Use of at least one coproduct from the vegetable-oil refining industry for obtaining a purified total unsaponifiable vegetable oil product
A vegetable oil and saponification technology, which is applied in the direction of fat oil/fat refining, anhydride/acid/halide active ingredients, and medical preparations containing active ingredients, etc. Effect
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Embodiment 1
[0150] Composition of Soybean Deodorized Distillate
[0151] The market for oils, more particularly soybean oil and DD, is severely constrained by the global availability of seeds and the growing need to develop vitamin E and phytosterols relevant to food, cosmetic or pharmaceutical applications.
[0152]This need has prompted the oil industry to optimize the deodorization process in order to obtain DD with a composition that is very conducive to the recovery of the unsaponifiable fraction.
[0153] Modifications made to the deodorizing plant were mainly aimed at increasing the deodorizing temperature and installing specific condensers capable of collecting a deodorizing distillate particularly rich in tocopherols and phytosterols.
[0154] It is this quality of DD that will preferably be addressed by the new invention.
[0155] As an example, the composition of a deodorized distillate of soybean is as follows:
[0156]
Embodiment 2
[0158] Distillation of deodorized distillates from soybeans
[0159] In the case of DD with a reduced concentration of unsaponifiables, the process of the invention can advantageously comprise a pretreatment by molecular distillation. It is applied to eliminate a portion of the light fraction of DD, mainly composed of fatty acids, in order to obtain the unsaponifiable-rich feedstock used in the process.
[0160] The test was carried out on a centrifugal molecular still with a maximum capacity of 25 kg / hour. The device consists of the following elements:
[0161] A conical circulating rotor with a diameter of 38 cm,
[0162] A water circulation coil (condenser),
[0163] Two recovery tanks for residue and distillate,
[0164] An induction heating system.
[0165] The vacuum unit consists of a vane pump (low vacuum) and an oil diffusion pump (molecular vacuum).
[0166] The product to be treated is first pumped into a continuous degasser consisting of a thin film, falling ...
Embodiment 3
[0175] Distillation of the deodorized distillate of sunflower
[0176] The test was carried out on the same apparatus as in Example 2.
[0177] The parameters used for this operation are as follows:
[0178] Feeding rate: 18.5kg / h
[0179] Vacuum degree: 10 -2 mmHg
[0180] Distillation temperature: 100°C
[0181] Distillation rate: 82.5%
[0182] Composition of the product:
[0183] Compound in g per 100g
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