Study on gas-liquid flow characteristics in stirred tank with dual- impeller based on CFD-PBM coupled model

Author(s):  
Songsong Wang ◽  
Deyu Luan ◽  
Ying Zhang ◽  
Longbin Li ◽  
Zhaorui Wang ◽  
...  
2018 ◽  
Vol 170 ◽  
pp. 13-23 ◽  
Author(s):  
Wen-Ling Li ◽  
Yi Ouyang ◽  
Xue-Ying Gao ◽  
Chen-Yu Wang ◽  
Lei Shao ◽  
...  

2005 ◽  
Vol 2005.58 (0) ◽  
pp. 381-382
Author(s):  
Akimaro KAWAHARA ◽  
Kazuyuki KUMAGAE ◽  
Fujitaka MORI ◽  
Michio SADATOMI

Author(s):  
Dmitry Vladimirovich Gradov ◽  
Arto Laari ◽  
Ilkka Turunen ◽  
Tuomas Koiranen

Abstract Hydrodynamics of gas-liquid flow in a round-bottom stirred tank is modelled at two gas flow rates, constant bubble size and agitator speed of 300 rpm. A round-bottom tank equipped with four baffles and a Rushton turbine was chosen to represent a typical reactor used in hydrometallurgical processes operating under pressure. The applicability of different momentum interchange models and the Realizable k-ε, SST k-ω, and RSM turbulence models was studied using CFD software. The results were compared and validated against experimental data from Particle Image Velocimetry measurements by means of liquid and gas velocity distributions. In addition, energy balance between power input and dissipation energy was compared for the different turbulence models. The CFD model was found to be in good agreement with the measurements. Of the turbulence models studied, the Realizable k-ε model showed best agreement with the measured velocity profiles. Popular drag force models proposed in the literature were assessed, as was the influence of inclusion of non-drag forces. Gas flow was found to affect the liquid phase flow in the tank by generating an additional secondary circulation loop in the upper part of the reactor.


2009 ◽  
Vol 32 (8) ◽  
pp. 1266-1273 ◽  
Author(s):  
Y.-H. Zhang ◽  
Y.-M. Yong ◽  
Z.-S. Mao ◽  
C. Yang ◽  
H.-Y. Sun ◽  
...  

Energies ◽  
2019 ◽  
Vol 12 (24) ◽  
pp. 4653 ◽  
Author(s):  
Ryan Anugrah Putra ◽  
Martin Neumann-Kipping ◽  
Thomas Schäfer ◽  
Dirk Lucas

The gas–liquid flow characteristics for blade, single, and the double-helical swirl elements were numerically investigated and compared in this work. The Euler–Euler model assuming bi-modal bubble size distributions was used. The experiment, conducted in a vertical pipe equipped with a static blade swirl element, was used as the basis for the computational fluid dynamics (CFD) simulations. In the experiment, high-resolution gamma-ray computed tomography (HireCT) was used to measure the gas volume fractions at several planes within the blade swirl element. The resulting calculated profiles of the pressure, liquid and gas velocities as well as the gas fraction showed a large influence of the swirl elements’ geometry. The evolution and characteristics of the calculated gas–liquid phase distributions in different measurement planes were found to be unique for each type of swirl element. A single gas core in the center of the pipe was observed from the simulation of the blade element, while multiple cores were observed from the simulations of the single and double helix elements. The cross-sectional gas distribution downstream of the single and double helical elements changed drastically within a relatively short distance downstream of the elements. In contrast, the single gas core downstream of the blade element was more stable.


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