Preparation process of neopentyl polyacohol octocapric acid ester
A technology of neopentyl polyol and alcohol octadecanoate, applied in the preparation of carboxylate, the preparation of organic compounds, organic chemistry and other directions, can solve the problems of high production cost, lower acid value and darker color, etc. The effect of lower production costs, lower operating pressures and temperatures, and lower overall costs
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[0012] The preparation technology of neopentyl polyalcohol octadecanoic acid ester of the present invention, utilizes molecular distillation technology to refine the method for neopentyl polyalcohol octadecanoic acid ester to comprise the steps: (1) take neopentyl polyalcohol and octadecanoic acid as The raw materials are fed according to a certain ratio, and the crude product is obtained by esterification reaction under the condition of p-toluenesulfonic acid as a catalyst; (2) the crude product is subjected to molecular distillation to obtain a nearly colorless, low acid value, high-quality Neopentyl polyol capryl decanoate.
[0013] In the esterification reaction in the step (1), the raw material neopentyl polyol can be pentaerythritol, trimethylolpropane and neopentyl glycol; the alkyd molar ratio can be pentaerythritol and caprylic acid ester 1: 4.1~4.4, Trimethylol propane and octadecanoic acid ester 1: 3.1~3.3, neopentyl glycol and octadecanoic acid ester 1: 2.1~2.2; th...
Embodiment 1
[0017] Add 136g of pentaerythritol, 687.3g of octadecanoic acid, and 8.2g of p-toluenesulfonic acid (alkyd molar ratio: 1:4.35) in sequence in a 1000mL esterification reaction kettle equipped with a water separator, blow nitrogen gas, and start stirring Slowly raise the temperature to 180-185°C, and react at this temperature, distill off the water generated by the reaction, after 4.0 hours of reaction, no water has been distilled out, and after cooling down to 60°C, the crude product of pentaerythritol caprylic decanoate is obtained; then the crude product is packed into the constant temperature storage tank, and then into the first-level wiped-film molecular still to separate and remove water, low molecular weight components and free p-toluenesulfonic acid. The evaporation temperature is 130°C and the vacuum is 500Pa; About 55g of unreacted octadecanoic acid was separated by a molecular still, the evaporation temperature was 160°C, and the vacuum degree was 10Pa. The obtained ...
Embodiment 2
[0019] Add 136g of pentaerythritol, 647.8g of octadecanoic acid, and 6.3g of p-toluenesulfonic acid (the molar ratio of alkyd to acid: 1:4.1) in sequence in a 1000mL esterification reaction kettle equipped with a water separator. Slowly raise the temperature to 175-180°C, and react at this temperature, distill off the water generated by the reaction, and after 5.0 hours of reaction, no water has been distilled out, and after cooling down to 60°C, the crude product of pentaerythritol caprylic decanoate is obtained; then the crude product is packed into the constant temperature storage tank, and then into the first-stage wiped-film molecular still to separate and remove water, low molecular weight components and free p-toluenesulfonic acid. The evaporation temperature is 120°C and the vacuum degree is 100Pa; About 15g of unreacted octadecanoic acid was separated by the molecular still, the evaporation temperature was 150°C, and the vacuum degree was 1Pa. The obtained nearly color...
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