Co-production method for extracting idesia polycarpa grease and phospholipid
A phospholipid and oil technology, applied in the direction of fat oil/fat refining, fat production, etc., can solve the problems such as difficult refining of sycamore crude oil, long time-consuming and difficult separation of sycamore oil, achieve good emulsification, shorten heating time, improve The effect of economic value
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Embodiment 1
[0033] The present embodiment provides a co-production method for extracting Jatropha tomentosa oil and phospholipids, comprising the following steps:
[0034] S1. Heating the crude jatropha oil. The jatropha crude oil used in this embodiment is obtained by squeezing the jatropha fruit in a press after microwave treatment and hot air drying. Heat jatropha crude oil to 75°C and add citric acid, the amount of citric acid added is 0.15% of the mass of jatropha crude oil, stir for 50 minutes, continue to add water accounting for 4% of the mass of jatropha crude oil, and hydrate for 10 minutes Centrifuged to obtain gum and degummed oil.
[0035] Carry out crude purification treatment to the colloid obtained above: add ethyl acetate to the colloid, the mixed mass ratio of colloid and ethyl acetate is 1:0.8, obtain phospholipid phase and ethyl acetate-oil mixed phase after extraction for 30min, The ethyl acetate-oil mixed phase was subjected to vacuum distillation at a pressure of 0...
Embodiment 2
[0042] The difference between this example and Example 1 is that in S1, phosphoric acid is added after heating the jatropha crude oil to 80°C. Add 5% water to the crude oil of jatropha, and centrifuge after hydration for 15 minutes. When the isolated colloid was subjected to rough purification, the mass ratio of the colloid to ethyl acetate was 1:1, and the extraction time was 38min. After the extraction, the phospholipid phase and the ethyl acetate-oil mixed phase were respectively placed in The ethyl acetate in the recovery process was distilled under reduced pressure under the environment of 0.1 MPa. In S2, after the colloid is dissolved in absolute ethanol, it is heated in a water bath at 70±1°C, and the mass of activated clay added during decolorization is 2% of the mass of the colloid. In S3, add sodium hydroxide lye, stir, and separate after standing for 8 hours. In S4, the temperature of the deacidified oil was adjusted to 80°C, and the amount of water added for wash...
Embodiment 3
[0044] The difference between this example and Example 1 mainly lies in: in S1, phosphoric acid is added after heating the jatropha crude oil to 85°C, the amount of phosphoric acid added is 0.25% of the mass of jatropha crude oil, after stirring for 30 minutes, continue to add The quality of jatropha crude oil is mixed with 6% water, hydrated for 20 minutes and then centrifuged. When the isolated colloid is subjected to rough purification, the mass ratio of the colloid to ethyl acetate is 1:1.2, and the extraction time is 45min. After the extraction, the phospholipid phase and the ethyl acetate-oil mixed phase are respectively placed in The ethyl acetate in the recovery process was distilled under reduced pressure under the environment of 0.12 MPa. In S2, after the colloid is dissolved in absolute ethanol, it is heated in a water bath at 71±1°C, and the mass of activated clay added during decolorization is 2.2% of the mass of the colloid. In S3, after adding sodium hydroxide ...
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