Calculation method of liquid-liquid flow field in sieve tray extraction tower using low Reynolds number turbulent flow model
A turbulence model and low Reynolds number technology, applied in calculation, design optimization/simulation, electrical digital data processing, etc., can solve problems such as high flow velocity and unfavorable two-phase contact mass transfer
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[0082] like Figure 1-6 As shown in one of them, the invention discloses a method for calculating the liquid-liquid flow field of a sieve plate extraction tower using a low Reynolds number turbulence model, which includes the following steps:
[0083] Step S1: Determine the physical model of the sieve tray extraction tower, including the geometric structure of the physical model, the composition of the continuous phase and the dispersed phase and the calculation area; as a preferred embodiment, the calculation area of the sieve tray extraction tower in the step S1 is the two-dimensional section of the extraction area of the sieve extraction tower;
[0084] In this embodiment, dilute acetic acid solution is used as the continuous phase, sec-butyl acetate is used as the dispersed phase, and the continuous phase flows in from the top of the tower as the heavy phase. to the next tray. The light phase, as the dispersed phase, enters from the bottom of the tower, disperses int...
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