Alkaline refining deacidification method for cottonseed mixed oil
A technology of alkali refining deacidification and mixed oil, which is applied in the direction of fat oil/fat refining and fat production, which can solve the problems of high production equipment requirements, low oil refining rate, and many supporting equipment, so as to avoid saponification loss and operating cost The effect of low and process simplification
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Embodiment 1
[0027] The concrete steps of the alkali refining deacidification method of the cottonseed mixed oil of the present embodiment are as follows:
[0028] (1) Add the dilute NaOH solution with a mass percentage concentration of 1% into the neutralization reaction tank 3, and the addition amount is 60% of the volume of the neutralization reaction tank.
[0029] (2) Take 200 kg of mixed oil of cottonseed to be treated, the mass concentration of the mixed oil is 21%, and the acid value is 5.6 (measured according to the method described in GB / T 5530-2005 Determination of acid value and acidity of animal and vegetable oils and fats); The oil is first heated to a temperature of 50°C by the heater 1, and then pumped into the porous oil droplet distribution plate 2 at the conical bottom of the neutralization reaction tank 3, where it is distributed into oil droplets with a diameter of 1-2 mm.
[0030] (3) The oil droplets formed in step (2) enter the dilute NaOH solution in the neutraliza...
Embodiment 2
[0033] The concrete steps of the alkali refining deacidification method of the cottonseed mixed oil of the present embodiment are as follows:
[0034] (1) Add the dilute NaOH solution with a mass percentage concentration of 3% into the neutralization reaction tank 3, and the addition amount is
[0035] Neutralize 50% of the volume of the reaction tank.
[0036] (2) Take 200 kg of cottonseed mixed oil to be processed (same as above), heat it to a temperature of 60°C through the heater 1, and then pump it into the neutralization reaction tank 3, the porous oil drop distribution plate 2 at the conical bottom of the tank, and Distributed into oil droplets with a diameter of 1~2mm.
[0037] (3) The oil droplets formed in step (2) enter the dilute NaOH solution in the neutralization reaction tank 3 to undergo a neutralization reaction, and the deacidified oil and fat obtained from the reaction are separated from the dilute NaOH solution, and rise to the top layer of the dilute NaOH...
Embodiment 3
[0040] The concrete steps of the alkali refining deacidification method of the cottonseed mixed oil of the present embodiment are as follows:
[0041] (1) Add the dilute NaOH solution with a mass percentage concentration of 4% into the neutralization reaction tank 3, and the addition amount is 55% of the volume of the neutralization reaction tank.
[0042] (2) Take 200 kg of cottonseed mixed oil to be processed (same as above), firstly heat it to a temperature of 70°C through the heater 1, and then pump it into the neutralization reaction tank 3, the porous oil droplet distribution plate 2 at the cone mouth of the conical tank bottom, and Distributed into oil droplets with a diameter of 1~2mm.
[0043] (3) The oil droplets formed in step (2) enter the dilute NaOH solution in the neutralization reaction tank 3 to undergo a neutralization reaction, and the deacidified oil and fat obtained from the reaction are separated from the dilute NaOH solution, and rise to the top layer of...
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Abstract
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