Method for extracting krill oil with high phosphatide content from Antarctic krills
A technology of Antarctic krill oil and Antarctic krill, applied in the direction of fat oil/fat production, fat production, etc., can solve the problem of high extraction process temperature, large difference between Antarctic krill and lobster components, and the inability to apply Antarctic krill shrimp oil extraction, etc. problem, to achieve the effect of high extraction efficiency and good phospholipid enrichment effect
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Embodiment 1
[0013] (1) Drying: drying the fresh Antarctic krill at 55-75° C. to obtain dry Antarctic krill with a water content (mass percentage) of 8-10%;
[0014] (2) Extraction: Take 6.5 times the weight of dry Antarctic krill and extract dry Antarctic krill 3 times at 25-30°C. After each extraction, filter the dried Antarctic krill; , the extraction rate of phospholipids was 92.0%;
[0015] (3) solvent volatilization: merge 3 extraction solutions, extract solution at temperature 25~55 ℃, evaporate under vacuum tightness-0.06~-0.085Mpa, remove the normal hexane in extraction solution, obtain phospholipid content (mass percentage ) is 32.0% Antarctic krill oil; then nitrogen or carbon dioxide gas is continuously passed through the Antarctic krill oil at normal temperature to remove the residual n-hexane in the shrimp oil, so that the residual amount of n-hexane meets the national standard;
[0016] (4) Enrichment of phospholipids: Add 80% ethanol with the same volume concentration (mas...
Embodiment 2
[0018] (1) Drying: drying the fresh Antarctic krill at 55-75° C. to obtain dry Antarctic krill with a water content (mass percentage) of 8-10%;
[0019] (2) Extraction: Take No. 6 gasoline with 6 times the weight of dry Antarctic krill and extract dry Antarctic krill 4 times at 25-35°C. After each extraction, filter out the dry Antarctic krill; after 4 extractions The extraction rate of phospholipids was 92.2%;
[0020] (3) solvent volatilization: merging 4 times of extracts, the extract is evaporated at temperature 25~55 ℃, under vacuum tightness-0.06~-0.085Mpa, removes No. 6 gasoline in the extract, obtains phospholipid content (mass percent content) is 31.5% Antarctic krill oil; then nitrogen or carbon dioxide gas is continuously passed through the Antarctic krill oil at room temperature to remove the residual No. 6 gasoline in the shrimp oil, so that the residual amount meets the national standard;
[0021] (4) Enrichment of phospholipids: Add 90% (mass percent concentrat...
Embodiment 3
[0023] (1) Drying: drying the fresh Antarctic krill at 55-75° C. to obtain dry Antarctic krill with a water content (mass percentage) of 8-10%;
[0024] (2) Extraction: Take petroleum ether 7 times the weight of dry Antarctic krill and extract dry Antarctic krill three times at 25-35°C. After each extraction, filter the dry Antarctic krill with filter paper; after three extractions , the extraction rate of phospholipids was 91.5%;
[0025] (3) solvent volatilization: merge the extracts for 3 times, evaporate the extract at a temperature of 25~55 ℃, and under the vacuum degree of -0.06~-0.085Mpa, remove the petroleum ether in the extract, and obtain a phospholipid mass percentage of 31.5 % Antarctic krill oil; then continuously pass nitrogen or carbon dioxide gas to the Antarctic krill oil at room temperature to remove the residual petroleum ether in the shrimp oil, so that the residual petroleum ether meets the national standard;
[0026] (4) Enrichment of phospholipids: Add ...
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