Polyester polyol as well as preparation method and application thereof
A polyester polyol and polyol technology, applied in the field of polyester polyol and its preparation, can solve the problems of harsh production environment, limited product performance, etc., and achieve the effects of long service life, strong crystallinity and cost saving
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Embodiment 1
[0022] Add 4672Kg of adipic acid, 5312Kg of terephthalic acid, 4992Kg of ethylene glycol, 1.5Kg of catalyst tetrabutyl titanate to the reaction kettle; seal the kettle with nitrogen, heat it to 140°C and control the reflux tower top temperature at 101°C to Heating rate per hour at 10℃ to 220℃, react at 220℃ for 3h, when the water output rate reaches more than 90%, control the water output rate to 200Kg / h, turn on the vacuum pump to vacuum until the acid value drops below 1.0mgKOH / g , Prepared a polyester polyol with a hydroxyl value of 113.18mgKOH / g and an acid value of 0.30mgKOH / g, using it and TDI-100 to synthesize a prepolymer with an isocyanate content of 6.2% by weight, and the prepolymer It reacts with MOCA in a mass ratio of 100:17.7 to obtain a polyurethane elastomer.
[0023] The performance is as follows: hardness 69D, rebound 37%, tear strength: 195.58KN / m, DIN wear: 43.23mm 3 , And the performance of polyurethane elastomer made of polyester polyol synthesized with adi...
Embodiment 2
[0025] Add 3776Kg of succinic acid, 666.3Kg of terephthalic acid and 3109Kg of ethylene glycol to the reaction kettle. The catalyst is 0.13Kg of tetrabutyl titanate; the kettle is sealed with nitrogen, and the reflux tower top temperature is controlled at 102°C after heating to 145°C. , Heat up to 222±2℃ at a heating rate of 15℃ per hour, react for 2.5h at 222±2℃, when the water output rate reaches 90% or more, control the water output rate to 1200Kg / h, turn on the vacuum pump to vacuum to the acid value Decrease below 1.0mgKOH / g, temperature? A polyester polyol with a hydroxyl value of 112.90mgKOH / g and an acid value of 0.29mgKOH / g was prepared, and a prepolymer with an isocyanate content of 4.5% by weight was synthesized with MDI-100. BDO reacts according to the mass ratio of 100:4.6 to obtain polyurethane elastomer.
[0026] The performance is as follows: hardness 49D, rebound 34%, tear strength: 152.38KN / m, DIN abrasion: 40.77mm 3 , And the performance of polyurethane elasto...
Embodiment 3
[0028] Add 1332Kg of adipic acid, 7548Kg of terephthalic acid, and 6216Kg of butanediol to the reaction kettle. The catalyst is 0.35Kg of stannous octoate; the kettle is sealed with nitrogen, and the temperature of the reflux tower top is controlled at 101°C after heating to 140°C. The heating rate per hour is increased to 223℃, and the reaction is carried out at 223℃ for 4 hours. When the water output rate reaches 90% or more, the water output rate is controlled to 1000Kg / h, and the vacuum pump is turned on to vacuum until the acid value drops below 1.0mgKOH / g. A polyester polyol with a hydroxyl value of 76.02mgKOH / g and an acid value of 0.37mgKOH / g was prepared, and a prepolymer with an isocyanate content of 3.6% by weight was synthesized with liquefied MDI. The prepolymer was combined with E -300 reacts according to the mass ratio of 100:6.87 to obtain polyurethane elastomer.
[0029] The performance is as follows: hardness 77D, rebound 39%, tear strength: 219.37KN / m, DIN wear...
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