Method for calculating sieve plate extraction tower liquid flow field by using low Reynolds number turbulence model

A technology of turbulent flow model and low Reynolds number, applied in calculation, electrical digital data processing, design optimization/simulation, etc., can solve problems such as unfavorable two-phase contact mass transfer and high flow velocity

Inactive Publication Date: 2017-05-17
FUZHOU UNIV
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Problems solved by technology

The simulation results show that in the traditional sieve tray extraction tower, the flow velocity of the continuous phase in the local area of ​​the tray is too high, which will cause the continuous phase to form a reflux zone between the two trays, which is extremely unfavorable for the contact mass transfer of the two phases

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  • Method for calculating sieve plate extraction tower liquid flow field by using low Reynolds number turbulence model
  • Method for calculating sieve plate extraction tower liquid flow field by using low Reynolds number turbulence model
  • Method for calculating sieve plate extraction tower liquid flow field by using low Reynolds number turbulence model

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[0082] Such as 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 sieve tray extraction tower in the step S1, the calculation area 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 into...

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Abstract

The invention discloses a method for calculating a sieve plate extraction tower liquid flow field by using a low Reynolds number turbulence model. The method includes the following steps: (1) determining a sieve plate extraction tower physical model; (2) establishing a sieve plate extraction tower three-dimensional calculation Euler-Euler two-phase flow model; (3) using the low Reynolds number turbulence model to seal a Navier-Stokes equation (N-S equation); (4) determining a boundary condition and an initial condition for solving the three-dimensional calculation Euler-Euler two-phase flow model; (5) performing discretization on a fluid mechanics basic equation in a computational domain; and (6) solving a mass conservation equation and a momentum conservation equation, and acquiring flow field data of each grid unit in the sieve plate extraction tower; and (7) measuring an actual flow field of the extraction tower by using a particle imaging velocity measurement technique, performing adjustment and feedback according to the measured data, and finally determining a practical model. The model method for precisely calculating the sieve plate extraction tower liquid flow field is implemented, and reliable fluid mechanics information for an actual design of the sieve plate extraction tower.

Description

technical field [0001] The invention relates to a method for calculating the liquid-liquid flow field of a sieve plate extraction tower by using a low Reynolds number turbulent flow model. Background technique [0002] In the sieve plate extraction tower, due to the function of the sieve plate, the axial back mixing is reduced, and at the same time, due to the multiple dispersion and coalescence of the dispersed phase, the surface of the droplet is constantly updated, so that the efficiency of the sieve plate extraction tower is higher than that of the packed tower. In addition, the sieve plate extraction tower has the advantages of simple structure, low price, large processing capacity, and can handle corrosive liquids, so it is widely used in many extraction processes, especially in aromatics extraction, lubricating oil refining, anthraquinone and It plays an important role in the process of hydrogen peroxide preparation and so on. The design of energy-saving and high-eff...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): G06F17/50
CPCG06F30/20
Inventor 黄智贤周元杨臣邱挺叶长燊王晓达王红星李玲杨金杯
Owner FUZHOU UNIV
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