester raw material contains aromatic dibasic acid ester, and the aromatic dibasic acid ester accounts for 60% of the molar ratio of the dibasic acid ester raw material.
[0044] The moisture content in the polymerization raw material does not exceed 5%.
Embodiment 3
[0046] A polyester amide polymerization process, the polymerization raw materials are calculated by mass, including 10 parts of polymerized monomer dibasic acid, 3 parts of diamine and 15 parts of reactive dispersion medium polyester amide; the raw materials are added to the screw extruder by weight measurement out of the device for melt reaction and mixing evenly, and then enter the subsequent screw extrusion device to complete the continuous polymerization reaction, and then extrude and granulate from the screw extrusion device to obtain polyester amide with a suitable molecular weight.
[0047] The screw of the screw extrusion device is sequentially divided into a feeding section and a melting and dispersing section. The material does not melt in the feeding section, and the temperature of the melting and dispersing section is not lower than the melting point of the polyester amide raw material.
[0048] First put the dibasic acid and polyester amide into the screw extrusion...
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Abstract
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