Method for reducing trans fatty acid content in vegetable oil grease by two-stage type deodorization tower
A technology of trans fatty acid and vegetable oil, which is applied in the direction of fat oil/fat refining and fat production, can solve the problems of reducing the content of trans fatty acid, reducing the heating time, and high content of trans fatty acid, so as to reduce the content of trans fatty acid and reduce The effect of high temperature heating time
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specific Embodiment approach 1
[0015] Specific implementation mode one: the steps of this implementation mode are as follows:
[0016] Step 1: Take a certain amount of decolorized soybean oil and refined oil respectively, and measure the content of trans fatty acid; the decolorized soybean oil enters the double-helix heat exchanger, and the temperature is respectively increased to 170°C, 180°C, 190°C, 200°C, 210°C °C, enter the upper plate tower, enter the lower plate tower after preliminary deodorization, fix the deodorization conditions of the lower plate tower, measure the content of trans fatty acids in the refined oil, and determine the deodorization temperature of the upper stage.
[0017] Step 2: In the upper plate tower, use direct steam with a steam volume of 0.1%, 0.2%, 0.3%, 0.4%, and 0.5% respectively to carry out upper-stage stripping, and enter the lower plate tower after preliminary deodorization, and fix the deodorization of the lower plate tower. Conditions, measure the content of trans fat...
specific Embodiment approach 2
[0023] Embodiment 2: This embodiment differs from Embodiment 1 in that the deodorization temperature is controlled at 170° C. to 200° C. in Step 1, and other components and steps are the same as Embodiment 1.
specific Embodiment approach 3
[0024] Embodiment 3: The difference between this embodiment and Embodiment 1 is that in Step 1, the deodorization temperature of the upper stage is controlled at 170° C. to 180° C., and other components and steps are the same as Embodiment 1.
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