Use of leaching solvent in preparing edible fat and oil
An edible oil and solvent technology, which is applied in the field of leaching solvents in the preparation of edible oil, can solve the problems of high production cost, large amount of steam required for heating, and large amount of cooling water circulation, and achieve less heating steam and less time. Evaporation latent heat and boiling point are low, and the effect of cooling circulating water is reduced
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Embodiment 1
[0035] Embodiment 1: on 30 tons / day pre-pressed rapeseed cake leaching production line, adopt solvent of the present invention, in leaching process, be used for leaching the grease in the rapeseed cake;
[0036] Described solvent is made up of following components by weight ratio:
[0037] (1) Isohexane: 97%, consisting of 2,2-dimethylbutane, 2,3-dimethylbutane, 2-methylpentane, 3-methylpentane; each accounts for solvent weight Proportion:
[0038] 2,2-Dimethylbutane: 4.6%
[0039] 2,3-Dimethylbutane: 12.4%
[0040] 2-Methylpentane: 51.5%
[0041] 3-Methylpentane: 28.5%
[0042] (2) n-hexane: 2%;
[0043] (3) Others: 1%, including butane and pentane,
[0044] Carry out leaching oil production with solvent of the present invention, successive steps are:
[0045] 1) leaching, the pre-pressed rapeseed cake is extracted with the solvent of the present invention, the rapeseed cake is soaked with 7% water content, 18% oil content, micro-negative pressure (vacuum degree is les...
Embodiment 2
[0052] Embodiment 2: On the 30 tons / day puffed rice bran extraction production line, adopt described solvent to be made up of the following components by weight ratio:
[0053](1) Isohexane: 94%, composed of 2,2-dimethylbutane, 2,3-dimethylbutane, 2-methylpentane, 3-methylpentane; (2) normal Hexane: 3%; (3) Others: 3%, including butane and pentane, used to extract the oil in it.
[0054] 1) Leaching, the pretreated puffed rice bran is extracted with the solvent of the present invention, the water content of the impregnation material is 6%, the oil content of the impregnation material is 16%, and the operating temperature of leaching under slight negative pressure (vacuum degree is less than 0.03MPa): 48 °C, mass ratio of material to solvent: 1:0.8, to obtain leaching wet meal with a concentration of 16% concentrated mixed oil and a water and volatile matter content of 25-30%;
[0055] 2) Evaporating, steaming the leached wet meal, that is, desolvation, steaming, dehydration a...
Embodiment 3
[0061] Example 3: On a 30 t / day puffed rice bran extraction production line, the solvent of the present invention is used for extraction to produce oil, and the same solvent as in Example 1 is used to extract the oil therein.
[0062] The steps in turn are:
[0063] 1) Leaching, the pretreated puffed rice bran meal is extracted with the solvent of the present invention, the water content of the impregnated material is 5%, the impregnated material contains 15% oil, and the operating temperature of the leaching is slightly negative pressure (vacuum degree is less than 0.03MPa): 48°C, mass ratio of material to solvent: 1:0.8, to obtain leaching wet meal with a concentration of 16% concentrated mixed oil and a water and volatile matter content of 25-30%;
[0064] 2) Evaporating, steaming the leached wet meal, that is, desolvation, steaming, dehydration and cooling, to obtain the finished meal, the temperature of the meal is 105 ° C, and the moisture and volatile matter of the meal...
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