부상분리방식(Flotating Separation Type)을 이용한 기포 거동에 대한 유동특성에 관한 연구
A Study on Flow Characteristics of Bubble Behavior using Flotating Separation Type
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초록
An important variable in the oil-water separation process is the size and dispersion diagram of the bubbles formed in the induced gas flotation(IGF). In this study, the influence of the behavior and characteristics of the fine bubbles generated in the IGF device on the oil-water separation performance was evaluated by a numerical analysis method. For this reason, it constitutes Grid system suitable for bubble characteristic analysis. By applying Reynolds-averaged Navier-Stokes equations, a continuous abnormal flow analysis model of water and air was established. For the numerical flow analysis model, we applied the Eulerian-Eulerian approach that can be used for the reaction model in which bubbles are formed at one point of the Euler method applied when the base is liquid. As a result, it was confirmed that the bubbles in the IGF device were evenly dispersed as the flow velocity of bubbles increased and the particle size decreased. Such a phenomenon was caused by changes in Reynolds number and drag related to the flow characteristics, and could be explained by Stokes' law of viscosity.
Abstract
An important variable in the oil-water separation process is the size and dispersion diagram of the bubbles formed in the induced gas flotation(IGF). In this study, the influence of the behavior and characteristics of the fine bubbles generated in the IGF device on the oil-water separation performance was evaluated by a numerical analysis method. For this reason, it constitutes Grid system suitable for bubble characteristic analysis. By applying Reynolds-averaged Navier-Stokes equations, a continuous abnormal flow analysis model of water and air was established. For the numerical flow analysis model, we applied the Eulerian-Eulerian approach that can be used for the reaction model in which bubbles are formed at one point of the Euler method applied when the base is liquid. As a result, it was confirmed that the bubbles in the IGF device were evenly dispersed as the flow velocity of bubbles increased and the particle size decreased. Such a phenomenon was caused by changes in Reynolds number and drag related to the flow characteristics, and could be explained by Stokes' law of viscosity.
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