From a review of technical literature, it was not apparent if the Lagrangian or the Eulerian dispersed phase modeling approach was more valid to simulate dilute erosive slurry flow. In this study, both modeling approaches were employed and a comparative analysis of performances and accuracy between the two models was carried out. Due to an impossibility to define, for the Eulerian model already implemented in FLUENT, a set of boundary conditions consistent with the Lagrangian impulsive equations, an Eulerian dispersed phase model was integrated in the FLUENT code using subroutines and user-defined scalar equations. Numerical predictions obtained from the two different approaches for two-phase flow in a sudden expansion were compared with the measured data. Excellent agreement was attained between the predicted and observed fluid and particle velocity in the axial direction and for the kinetic energy. Erosion profiles in a sudden expansion computed using the Lagrangian scheme yielded good qualitative agreement with measured data and predicted a maximum impact angle of 29 deg at the fluid reattachment point. The Eulerian model was adversely affected by the reattachment of the fluid phase to the wall and the simulated erosion profiles were not in agreement with the Lagrangian or measured data. Furthermore, the Eulerian model under-predicted the Lagrangian impact angle at all locations except the reattachment point.

1.
Finnie
,
I.
, 1995, “
Some Reflections on the Past and Future of Erosion
,”
Wear
0043-1648,
186-187
, pp.
1
10
.
2.
Durst
,
F.
,
Milojevic
,
D.
, and
Schonung
,
B.
, 1984, “
Eulerian and Lagrangian Predictions of Particulate Two-Phase Flows: A Numerical Study
,”
Appl. Math. Model.
0307-904X,
8
, pp.
101
115
.
3.
Adeniji-Fashola
,
A.
, and
Chen
,
C. P.
, 1990, “
Modeling of Confined Turbulent Fluid-Particle Flows Using Eulerian and Lagrangian Schemes
,”
Int. J. Heat Mass Transfer
0017-9310,
33
, pp.
691
701
.
4.
Lee
,
B. E.
,
Tu
,
J. Y.
, and
Fletcher
,
C. A. J.
, 2002, “
On Numerical Modelling of Particle-Wall Impaction in Relation to Erosion Prediction: Eulerian Versus Lagrangian Method
,”
Wear
0043-1648,
252
, pp.
179
188
.
5.
Chen
,
X.
,
McLaury
,
B. S.
, and
Shirazi
,
S. A.
, 2002, “
Effects of Applying a Stochastic Rebound Model in Erosion Prediction of Elbow and Plugged Tee
,”
Proceedings of ASME FEDSM 2002
, Montreal, Quebec, Canada.
6.
Patankar
,
S. V.
, 1980,
Numerical Heat Transfer and Fluid Flow
,
Taylor & Francis
,
London
.
7.
Ferziger
,
J. H.
, and
Peric
,
M.
, 2002,
Computational Method for Fluid Dynamics
,
Springer
,
New York
.
8.
Drew
,
D. A.
, 1983, “
Mathematical Modeling of Two-phase Flow
,”
Annu. Rev. Fluid Mech.
0066-4189,
15
, pp.
261
291
.
9.
Fluent
, 2007, FLUENT 6.3 User’s Guide, Fluent Inc., Lebanon, NH.
10.
Morsi
,
S. A.
, and
Alexander
,
A.
, 1972, “
An Investigation of Particle Trajectories in Two-Phase Flow Systems
,”
J. Fluid Mech.
0022-1120,
55
, pp.
193
208
.
11.
Crowe
,
C. T.
,
Sommerfield
,
M.
, and
Tsuji
,
Y.
, 1998,
Multiphase Flows With Droplets and Particles
,
CRC
,
Boca Raton, FL
.
12.
Gosman
,
A. D.
, and
Ioannides
,
E.
, 1981, “
Aspects of Computer Simulation of Liquid-Fuelled Combustors
,” AIAA Paper No. 81-0323.
13.
Humphrey
,
J. A. C.
, 1990, “
Fundamentals of Fluid Motion in Erosion by Solid Particle Impact
,”
Int. J. Heat Fluid Flow
0142-727X,
11
, pp.
