Two-Phase Swirling Flow in a Gas-Liquid Separator
Hironobu KATAOKA, Akio Tomiyama, Shigeo Hosokawa, Akira Sou, Masao Chaki
Abstract
Open-access reader
Hironobu KATAOKA, Akio Tomiyama, Shigeo Hosokawa, Akira Sou, Masao Chaki
Abstract
Open-access reader
Air-water swirling flows in a one-fifth model of a steam separator in a boiling water nuclear reactor are measured to obtain a database for modeling and verification of numerical methods for predicting swirling flows in the separator. Flow patterns, liquid film thicknesses, separated flow rates and the ratio Ws* of the separated flow to the total liquid flow are measured using a high-speed camera, a laser focus displacement meter and flowmeters. Main conclusions obtained are as follows: (1) liquid transfer from droplets to liquid film is caused not only by droplet deposition but also by the collection of droplets on the vanes of the swirler, (2) Ws* increases with the gas volume flux JG and does not depend on the liquid volume flux JL so much because a large centrifugal force caused by the swirler makes most of droplets in the gas core deposit on the liquid film before the separation and (3) a local peak appears in the axial distribution of film thickness, the position of which corresponds to the location where the droplet deposition caused by the centrifugal force has completed.
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Air-water swirling flows in a one-fifth model of a steam separator in a boiling water nuclear reactor are measured to obtain a database for modeling and verification of numerical methods for predicting swirling flows in the separator. Flow patterns, liquid film thicknesses, separated flow rates and the ratio Ws* of the separated flow to the total liquid flow are measured using a high-speed camera, a laser focus displacement meter and flowmeters. Main conclusions obtained are as follows: (1) liquid transfer from droplets to liquid film is caused not only by droplet deposition but also by the collection of droplets on the vanes of the swirler, (2) Ws* increases with the gas volume flux JG and does not depend on the liquid volume flux JL so much because a large centrifugal force caused by the swirler makes most of droplets in the gas core deposit on the liquid film before the separation and (3) a local peak appears in the axial distribution of film thickness, the position of which corresponds to the location where the droplet deposition caused by the centrifugal force has completed.
Key concepts: Separator (oil production), Materials science, Mechanics, Two-phase flow, Centrifugal force, Multiphase flow, Boiling, Bubble