Extension of Hill–Koch–Ladd drag correlation over all ranges of Reynolds
number and solids volume fraction
Sofiane Benyahia
a,
⁎
, Madhava Syamlal
b,1
, Thomas J. O'Brien
b,1
a
Fluent Incorporated, 3647 Collins Ferry Road, Suite A, Morgantown, WV 26505, United States
b
US Department of Energy, MS-N04, 3610, Collins Ferry Road, Morgantown, WV 26505, United States
Received 27 April 2005; received in revised form 15 November 2005; accepted 12 December 2005
Abstract
Hill et al. [R. J. Hill, D.L. Koch, J.C. Ladd, J. Fluid Mech. (2001), 448, pp. 213–241 and 243–278] proposed a set of drag correlations, based
on data from Lattice–Boltzmann simulations. These correlations, while very accurate within the range of void fractions and Reynolds numbers
used in the Lattice–Boltzmann simulations, do not cover the full range of void fractions and Reynolds numbers encountered in fluidized bed
simulations. In this paper a drag correlation applicable to the full range of void fractions and Reynolds numbers is developed by blending the Hill–
Koch–Ladd (HKL) drag correlation with known limiting forms of the gas–solids drag function such that the blended function is continuous with
respect to Reynolds number and void fraction. This study also corrects a misinterpretation of the HKL drag correlation that was published in the
literature, which makes the drag function discontinuous with respect to the Reynolds number.
Two examples of gas/solids flows in a bubbling fluidized bed and a one-dimensional channel flow are used to illustrate differences between the
proposed extension of HKL drag correlation and another form published in the literature.
© 2005 Elsevier B.V. All rights reserved.
Keywords: Drag correlation; LBM simulation; Gas/solids fluidization
1. Introduction
Due to the recent advances in computational resources and
software development, it has become possible to perform
detailed calculations of heavily loaded, gas-particle flows based
on two-fluids or DEM-fluid methods [1,2]. Both of these
approaches are based on fundamental physical laws, which
imply that they can be used as predictive methods. However,
they require the knowledge of several constitutive closure laws
the most important of which describes the momentum exchange
between the fluid and the particles. Such a correlation is
dependent on many parameters of the system, the foremost of
which are the Reynolds number of the flow and the solids
volume fraction. Other features, such as particle shape,
roughness, and the packing “fabric”, may also be important
but are seldom considered. Until recently, this closure law could
only be determined by the analysis of experimental data, which
leads to empirical correlations with limited theoretical under-
pinnings ([3] and references therein). Because of the empirical
nature of this principal closure law, the two-fluids or DEM-fluid
methods cannot truly be called ab initio methods. Ironically,
closure formulations for secondary constitutive law, the
granular stress, are much more firmly based in theory, thanks
to the kinetic theory of granular materials ([4] and references
therein).
However, recent articles [5–9] have used the Lattice–
Boltzmann method (LBM) to calculate the drag exerted by a
fluid flow on a collection of randomly dispersed, fixed
particles. Such calculations, repeated for different values of
the Reynolds number and the solids volume fraction, can be
used to derive a drag law. Thus, this essential constitutive
law of two-fluids and discrete element models of multiphase
flow can now be determined from first principles. The most
extensive numerical-experimental (a terminology justified by
the fact that LBM uses first principles calculations) data
Powder Technology 162 (2006) 166 – 174
+ MODEL
PTEC-06446; No of Pages 9
www.elsevier.com/locate/powtec
⁎
Corresponding author. Tel.: +1 304 285 1373; fax: +1 304 598 7185.
E-mail addresses: sof@fluent.com (S. Benyahia), tobrie@netl.doe.gov
(T.J. O'Brien).
1
Tel.: +1 304 285 4571.
0032-5910/$ - see front matter © 2005 Elsevier B.V. All rights reserved.
doi:10.1016/j.powtec.2005.12.014
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