Experiments and numerical computations have highlighted that heavy particle
s entrained in wall-bounded (e.g. nonhomogeneous) turbulent flows tend to a
ttain a nonuniform distribution in the normal-to-the-wall direction, with h
igher concentrations near the wall. Recently, a Eulerian model for predicti
ng particle deposition rates that explains the experimental observations on
the basis of turbophoretic force was presented. This force causes particle
s to gain a net drift velocity down the gradients of turbulence intensities
. In this paper, we investigate the feasibility of the Eulerian approach fo
r modeling the phenomenology of turbulent dispersion in pipe flow with refl
ecting walls. Model predictions are compared with original results obtained
through direct numerical simulations (DNS) and Lagrangian particle trackin
g in a turbulent pipe flow (Re = 4900). We show that the direct implementat
ion of the model proposed recently tends to overpredict concentration peaks
at the pipe wall, a trend that had already been observed in the context of
deposition theory (perfectly absorbing wall). We propose a modified model
for computing turbophoretic. drift velocity by providing an estimate for a
term that was considered negligible in the original formulation of the part
icle momentum balance equation. A better agreement (order of magnitude) bet
ween DNS results and model predictions is found. (C) 2001 Elsevier Science
Ltd. All rights reserved.