Method of refining OMEGA3 unsaturated fatty acid from fur seal oil
A technology of unsaturated fatty acids and seal oil, applied in the field of medicine, can solve the problems of increased steps and costs, cumbersome crude oil of seal oil, residue of organic solvents in seal oil, etc., and achieve the effect of reducing the probability of residue, low cost and simple steps
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Embodiment 1
[0031] Equipment: German VTA short-range molecular distillation apparatus is adopted, with a distillation area of 0.4m 2 .
[0032] Raw material: seal oil crude oil 50 kg.
[0033] Conditions: two-stage vacuum distillation is adopted, the pressure of the first pole molecular still is 10Pa; the pressure of the second pole molecular still is 0.01-0.3Pa; the feed rate is 10 kg / hour; the evaporation temperature of the first pole is 140°C , the evaporation temperature of the second pole is 300°C; the rotational speed of the wiped film rotor of the first pole is 100 rpm, and the rotational speed of the wiped film rotor of the second pole is 250 rpm.
[0034] operate:
[0035] 1 Routine inspection before starting the instrument
[0036] Before each molecular distillation experiment, the following items need to be checked routinely:
[0037] 1.1 Check whether the cooling and heating circuits are connected smoothly
[0038] 1.2 Check whether there is pump oil in the vacuum pump,...
Embodiment 2
[0068] Method is with embodiment 1.
[0069] The conditions are: the pressure of the first pole molecular still is 5Pa, the pressure of the second pole still is 0.1~0.3Pa; the feed rate is 8kg / h; the evaporation temperature of the first pole is 140°C, and the evaporation temperature of the second pole is The temperature is 300° C.; the rotation speed of the first pole wiped film rotor is 100 rpm, and the second pole wiped film rotor speed is 250 rpm.
[0070] After 6.25 hours, 21.7 kg of heavy fraction was obtained.
[0071] Through content determination, the content of eicosapentaenoic acid (EPA), docosahexaenoic acid (DHA) and docosapentaenoic acid (DPA) in the prepared OMEGA3 unsaturated fatty acid is 30%-40% .
Embodiment 3
[0073] Method is with embodiment 1.
[0074] The conditions are: the pressure of the first pole molecular still is 1Pa, the pressure of the second pole still is 0.05~0.1Pa; the feed rate is 5kg / h; the evaporation temperature of the first pole is 140°C, and the evaporation temperature of the second pole is The temperature is 300° C.; the rotation speed of the first pole wiped film rotor is 100 rpm, and the second pole wiped film rotor speed is 250 rpm.
[0075] After 10 hours, 16.1 kg of heavy component was obtained
[0076] Through content determination, the content of eicosapentaenoic acid (EPA), docosahexaenoic acid (DHA) and docosapentaenoic acid (DPA) in the prepared OMEGA3 unsaturated fatty acid is 40%-50% .
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