scholarly journals Sparse identification of multiphase turbulence closures for coupled fluid–particle flows – CORRIGENDUM

2021 ◽  
Vol 920 ◽  
Author(s):  
S. Beetham ◽  
R.O. Fox ◽  
J. Capecelatro
2008 ◽  
Vol 227 (4) ◽  
pp. 2514-2539 ◽  
Author(s):  
O. Desjardins ◽  
R.O. Fox ◽  
P. Villedieu

2006 ◽  
Vol 44 (1) ◽  
pp. 70-78 ◽  
Author(s):  
Nikolai Lukerchenko ◽  
Zdenek Chara ◽  
Pavel Vlasak

Author(s):  
Sijun Zhang ◽  
Madhaveswer Gentela

In this paper, a macro particle method is developed to model the fluid-particle flows. The macro particle is formed by a collection of micro-sized particle so that the number of macro particle to be tracked is much less than the number of smaller particle. Unlike the calculations of instantaneous point variables of fluid phase with moving discrete boundaries of the smaller particles with direct numerical simulation, the boundary of each macro particle is just dealt with the blocked-off approach. On the other hand, the flow fields based on the present method is solved by original Navier-Stokes, rather than the modified ones based on the locally averaged theorem. The flow fields are solved on the length scale of computational cell, while the resolutions of solid particles are the size of macro particle, which is determined as needed in specific applications. The macro particle method is validated by several cases, which demonstrate the macro particle method could accurately resolve fluid-particle systems in an efficient, robust and flexible fashion.


2009 ◽  
Vol 188 (3) ◽  
pp. 195-205 ◽  
Author(s):  
C.R. Duarte ◽  
M. Olazar ◽  
V.V. Murata ◽  
M.A.S. Barrozo

1987 ◽  
Vol 109 (3) ◽  
pp. 324-331
Author(s):  
R. C. Givler ◽  
R. R. Mikatarian

In order to understand how a particulate plug may evolve within the flow of an essentially homogeneous suspension, we have developed a fluid-particle flow model. This theoretical model is based upon a monodisperse collection of rigid, spherical particles suspended in an incompressible, Newtonian liquid. Balance equations of mass and momentum are given for each phase within the context of a continuum mixture theory. The interactions between the phases are dominated by interfacial drag forces and unequilibrated pressure forces. The pressure associated with the solid particles is given by a phenomenological model based upon the flow dynamics. Of primary concern is the calculation of solid particle concentrations within a flow field to indicate the initiation of a particulate plug.


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