Phosphoric flame-proof copolyester ionomer and preparation method thereof
A flame-retardant copolyester and ionomer technology, which is applied in the field of phosphorus-containing flame-retardant copolyester ionomer and its preparation, can solve the limited contribution of flame-retardant properties, destroy the regularity of polyester chains, and affect polyester Molecular crystallization and other problems to achieve the effect of increasing viscosity, ingenious molecular design, good regularity and symmetry
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Embodiment 1
[0052] Add 860g of terephthalic acid, 433mL of ethylene glycol (EG) and 0.301g of antimony trioxide into the reaction kettle, fill with nitrogen to remove the air in the kettle, pressurize to 0.07MPa; within 2h, raise the temperature to 240°C to start esterification Reaction, control the pressure in the kettle to be 0.3-0.4MPa. After maintaining for 2 hours, the pressure begins to decrease. After 1.5 hours, the temperature gradually rises to 260°C, the pressure drops to normal pressure, and the esterification reaction ends; nitrogen is slowly introduced into the reaction kettle, And the ionic monomer 3-(2-hydroxyethoxy)-3-oxopropyl (phenyl) sodium phosphinate (SHPPP) of 1.45g, the ethylene glycol solution is added in the reactor, and the temperature is controlled Above 210°C, when the temperature of the system rises slowly to 260°C, stop the nitrogen system and enter the vacuum polymerization stage, firstly, 260-270°C low vacuum polycondensation reaction for 0.5h, then raise th...
Embodiment 2
[0056] 860g of terephthalic acid, 433mL of ethylene glycol and 0.301g of antimony trioxide were added to the reactor, and the esterification reaction was carried out according to the steps and conditions given in Example 1; Nitrogen, and the ethylene glycol solution of the ionic monomer 3-(2-hydroxyethoxy)-3-oxopropyl (phenyl) phosphinate sodium of 14.5g is added in the reactor, and then according to the embodiment The steps and conditions given in 1 are carried out after polycondensation, and the material is discharged.
[0057] The intrinsic viscosity [η] of the ionomer is 0.67dL / g; the limiting oxygen index LOI is 25.6.
Embodiment 3
[0059] 860g of terephthalic acid, 433mL of ethylene glycol and 0.301g of antimony trioxide were added to the reactor, and the esterification reaction was carried out according to the steps and conditions given in Example 1; Nitrogen, and the ethylene glycol solution of the ionic monomer 3-(2-hydroxyethoxy)-3-oxopropyl (phenyl) phosphinate sodium of 72.5g is added in the reactor, and then according to the embodiment The steps and conditions given in 1 are carried out after polycondensation, and the material is discharged.
[0060] The intrinsic viscosity [η] of the ionomer is 0.64dL / g; the limiting oxygen index LOI is 27.0.
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