Method for reducing oilseed acid value
A technology of oil acid value and oil, which is applied in the direction of fatty acid esterification, etc., can solve the problems of difficult recovery of glycerin, cumbersome process operation, and large material loss, so as to be beneficial to environmental protection and subsequent processing, simplify operation steps, and reduce oil acid value effect
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Embodiment 1
[0024] Provide acidified oil with an acid value of 140mgKOH / g and methanol into the tubular reactor, and the liquid hourly space velocity of the acidified oil is 0.6h -1 , the molar ratio of alcohol to oil is 5.8, the temperature in the reactor is 246°C, the pressure is 0.7MPa, and the acid value of the oil after reaction is 17.6mgKOH / g.
Embodiment 2
[0026] Provide acidified oil with an acid value of 152mgKOH / g and methanol into the tubular reactor, and the hourly space velocity of the acidified oil is 0.6h -1 , the molar ratio of alcohol to oil is 5.8, the temperature in the reactor is 213° C., the pressure is 2.5 MPa, and the acid value of the oil after reaction is 16.9 mgKOH / g.
Embodiment 3
[0028] Food waste oil and methanol with an acid value of 87mgKOH / g are used as raw materials and supplied to the tubular reactor, and the hourly space velocity of the waste oil is 0.6h -1 , the molar ratio of alcohol to oil is 5.8, the temperature in the reactor is 262°C, the pressure is 0.7MPa, and the acid value of the oil after reaction is 3.5mgKOH / g.
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