Method for removing free fatty acid from fatty glyceride
A technology for free fatty acids and fatty acid glycerides, which is applied in the field of removing free fatty acids in fatty glycerides, can solve the problems of difficult product use, high acid value of finished products, human injury, etc. Effect
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Embodiment 1
[0025] The high acid value fatty acid glyceride raw material is first preheated to 70° C. under the condition of a pressure of 0.08 MPa. Then pump the high acid value fatty acid glyceride into the thin film evaporator after preheating, and conduct thin film evaporation at 130°C under the pressure of 1000Pa to remove water, and then perform molecular distillation on the high acid value fatty acid that evaporates to remove water, at 220°C, Carry out molecular distillation under the condition of pressure 10Pa, collect glyceride fraction to obtain the fatty acid glyceride of low acid value, and its acid value is 0.30mgKOH / g.
Embodiment 2
[0027] The high acid value fatty acid glyceride raw material is heated to 70°C under the pressure of 0.07MPa. Preheated high-acid glycerides are pumped into the thin-film evaporator, and thin-film evaporation is performed at 110°C and a pressure of 900Pa, and the high-acid fatty acids are evaporated to remove water, followed by molecular distillation, which is carried out at 200°C and a pressure of 10Pa. The glyceride fraction obtains fatty acid glycerides with low acid value, and its acid value is 0.33mgKOH / g.
Embodiment 3
[0029] The high fatty acid glyceride raw material is heated to 70°C under the pressure of 0.08MPa. Preheated high-acid glycerides are pumped into the thin-film evaporator, and thin-film evaporation is performed at 100°C and a pressure of 1000Pa, and the high-acid fatty acids are evaporated to remove moisture, followed by molecular distillation, which is carried out at 180°C and a pressure of 9Pa. The glyceride fraction obtains fatty acid glycerides with low acid value, and its acid value is 0.36mgKOH / g.
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Abstract
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