A method for preparing unsaturated polyester resin from recycled materials containing saturated dibasic acid
A polyester resin and dibasic acid technology, applied in the chemical industry, can solve the problems of dark resin color, reduce costs, etc., and achieve the effect of solving the problem of dark resin color, reducing costs, and reducing product production costs
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Embodiment 1
[0024] The primary esterification kettle is fed with 1932 kg of diethylene glycol and 1344 kg of ethylene glycol, 2934 kg of recycled saturated dibasic acid (containing 0.88% cobalt and manganese), and 5.9 kg of zinc acetate. The value is 7mgKOH / g, cooled to 185°C with cooling oil, added 43.6 kg of oxalic acid, kept for 1 hour, and filtered with nitrogen to remove cobalt manganese oxalate. After press filtration, throw 2618 kg of maleic anhydride, 120 kg of benzoic acid, 450 kg of propylene glycol, 0.19 kg of polymerization inhibitor, 8.7 kg of color reducer, and 10.2 kg of antioxidant, heat up to 210°C, keep warm and take samples to measure the acid value 50mgKOH / g, the viscosity is 350-400Pa·c, cool down to 190°C, start decompression and compression polymerization, gradually increase the vacuum degree to -0.08MPa, stabilize for 40 minutes, when the acid value drops to 30-35mgKOH / g, the viscosity is 500-550Pa· After the polycondensation is over, add 4.4 kg of paraffin and 0....
Embodiment 2
[0026] Feed 1974 kg of diethylene glycol and 1442 kg of ethylene glycol into the primary esterification tank, 2982 kg of recycled saturated dibasic acid (containing 0.88% cobalt and manganese), and 5.9 kg of zinc acetate. Value ≤ 7mgKOH / g, cooling oil to 185 ° C, add 44.3 kg oxalic acid, keep warm for 1 hour, nitrogen pressure filter to remove cobalt manganese oxalate. After press filtration, throw 2758 kg of maleic anhydride, 140 kg of benzoic acid, 436 kg of propylene glycol, 0.2 kg of polymerization inhibitor, 8.8 kg of color reducer, and 10.3 kg of antioxidant, heat up to 210°C, keep warm and take samples to measure the acid value 50mgKOH / g, the viscosity is 350-400Pa·c, cool down to 190°C, start decompression and compression polymerization, gradually increase the vacuum degree to -0.08MPa, stabilize for 40 minutes, when the acid value drops to 30-35mgKOH / g, the viscosity is 500-550Pa· After the polycondensation is over, add 4.47 kg of paraffin and 0.38 kg of hydroquinone...
Embodiment 3
[0028] The primary esterification kettle is fed with 2044 kg of diethylene glycol and 1428 kg of ethylene glycol, 3024 kg of recycled saturated dibasic acid (containing 0.88% cobalt and manganese), and 6.0 kg of zinc acetate. Value ≤ 7mgKOH / g, cooling oil to 185 ° C, add 44.9 kg oxalic acid, keep warm for 1 hour, nitrogen pressure filter to remove cobalt manganese oxalate. After press filtration, throw 2752 kg of maleic anhydride, 145 kg of benzoic acid, 430 kg of propylene glycol, 0.2 kg of polymerization inhibitor, 9.0 kg of color reducer, and 10.5 kg of antioxidant, heat up to 210°C, keep warm and take samples to measure the acid value 50mgKOH / g, the viscosity is 350-400Pa·s, cool down to 190°C, start decompression and compression polymerization, gradually increase the vacuum degree to -0.08MPa, stabilize for 40 minutes, when the acid value drops to 30-35mgKOH / g, the viscosity is 500-550Pa· After the polycondensation is over, add 4.5 kg of paraffin and 0.38 kg of hydroquin...
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