Method for preparing polyester polyol with polyethylene terephthalate waste material
A technology of polyethylene terephthalate and polyester polyol, which is applied in the field of polyester polyol, can solve problems such as easy crystallization, increase production cost, affect hydrolysis resistance stability and catalyst activity, and achieve environmental pollution small effect
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Embodiment 1
[0021] Feed 384g of PET waste, 230g of diethylene glycol, and 2g of tetrabutyl titanate. Under nitrogen protection, raise the temperature at 180°C and stir for 5 hours. Add 100g of epoxy biodiesel and react at 200°C for 4 hours. Turn off the nitrogen, vacuumize, keep the vacuum at -0.07MPa, control the temperature at 210°C, heat and stir for 2 hours, and cool to obtain the product. The product has a hydroxyl value of 308mgKOH / g, a viscosity (25°C) of 2500cps, and an acid value of <0.2mgKOH / g.
Embodiment 2
[0023] Feed 384g of PET waste, 130g of diethylene glycol, 74.5g of triethanolamine, and 2g of antimony trioxide. Under nitrogen protection, raise the temperature at 220°C and stir for 4 hours, add 110g of epoxy biodiesel and 100g of diethylene glycol, and react at 200°C for 8 Hour. Turn off the nitrogen, vacuumize, keep the vacuum at -0.07MPa, control the temperature at 210°C, keep stirring for 4 hours, and cool to obtain the product. The product has a hydroxyl value of 450mgKOH / g, a viscosity (25°C) of 3500cps, and an acid value of <0.2mgKOH / g.
Embodiment 3
[0025] Feed 384g of PET waste, 160g of diethylene glycol, 67g of trimethylolpropane, and 3g of tetrabutyl titanate. Under the protection of nitrogen, heat up to 200°C and stir for 6 hours. Add 180g of epoxy biodiesel and 140g of diethylene glycol, 200 °C for 4 hours. Turn off the nitrogen, vacuumize, keep the vacuum at -0.07MPa, control the temperature at 220°C, keep stirring for 5 hours, and cool to obtain the product. The product has a hydroxyl value of 400mgKOH / g, a viscosity (25°C) of 3000cps, and an acid value of <0.2mgKOH / g.
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Abstract
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