Method for preparing fish oil ethyl ester from fish wastes
A technology for fish waste and fish oil ethyl ester, which is applied in the directions of fatty acid esterification, ester group and hydroxyl reaction preparation, bulk chemical production, etc., can solve the problems of low fish oil yield and purity, etc. The effect of low temperature and high separation efficiency
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Embodiment 1
[0021] a. Raw material processing Select 50kg of fish head from fish processing, and cut into 1×1cm fritters in a shearing machine;
[0022] B, freezing puts the above-mentioned prepared fish head fragments into a liquid nitrogen cold storage for freezing;
[0023] c, pulverization: pulverize the frozen fish head fragments;
[0024] d, once the fish scraps after pulverizing are extracted by using supercritical carbon dioxide (SC-CO2) 2 ) extraction, the control temperature is 40°C, the pressure is 20MPa, CO 2 The flow rate is 1.8kg·h -1 g -1 , the extraction time is 6h to obtain a liquid oil mixture;
[0025] e, under reduced pressure, the liquid oil mixture obtained above is decompressed with CO 2 Under reduced pressure, the oil comes out, and the oil with a purity of 72% is obtained;
[0026] f. Secondary extraction The low-purity oil prepared above was extracted with SC-CO with 10% ethanol 2 Extract to obtain oil with a purity of 90%;
[0027] G, ethyl esterificatio...
Embodiment 2
[0030] a. Raw material processing Select 10 kg of fish offal from fish processing and cut them into small pieces of 1 × 1 cm in a special shearing machine;
[0031] B, freezing puts the above-mentioned prepared fish viscera pieces into a liquid nitrogen cold storage for freezing;
[0032] c, pulverize the frozen fish viscera fragments to pulverize;
[0033] d, once extracted the pulverized fish skin with supercritical carbon dioxide (SC-CO2) 2 ) extraction, the control temperature is 25°C, the pressure is 13MPa, CO 2 The flow rate is 1.5kg·h -1 g -1 , and the extraction time was 4 hours to obtain a liquid oil mixture;
[0034] e, under reduced pressure, the liquid oil mixture obtained above is decompressed with CO 2 Under reduced pressure, the oil comes out, and the oil with a purity of 69% is obtained;
[0035] f. Secondary extraction The low-purity oil prepared above was extracted with SC-CO with 5% ethanol 2 Extract to get 86% oil;
[0036] g, ethyl esterification: ...
Embodiment 3
[0039] a, raw material processing selects 100kg of fish skin leftovers from fish processing, and cuts them into 2×2cm fritters in a shearing machine;
[0040] B, freezing puts the fish skin fragment of above-mentioned preparation into liquid nitrogen cold storage and carries out freezing treatment;
[0041] c, pulverize and pulverize the frozen fish skin fragments;
[0042]d, once extracted the pulverized fish skin with supercritical carbon dioxide (SC-CO2) 2 ) extraction, the control temperature is 55°C, the pressure is 40MPa, CO 2 The flow rate is 2.0kg·h -1 g -1 , the extraction time is 10h to obtain a liquid oil mixture;
[0043] e, under reduced pressure, the liquid oil mixture obtained above is decompressed with CO 2 Decompression, the oil is separated out, and the oil with a purity of 78% is obtained;
[0044] f. Secondary extraction The low-purity oil prepared above was extracted with SC-CO with 20% ethanol 2 Extract to get 95% oil;
[0045] g. Ethylization tre...
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