Spun filament type low-melting-point polyester chip and preparation method thereof
A low-melting-point polyester and filament technology, which is applied in the field of spinning filament-type low-melting-point polyester, can solve problems such as poor wearing comfort, lower melting point, and affect filament strength, and achieve hot-melt adhesive flow performance Excellent, reduced polycondensation cycle, and improved production efficiency
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Embodiment 1
[0029] The preparation method of spinning filament type low-melting point polyester chip in the present embodiment is as follows:
[0030] Step 1, one esterification
[0031] Step 11. Add 255kg of IPA and 300kg of TEG (alkyd molar ratio: 1.3) to the slurry preparation kettle. After stirring evenly, add the esterification kettle through a metering pump to carry out the esterification reaction. The esterification temperature is controlled at 255-260 ℃, the esterification pressure is controlled at normal pressure, and the esterification reaction of TEG is completed when the esterification water is received to 44kg (the esterification rate is 80%).
[0032] Step 12. Add 1625kg of IPA and 1300kg of DEG (alkyd molar ratio: 1.25) to the slurry configuration kettle. After stirring evenly, add an esterification kettle through a metering pump to carry out the esterification reaction. The esterification temperature is controlled at 250-255 °C, the esterification pressure is controlled a...
Embodiment 2
[0040] The preparation process of this embodiment is the same as that of Example 1, the difference is that: in Example 1, the total amount of PTA is 5500kg, and the total amount of IPA is 2200kg; in this embodiment, the total amount of PTA is 5000kg, and the total amount of IPA is 2700kg; Process, all carries out according to the alkyd acid molar ratio of embodiment 1.
Embodiment 3
[0042] The preparation process of this embodiment is the same as that of Example 1, the difference being that: in Example 1, the total amount of PTA is 5500kg, and the total amount of IPA is 2200kg; in this embodiment, the total amount of PTA is 4500kg, and the total amount of IPA is 3200kg; Process, all carries out according to the alkyd acid molar ratio of embodiment 1.
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