Use of isopropyl acetate as leaching solvent in plant oil and fat leaching and oil and fat leaching method using isopropyl acetate
A technology of isopropyl acetate and vegetable oil, applied in the direction of fat oil/fat production, fat production, etc., can solve the problems of insufficient attention to toxicity, large loss of ethanol solvent, large batch impact, etc., and achieve stable supply and quality, and extraction capacity The effect of enhancing and improving the processing ability
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Embodiment 1
[0055] Embodiment 1 (comparative embodiment)
[0056] Soybean is selected as the oil plant, and the vegetable oil extraction solvent is used as the extraction solvent to extract soybean oil. The process is as follows:
[0057] The raw soybeans are cleaned, dried, crushed and peeled, and then heated to 78°C to soften and compact the blanks, the thickness of which is about 0.3mm; the prepared blanks are leached in a rotary extractor with vegetable oil extraction solvent , the solvent and the raw material are contacted by soaking, spraying, mixing and countercurrent. The ratio of leaching solvent to oil is 0.8:1 by weight; the leaching time is 60min; It is 35wt% wet meal. The high-temperature desolventization process is used to desolventize the wet meal, and the residual oil content of the meal is about 0.8wt% after steaming off-line. Pass the mixed oil into the evaporator for evaporation, the outlet solvent gas temperature is 70°C; then re-evaporate the once-evaporated mixed o...
Embodiment 2
[0059] Soybean is selected as the oil plant, and isopropyl acetate is used as the extraction solvent to extract soybean oil. The process is as follows:
[0060] The raw soybeans are cleaned, dried, crushed and peeled, and then heated to 78°C to soften and prick the billet. The thickness of the billet is about 0.3mm; the prepared billet is leached with isopropyl acetate in a rotary extractor , the solvent and the raw material are contacted by soaking, spraying, mixing and countercurrent. The ratio of leaching solvent to oil is 0.8:1 by weight; the leaching time is 60min; It is 30wt% wet meal. The high-temperature desolventization process is used to desolventize the wet meal, and the residual oil content of the meal is about 0.6wt% after steaming off-line. Pass the mixed oil into the evaporator for evaporation, the outlet solvent gas temperature is 88°C; then re-evaporate the once-evaporated mixed oil, the outlet solvent gas temperature is 90°C, and then remove part of the solv...
Embodiment 3
[0062] Peanuts are selected as the oil plant, and isopropyl acetate is used as the extraction solvent to extract peanut oil. The process is as follows:
[0063] The raw peanuts are cleaned, dried, crushed and peeled, and then heated to 74°C to soften and prick the billet. The thickness of the billet is about 0.3mm; Dry the billet at 75°C to a moisture content of 3%; use isopropyl acetate to extract the prepared billet in a horizontal leaching device, and the solvent and the billet are contacted in a countercurrent manner by soaking, spraying, mixing, and the leaching solvent and The oil-to-plant ratio is 0.4:1 by weight; the leaching time is 80 minutes; the temperature is 85°C, and a wet meal with 49% mixed oil and 25% solvent content is obtained. The high-temperature desolventization process is used to desolventize the wet meal, and the residual oil content of the meal is about 0.6wt% after steaming off-line. Pass the mixed oil into the evaporator for evaporation, the outlet...
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