Method for refining cosmetic camellia oil by adopting short-path distillation
A short-path distillation, cosmetic-grade technology, applied in the direction of oil/fat refining, fat production, etc., can solve the problems of large loss of camellia oil, secondary pollution, and more oil wasted, and achieve the goal of reducing implementation costs and avoiding secondary pollution. Effect
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Embodiment 1
[0033] (1) Weighing a certain pressed camellia oil crude oil 10Kg, its measurement acid value AV is 8mgKOH / g; This pressed camellia oil crude oil directly enters buffer tank 1 place, is imported into the first stage film evaporator 2 by metering pump Dehydration and degassing are carried out at a temperature of 80°C and a pressure of -0.9Mpa. After dehydration and degassing, the pressed camellia oil continues to enter the next short-path distiller for deacidification and separation.
[0034] (2) The pressed camellia oil after dehydration and degassing is imported into the second-stage short-path distiller 3 through a pump to carry out deacidification and separation. Sour camellia oil.
[0035] (3) The pressed camellia oil after deacidification is pumped into the third-stage short-path distiller 4 for further deacidification and separation. The specific conditions are that the distillation temperature is 180° C. and the pressure is 0.1 Pa for separation.
[0036] The free fat...
Embodiment 2
[0038] (1) Weighing 10Kg of camellia oil crude oil extracted by a certain solvent, its measurement acid value AV is 6mgKOH / g, the camellia oil extracted by this solvent directly enters buffer tank 1, and is imported into the first-stage thin film evaporator by metering pump 2. Carry out dehydration and degassing, specifically at a temperature of 120°C and a pressure of -0.8Mpa. The solvent-extracted camellia oil after dehydration and degassing continues to enter the next short-path distiller for deacidification and separation.
[0039] (2) The solvent-extracted camellia oil after dehydration and degassing is input into the second-stage short-path distiller 3 through a pump to carry out deacidification and separation. Oil.
[0040] (3) The solvent-extracted camellia oil after deacidification is pumped into the third-stage short-path distiller 4 for further deacidification and separation. The specific conditions are that the distillation temperature is 170° C. and the pressure ...
Embodiment 3
[0043](1) Weigh 10Kg of pressed camellia oil from Huiying camellia oil factory in Hengyang, Hunan, and its measured acid value AV is 6.5mgKOH / g, and the camellia oil extracted by this solvent is directly put into buffer tank 1, and is input to the first stage by metering pump The thin film evaporator 2 performs dehydration and degassing, specifically at a temperature of 100°C and a pressure of -0.85Mpa. The solvent-extracted camellia oil after dehydration and degassing continues to enter the next short-path distiller for deacidification and separation.
[0044] (2) The solvent extracted camellia oil after dehydration and degassing is pumped into the second-stage short-path still 3 for deacidification and separation. The specific conditions are that the distillation temperature is 130° C. and the pressure is 5 Pa to separate the deacidification camellia oil .
[0045] (3) The solvent-extracted camellia oil after deacidification is pumped into the third-stage short-path distill...
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