A Study of Turbulence Properties of Continuous Phase in Gas–Liquid Flow in a Stirred Tank
スポンサーリンク
概要
- 論文の詳細を見る
Two-dimensional particle image velocimetry (PIV) and digital image analysis are used to quantify the hydrodynamics of gas–liquid flow in a cubic tank with a flat square base (length T=230 mm). The fluid is stirred by a half elliptical disk turbine (HEDT) of diameter D=77 mm. Flow fields at 8 different gas holdups from 2.24 to 5.78% are investigated. The gas is injected into the tank through a syringe needle. The measurements are taken in a plane which is 2 mm from the wall and the radial velocity could be ignored compared to the axial and tangential velocity. Therefore, the flow field is considered to be two-dimensional. The results show that the liquid mean velocity and turbulent kinetic energy (TKE) decrease with an increase in gas holdup, and the turbulent kinetic energy dissipation first increases, then decreases with an increase in gas holdup.
著者
-
Gao Zhengming
College Of Chemical Engineering Beijing University Of Chemical Technology
-
Huang Xiongbin
College Of Chemical Engineering Beijing University Of Chemical Technology
-
Geng Xuan
College of Chemical Engineering, Beijing University of Chemical Technology
-
Song Haixia
College of Chemical Engineering, Beijing University of Chemical Technology
-
Song Haixia
College Of Chemical Engineering Beijing University Of Chemical Technology
-
Geng Xuan
College Of Chemical Engineering Beijing University Of Chemical Technology
関連論文
- Large Eddy Simulation of Flow Fields in Vessels Stirred by Dual Rushton Impeller Agitators
- Experimental and CFD Studies of a Fluid Flow in a Draft-Tube Stirred Tank
- Effect of Temperature and Suspended Solids on Local Void Fraction in a Sparged Reactor with a Multi-Impeller Agitator
- Turbulence Properties of Solid-Liquid Flow in the Near-Wall Region of a Stirred Tank
- A Study of Turbulence Properties of Continuous Phase in Gas–Liquid Flow in a Stirred Tank
- A Study of Turbulence Properties of Continuous Phase in Gas-Liquid Flow in a Stirred Tank