Preparation method of novel waste cooking oil based unsaturated polyester resin
A technology for waste edible oil and polyester resin, which is applied in the field of preparation of new unsaturated polyester resin from renewable waste edible oil, can solve the problems of limited production scale and limited reuse of waste edible oil, and achieves dimensional stability of products Good, lower production cost, high hardness
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[0034] Preparation of B monoglyceride
[0035] Put waste cooking oil and glycerin with an acid value less than 1mgKOH / g into the reactor at a ratio of 2.5:1 to 3:1, and feed N into the reactor. 2 , at N 2 Under protection, add 0.1 to 0.3% catalyst Ca(OH) of the sum of waste edible oil and glycerol with a relative acid value less than 1mgKOH / g to the reactor 2 , the reaction kettle is heated to 210-250°C, and the catalyst Ca(OH) 2 Carry out alcoholysis reaction on the waste edible oil with an acid value less than 1mgKOH / g under the action, the reaction time is 3-5h, and then the temperature drops below 15°C to obtain monoglyceride, which is ready for use.
[0036] Carry out alcoholysis reaction of waste cooking oil with acid value less than 1mgKOH / g and glycerol to obtain monoglyceride, the general reaction formula is as follows:
[0037]
[0038]The synthesis principle of this step is: the redistribution of fatty acids occurs under the temperature of 210-250° C. and the ...
Embodiment 1
[0050] Embodiment 1, according to the above-mentioned preparation method:
[0051] A pre-esterification treatment of waste cooking oil
[0052] Put the preliminary purified 70% waste cooking oil and 30% glycerin into an autoclave, react at a high temperature of 200°C for 6 hours, carry out pre-esterification treatment on the preliminary purified waste cooking oil, after the pre-esterification treatment The acid value of waste cooking oil is 0.8mgKOH / g.
[0053] Preparation of B monoglyceride
[0054] Put waste edible oil and glycerin with an acid value of 0.8mgKOH / g into the reactor at a ratio of 2.5:1, and feed N into the reactor. 2 , at N 2 Under protection, add 0.1% catalyst Ca(OH) of the waste edible oil and glycerin amount of relative acid value 0.8mgKOH / g in the reactor 2 , the reaction kettle is heated to 210 ° C, in the catalyst Ca(OH) 2 Carry out alcoholysis reaction on the waste cooking oil with an acid value of 0.8mgKOH / g under the action of 3h, and then the te...
Embodiment 2
[0059] Embodiment 2, according to the above-mentioned preparation method:
[0060] A pre-esterification treatment of waste cooking oil
[0061] Put the preliminary purified 80% waste cooking oil and 20% glycerin into the autoclave, react at a high temperature of 215°C for 8 hours, carry out pre-esterification treatment on the preliminary purified waste cooking oil, after the pre-esterification treatment The acid value of waste cooking oil is 0.7mgKOH / g.
[0062] Preparation of B monoglyceride
[0063] Put waste edible oil and glycerin with an acid value of 0.7mgKOH / g into the reactor at a ratio of 2.7:1, and feed N into the reactor. 2 , at N 2 Under protection, add the catalyst Ca(OH) of 0.2% of the waste edible oil and glycerin amount of relative acid value 0.7mgKOH / g in the reactor 2 , the reaction kettle was heated to 230°C, and the catalyst Ca(OH) 2 Carry out alcoholysis reaction on the waste cooking oil with an acid value of 0.7mgKOH / g under the influence of alcoholy...
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