Method for producing unsaturated polyester resin by using glycerinum
A polyester resin and unsaturated technology, which is applied in the field of producing unsaturated polyester resin, can solve the problems of unsaturated resin market competitiveness, unsaturated resin production cost increase, etc., and achieve excellent chemical corrosion resistance and excellent mechanical properties , the effect of a wide range of sources
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Embodiment 1
[0023] Use a 1000ml four-necked ground flask as a reaction kettle, install a thermometer, an electric stirrer, a nitrogen inlet pipe and a fractionation device respectively, and drop in 40g of glycerol, 40g of benzoic acid and 0.4g of zinc acetate catalyst successively. Slowly heat up, and start to keep warm when the kettle temperature reaches 200°C. After the measured acid value is below 10mgKOH / g, start to cool down to 130°C, and put in two-step materials: 20g of propylene glycol, 60g of diethylene glycol, 54g of phthalic anhydride, 70g of maleic anhydride, 0.2g of triphenyl phosphite, and 0.04g of hydroquinone . Then gradually heat up under the situation of feeding nitrogen, and the temperature of the distillation head is controlled below 105°C. When the temperature of the kettle reaches 200-205°C, the heat preservation reaction starts, and the acid value is controlled below 50mgKOH / g, and the vacuum is started until the acid value is lower than 35mgKOH / g. Lower the mater...
Embodiment 2
[0025] The reaction device is the same as Example 1. 70g of glycerin, 74.4g of benzoic acid, and 0.72g of zinc acetate are fed in one step; 20g of propylene glycol, 50g of diethylene glycol, 54g of phthalic anhydride, and 70g of maleic anhydride are fed in the second step; 133g of styrene is fed. Other steps are operated in the same steps as in Example 1.
Embodiment 3
[0027] The reaction device is the same as Example 1. 56g of glycerin, 54g of benzoic acid, and 0.6g of zinc acetate are fed in one step; 16g of propylene glycol, 40g of diethylene glycol, 54g of phthalic anhydride, and 70g of maleic anhydride are fed in the second step; 133g of styrene is fed. Other steps are operated in the same steps as in Example 1.
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