Method for producing peanut oil
A production method and technology of peanut oil, applied in the direction of fat oil/fat production, fat production, fat oil/fat refining, etc., can solve the problems of complex safety hazards in the production process, excessive residue oil, unhygienic products, etc., and achieve supercritical Carbon dioxide extraction, improving the purity and oil yield, and protecting the effect of active ingredients
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Embodiment 1
[0032] The present invention provides a method for producing peanut oil, including the following steps:
[0033] S1. Dehulled peanut kernels with a moisture content of 7.8% are sent to a screw oil press for pressing. The pressing temperature is 43°C, the number of pressing times is 4, and the rotation speed of the screw press shaft is 36r / min to obtain peanuts. Crude oil A and peanut residue;
[0034] S2. Add ethanol to the peanut residue obtained in S1. The amount of ethanol used is 0.6 times the weight of the peanut residue. After stirring for 28 minutes, supercritical carbon dioxide extraction is carried out. The extraction pressure of supercritical carbon dioxide extraction is 29Mpa and the extraction temperature is 51. ℃, extraction time is 65 minutes, carbon dioxide flow rate is 26L / h, peanut crude oil B is obtained;
[0035] S3. Mix the peanut crude oil A obtained in S1 and the peanut crude oil B obtained in S2 to obtain a mixed crude oil. Add an adsorbent to the mixed crude ...
Embodiment 2
[0037] The present invention provides a method for producing peanut oil, including the following steps:
[0038] S1. Dehulled peanut kernels with 8.7% moisture content are sent to a screw oil press for pressing. The pressing temperature is 52°C, the number of pressing times is 5, and the speed of the screw press shaft is 38r / min to obtain peanuts. Crude oil A and peanut residue;
[0039] S2. Add ethanol to the peanut residue obtained in S1. The amount of ethanol used is 0.5 times the weight of the peanut residue. After stirring for 21 minutes, perform supercritical carbon dioxide extraction. The extraction pressure of supercritical carbon dioxide extraction is 30Mpa and the extraction temperature is 49. ℃, extraction time is 53 minutes, carbon dioxide flow rate is 24L / h, the supercritical carbon dioxide extractor used has two separation vessels, the pressure of the first separation vessel is 7.2Mpa, the temperature is 40℃, and the pressure of the second separation vessel is 4.6Mpa...
Embodiment 3
[0042] The present invention provides a method for producing peanut oil, including the following steps:
[0043] S1. Dehulled peanut kernels with a moisture content of 7.4% are sent to a screw oil press for pressing. The pressing temperature is 58°C, the number of pressing is 6 times, and the rotation speed of the screw press shaft is 32r / min to obtain peanuts. Crude oil A and peanut residue;
[0044] S2. Add ethanol to the peanut residue obtained in S1. The amount of ethanol used is 0.8 times the weight of the peanut residue. After stirring for 26 minutes, supercritical carbon dioxide extraction is performed. The extraction pressure of supercritical carbon dioxide extraction is 29Mpa and the extraction temperature is 53. ℃, the extraction time is 72 minutes, the carbon dioxide flow rate is 28L / h, the supercritical carbon dioxide extractor used has two separation vessels, the pressure of the first separation vessel is 8.7Mpa, the temperature is 39℃, and the pressure of the second s...
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