Method for supercritical extraction of linolenic acid
A linolenic acid, supercritical technology, applied in the direction of fatty acid production, fatty acid preparation/refining, etc., can solve the problems of linolenic acid product purity needs to be improved, extraction rate needs to be further improved, and extraction temperature is high, so as to regulate human physiological functions and improve human body Physiological functions, the effect of improving the extraction rate
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Embodiment 1
[0027] Take linseed oil and liquid CO 2 , linseed oil and liquid CO 2 The mass mixing ratio of the mixture is 1:1.8, injected into the extraction reaction kettle with a preheating temperature of 40°C, adding the above-mentioned magnetic steel balls whose mass is 10% of the total mass and whose diameter is 0.5mm, and the pressure of the extraction reaction kettle is adjusted to be 1.82× 10 7 Pa, under the condition of sufficient stirring, extract for 30 minutes to obtain the extraction product 1. The obtained extraction product 1 is injected into the separator for separation, and the CO 2 The extracted product 2 was obtained. The obtained extraction product 2 was injected into a horizontal vacuum rectification device, separated and purified at normal temperature and 90kPa to obtain linolenic acid with a purity of 95.8%. The extraction rate of linolenic acid is 89%.
Embodiment 2
[0029] Take linseed oil and liquid CO 2 , linseed oil and liquid CO 2 The mass mixing ratio of the mixture is 1: 2.2, injected into the extraction reactor whose preheating temperature is 35°C, adding the above-mentioned magnetic steel balls with a mass of 9% of the total mass and a diameter of 0.5mm, and adjusting the pressure of the extraction reactor to be 1.82×10 7 Pa, under the condition of sufficient stirring, extract for 30 minutes to obtain the extraction product 1. The obtained extraction product 1 is injected into the separator for separation, and the CO 2 The extracted product 2 was obtained. The obtained extraction product 2 was injected into a horizontal vacuum rectification device, separated and purified at normal temperature and 50kPa, and a linolenic acid product with a purity of 97.3% was obtained. The extraction rate of linolenic acid is 92%.
Embodiment 3
[0031] Take linseed oil and liquid CO2, linseed oil and liquid CO 2 The mass mixing ratio of the mixture is 1:2.2, injected into the extraction reactor whose preheating temperature is 38°C, adding the above-mentioned magnetic steel balls whose mass is 10% of the total mass and whose diameter is 0.5mm, and the pressure of the extraction reactor is adjusted to be 1.80×10 7 Pa, under the condition of sufficient stirring, the extraction time is 30 minutes, and the extraction product 1 is obtained. The obtained extraction product 1 is injected into the separator for separation, and the CO 2 The extracted product 2 was obtained. The obtained extraction product 2 was injected into a horizontal vacuum rectification device, separated and purified at normal temperature and 30kPa to obtain a linolenic acid product with a purity of 98.6%. The extraction rate of linolenic acid is 93%.
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