Production process and use of polyester polyol and its modifying material
A polyester polyol and production process technology, applied in the field of chemical raw material production, can solve the problems of not mentioning vegetable oil, unfavorable production efficiency, etc., and achieve the effects of good dimensional stability, good flame retardancy and cost reduction
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Embodiment 1
[0028] The preparation of embodiment 1 polyester polyol A:
[0029] Add 7.50 kg of castor oil, 1.49 kg of glycerin and 1.40 g of tetrabutyl titanate into a reactor equipped with a stirrer, a thermometer, and a nitrogen inlet pipe, raise the temperature to 220-240°C under the protection of nitrogen, and keep the temperature for 4 hours. Promptly obtain alcoholyzed castor oil A;
[0030] 17.88 kilograms of phthalic anhydride, 25.61 kilograms of diethylene glycol, alcoholyzed castor oil A and 3 grams of tetrabutyl titanate were added to an 80-liter reaction kettle equipped with a stirrer, a thermometer, a nitrogen inlet pipe and a rectification tower, under nitrogen protection Heat up to 200-220°C, keep warm for reaction, distill 2.10 kg of water; then slowly depressurize, adjust the vacuum degree at 0.075-0.085Mpa, keep warm at 200-220°C until the acid value is qualified.
[0031] The acid value of the product is 1.2mgKOH / g, the viscosity is 3700mPa·s (25°C), and the hydroxyl v...
Embodiment 2
[0032] The preparation of embodiment 2 polyester polyol B:
[0033] Add 7.5 kg of castor oil, 1.65 kg of pentaerythritol and 1.4 g of tetrabutyl titanate into a reactor equipped with a stirrer, a thermometer, and a nitrogen inlet tube, and raise the temperature to 220-240°C under the protection of nitrogen, and keep the temperature for 4 hours. Promptly obtain alcoholyzed castor oil B;
[0034] 17.88 kilograms of phthalic anhydride, 25.61 kilograms of diethylene glycol, alcoholyzed castor oil B and 3 grams of tetrabutyl titanate were added to an 80-liter reaction kettle equipped with a stirrer, a thermometer, a nitrogen inlet pipe and a rectification tower, under nitrogen protection Heat up to 200-220°C, keep warm for reaction, distill 2.10 kg of water; then slowly depressurize, adjust the vacuum degree at 0.075-0.085Mpa, keep warm at 200-220°C until the acid value is qualified.
[0035] The acid value of the product is 1.3mgKOH / g, the viscosity is 3800mPa·s (25°C), and the h...
Embodiment 4
[0042] The preparation of embodiment 4 polyisocyanurate foam:
[0043] As shown in Table 2, the polyester polyol component, catalyst, and foam stabilizer were mixed according to the ratio shown in Table 2, and preheated to 26°C. Then the polyisocyanate component preheated to 26°C was added to the polyol mixing component according to the ratio in Table 2, stirred for 6 seconds, and poured into a wooden box to form a polyisocyanurate foam.
[0044] PIR 1
PIR 2
PIR 3
Polyester polyol A
100
90
Polyester polyol B
100
Polyether 4110
10
H2O
0.5
0.5
0.5
DC5098
2
2
2
TCPP
20
20
20
POLYCAT 5
1.2
1.2
1.2
DABCO TMR-2
2
2
2
DABCO TMR-3
0.4
0.4
0.4
HCFC-141b
40
40
40
PM 200
240
...
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Abstract
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