Styrene-free environment-friendly unsaturated resin for insulating paint and preparation process thereof
A styrene-free, preparation technology, applied in the direction of coatings, polyester coatings, etc., can solve the problems of human health and environmental hazards, low flash point, volatile, etc., to maintain curing performance, improve compatibility, change regularity effect
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Embodiment 1
[0019] The unsaturated resin components include 2 parts of propylene glycol, 1 part of ethylene glycol, 2 parts of diethylene glycol, 3 parts of maleic anhydride, 4 parts of phthalic anhydride, 5 parts of benzoic acid and phthalic acid in parts by weight. 4 parts of diallyl diformate, 2 parts of vinyl toluene.
[0020] The preparation process of the present embodiment comprises the following steps:
[0021] A. Polycondensation reaction: react propylene glycol, ethylene glycol, diethylene glycol with maleic anhydride and phthalic anhydride in a molar ratio of 2:2:1:3:1 until the acid value reaches 60mgKOH / g;
[0022] B, end-capping esterification reaction: step A polycondensation reactant is cooled to 160 ℃, adding molar weight is the organic terminal acid benzoic acid of polycondensation reaction alcohol molar weight 12% and reacts, reaches 60mgKOH / g to acid value;
[0023] C, vacuum negative pressure reaction: open the vacuum pump, make the polyester obtained in step B pre...
Embodiment 2
[0030] The unsaturated resin components include 6 parts by weight of propylene glycol, 3 parts of ethylene glycol, 5 parts of diethylene glycol, 6 parts of maleic anhydride, 8 parts of phthalic anhydride, 10 parts of benzoic acid, 10 parts of diallyl diformate, 6 parts of vinyl toluene.
[0031] The preparation process of the present embodiment comprises the following steps:
[0032] A. Polycondensation reaction: react propylene glycol, ethylene glycol, diethylene glycol with maleic anhydride and phthalic anhydride in a molar ratio of 2:2:1:3:1 until the acid value reaches 65mgKOH / g;
[0033] B, end-capping esterification reaction: step A polycondensation reactant is cooled to 160 ℃, adding molar mass is the organic terminal acid benzoic acid of polycondensation reaction alcohol molar mass 12% and reacts, reaches 65mgKOH / g to acid value;
[0034] C, vacuum negative pressure reaction: open the vacuum pump, make the polyester obtained in step B pressurize and heat, until the ...
Embodiment 3
[0041] The unsaturated resin components include 3 parts by weight of propylene glycol, 2 parts of ethylene glycol, 3 parts of diethylene glycol, 4 parts of maleic anhydride, 5 parts of phthalic anhydride, 6 parts of benzoic acid, 5 parts of diallyl diformate, 3 parts of vinyltoluene.
[0042] The preparation process of the present embodiment comprises the following steps:
[0043] A. Polycondensation reaction: react propylene glycol, ethylene glycol, diethylene glycol with maleic anhydride and phthalic anhydride in a molar ratio of 2:2:1:3:1 until the acid value reaches 62mgKOH / g;
[0044] B, end-capping esterification reaction: step A polycondensation reactant is cooled to 160 ℃, adds molar mass and is the organic terminal acid benzoic acid of polycondensation reaction alcohol molar mass 12% and reacts, reaches 61mgKOH / g to acid value;
[0045] C, vacuum negative pressure reaction: open the vacuum pump, make the polyester obtained in step B pressurize and heat, until the a...
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