Vegetable oil polyols with high hydroxyl value as well as preparation method and application of vegetable oil polyols
A technology of vegetable oil polyols and high hydroxyl value, which is applied in the preparation of organic compounds, the preparation of ester groups and hydroxyl groups, and the preparation of ethers, etc. It can solve the problems of prone to cross-linking side reactions, low product quality, and cumbersome post-processing. , to achieve the effect of novel structure, low viscosity and side reaction control
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Embodiment 1
[0042] Mix 100g epoxidized soybean oil, 149g polyol (the product of the reaction between pentaerythritol and equimolar propylene oxide) and 0.04g sodium methylate, place in a conventional kettle-type reactor, pass into nitrogen protection, mechanically stir, and heat up to 190°C, stop the reaction after 3 hours of reaction to obtain soybean oil polyol with a hydroxyl value of 750 mgKOH / g and a viscosity of 2850 mPa·s.
Embodiment 2
[0044] Take 100g of epoxidized peanut oil as component A, and another 0.1g of tetrabutyl titanate is dissolved in 108g of polyol (the product of the reaction between ethylene glycol and twice the mole of propylene oxide) as component B, and A, Component B is pumped into the microchannel modular reaction device at the same time, and the reaction is carried out in the sandwichreactorHC at normal pressure and 180°C. The injection rates of A and B components are 1.5mL / min and 1.6mL / min respectively, and the reaction is maintained. The residence time was 12 minutes, and the reaction product was collected to obtain the peanut oil polyol with a hydroxyl value of 477 mgKOH / g and a viscosity of 2800 mPa·s.
Embodiment 3
[0046] Get 100g epoxy tung oil as component A, and get 0.04g sodium tert-butoxide and dissolve it in 133g polyol (product of 1,2-propanediol and equimolar propylene oxide reaction) in addition, it is component B, mix A, Component B was pumped into the microchannel modular reaction device at the same time, and reacted in the Hastelloy microchannel reactor at normal pressure and 200 ° C. The injection rates of A and B components were 0.9 mL / min and 1.1 mL / min, respectively. mL / min, keep the reaction residence time 10min, collect the reaction product to obtain tung oil polyol, its hydroxyl value is 627mgKOH / g, and its viscosity is 2650mPa·s.
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