Numerical simulation of mixing in a jet agitated horizontal cylindrical tank

2006 ◽  
Vol 20 (2) ◽  
pp. 127-136 ◽  
Author(s):  
Habib D. Zughbi
Author(s):  
Fre´de´ric Savreux ◽  
Pascal Jay ◽  
Albert Magnin ◽  
Jean-Michel Piau

The laminar isothermal mixing of a viscoplastic fluid is considered in the absence of any free surface and when the material can be modelled using a Bingham constitutive equation. The material is mixed by a rotating cylindrical tank and a fixed anchor impeller. A two-dimensional numerical simulation is performed with a finite elements method. The effects of viscoplasticity and inertia are related to an Oldroyd (Od) and to a Reynolds (Re) number. Stream lines, vortices, yield surfaces and power consumption are shown and analysed depending on the value of Od and Re parameters.


2016 ◽  
Vol 2016 (0) ◽  
pp. 0207
Author(s):  
Tomomi UCHIYAMA ◽  
Isao AOZASA ◽  
Akira ISHIKAWA ◽  
Kouji MOTOYAMA

2018 ◽  
Vol 06 (03) ◽  
pp. 38-52
Author(s):  
Tomohiro Degawa ◽  
Tomomi Uchiyama ◽  
Isao Aozasa ◽  
Akira Ishikawa ◽  
Koji Motoyama

2011 ◽  
Vol 354-355 ◽  
pp. 589-593 ◽  
Author(s):  
Song Ying Chen ◽  
Fu Chao Xie ◽  
Jun Jie Mao

Side-entering agitators are the main mixing system in the process of petroleum blending. Based on the three-dimensional gasoline components mixing model, the incompressible Reynolds equation is selected as the momentum equation and the algorithm of SIMPLE is employed to simulate the flow field of three side-entering agitators. In the unsteady multiphase flow, moving mesh and the standard k-ε turbulent model has been employed to get the mixing time. The results show that the model of side-entering agitators exists low-velocity zones, which are like structures of vortex in the central regions of blending tank, and the mixing time is 33.7s.


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