170
195
.
14.
Forder
,
A.
,
Thew
,
M.
, and
Harrison
,
D.
, 1998, “
A Numerical Investigation of Solid Particle Erosion Experienced Within Oilfield Control Valves
,”
Wear
0043-1648,
216
, pp.
184
193
.
15.
Pourahmadi
,
F.
, and
Humphrey
,
J. A. C.
, 1983, “
Modelling Solid-Fluid Turbulent Flows With Application to Predicting Erosive Wear
,”
PCH, PhysicoChem. Hydrodyn.
0191-9059,
4
, pp.
191
219
.
16.
Tu
,
J. Y.
, and
Fletcher
,
C. A. J.
, 1995, “
Numerical Computation of Turbulent Gas-Solid Particle Flow in a 90 Bend
,”
AIChE J.
0001-1541,
41
, pp.
2187
2197
.
17.
Chen
,
C. P.
, and
Wood
,
P. E.
, 1985, “
A Turbulence Closure Model for Dilute Gas-Particles Flow
,”
Can. J. Chem. Eng.
0008-4034,
63
, pp.
349
360
.
18.
Tu
,
J. Y.
, and
Fletcher
,
C. A. J.
, 1996, “
Eulerian Modelling of Dilute Particle-Laden Gas Flows Past Tubes
,”
Comput. Fluid Dyn. J.
0918-6654,
5
, pp.
45
70
.
19.
Schaaf
,
S. A.
and
Chambre
,
P. L.
, 1958, “
Flow of Rarefied Gases, Section H
,”
Fundamentals of Gas Dynamics
,
Princeton University Press
,
Princeton, NJ
.
20.
Soo
,
S. L.
, 1984, “
Development of Theories on Liquid Solid Flows
,”
J. Pipelines
0166-5324,
4
, pp.
137
145
.
21.
Founti
,
M. A.
, and
Klipfel
,
A.
, 1998, “
Experimental and Computational Investigations of Nearly Dense Two-Phase Sudden Expansion Flows
,”
Exp. Therm. Fluid Sci.
0894-1777,
17
, pp.
27
36
.
22.
White
,
F. M.
, 1999,
Fluid Mechanics
,
McGraw-Hill
,
New York
.
23.
White
,
F. M.
, 1991,
Viscous Fluid Flow
,
McGraw-Hill
,
New York
.
24.
Freitas
,
C. J.
, 1993, “
Editorial Policy Statement on the Control of Numerical Accuracy
,”
ASME J. Fluids Eng.
0098-2202,
115
, pp.
339
340
.
25.
Roache
,
P. J.
, 1998,
Verification and Validation in Computational Science and Engineering
,
Hermosa
,
Albuquerque, NM
.
26.
Roache
,
P. J.
, 1995,
Verification of Codes and Calculations
, AIAA Paper No. 696-702.
27.
Roache
,
P. J.
, 1997, “
Quantification of Uncertainty in Computation Fluid Dynamics
,”
Annu. Rev. Fluid Mech.
0066-4189,
29
, pp.
123
160
.
28.
Postlethwaite
,
J.
, and
Nesic
,
S.
, 1993, “
Erosion in Disturbed Liquid/Particle Pipe Flow: Effects of Flow Geometry and Particle Surface Roughness
,”
Corrosion
,
49
, pp.
850
857
.
29.
Oka
,
Y. I.
,
Ohnogi
,
H.
,
Hosokawa
,
T.
, and
Matsumura
,
M.
, 1997, “
The Impact Angle Dependence of Erosion Damage Caused by Solid Particle Impact
,”
Wear
0043-1648,
203–204
, pp.
573
579
.
30.
O’Mahony
,
A. P.
, 2006, “
Numerical Simulation of Slurry Erosion Using Lagrangian and Eulerian Techniques
,” Ph.D. thesis, University of Limerick, Limerick, pp.
55
84
.
31.
Hutchings
,
I. M.
, 1992,
Tribology: Friction and Wear of Engineering Materials
,
Edward Arnold
,
London, UK
.
You do not currently have access to this content.