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1st International Conference of Recent Trends in Information and Communication Technologies
*Corresponding author: [email protected]
Computational Fluid Dynamic (CFD) Study of Scour Gap Effect around a
Pipe Abbod Ali1, P. Ganesan1, Shatirah Akib2,*
1 Department of Mechanical Engineering, Faculty of Engineering, University of Malaya Kuala Lumpur,
Malaysia-50603,
2 Department of Civil Engineering, Faculty of Engineering, University of Malaya, Kuala
Lumpur, Malaysia-50603, Phone: +03-79677651
Abstract
A numerical investigation of incompressible and transient flow around circular pipe has been carried out
at different five phases. Flow equations such as Navier-Stocks and continuity equations have been solved
using finite volume method. Unsteady horizontal velocity and kinetic energy square root profiles are
plotted using standard k model and Large Eddy Simulation (LES) model and their sensitivity is
checked against published experimental results. Flow parameters such as drag coefficient and lift
coefficient are studied and presented graphically to investigate the flow behavior around an immovable
pipe and scoured bed. The standard k-ε model and LES both can predict accurate results in comparison to
other turbulence models
Keywords: CFD; unsteady flow; flow around circular pipe; turbulence models; vortex shedding;
scouring; interfacial forces; vortex induced vibration (VIV).
IRICT 2014 Proceeding
12th -14th September, 2014, Universiti Teknologi Malaysia, Johor, Malaysia
Abbod Ali et. al. /IRICT (2014) 561-574 562
1 Introduction
Scouring can be defined as the erosion of sand bed sediment surrounding the obstruction i.e.,
bridge piers and abutments when the obstruction is exposed to continuously strong flow field
or flood events [1-4].The sand bed can be undermined due to the normal flow field subjected
to the obstruction under flow conditions by which its rate increases with larger flow events. In
other words, scouring is basically caused when the foundation of the bed is swept away under
flood conditions in which the flow around the obstruction accelerates and induces high shear
stress over the seabed surface [5, 6]. The resulted reduction of the sand bed around the pier
and abutment below the normal and natural river level is called the scour depth. A scour hole is
a pit or void that forms as a result of the sand bed sediment removal from the river bed [7].
Cylindrical bridge piers are the mostly used hydraulic structures in coastal, offshore and river
engineering. Thus, scour around bridge piers and submarines prediction is attracted by the
hydraulic and ocean engineers. Local scouring surrounding the bridge piers is considered to
be one of the mostly common causes of bridge pier failure [8-10].The local scour around river
hydraulic structures is a disaster mitigation of the engineering structure [11, 12]. It leaves them
in unsafe conditions requiring maintenance and occasionally results in loss of life. Damage of
hydraulic structure because of local scouring is a global concern, and it has been studied by
many researchers experimentally and numerically for several decades such as [13, 14].
Mao [22] studied the interaction between a pipeline and erodible bed. Author observed the scour
around horizontal cylinders in steady current and wave conditions, as well as with different
Reynolds numbers (Re), Shields parameters, and pipeline gaps. These experiments examined
scour features such as shape and size of the scour hole, and the time scale of the scour
formation. Later this work was further investigated by Jensen [23]. They investigated
experimentally the flow around a pipeline placed initially on a flat, erodible bed at five
characteristics stages of a progressive process in currents. The results showed that as the scour
develops with time and space, the mean flow field and turbulence around and the forces on a
pipeline undergo considerable changes. This study aims to investigate the effect of turbulence
models on the flow field behavior at different five scouring phases and study the effect of
scouring on flow parameters such as drag coefficient C𝑑 , lift coefficient Cl.
Abbod Ali et. al. /IRICT (2014) 561-574 563
2 Methodology
2.1 Geometrical structure and Boundary conditions
Fig. 1 shows the schematic of the two dimensional (2D) geometrical domain used in the
present study along with the corresponding boundary conditions. A logarithmic velocity
profile as presented in Fig. 3 is created using user-defined functions (UDF) in Fluent based
on the following formulation [24].
Figure 1: Geometrical model of computational domain and boundary conditions
Figure 2: The grid for model calculation
Abbod Ali et. al. /IRICT (2014) 561-574 564
lny
U
K y
u
(1)
Where U is an approach velocity (m/s), u
is friction (or shear) velocity, 1 2
u
(m/s) , y= water (or flow) depth (m) and y is roughness height (m).
The velocity profile is applied at the inlet. The profile from the presented CFD model is
compared with that from the experimental study of Dudley [25] for consistency, see Fig. 3.
Zero pressure outlet boundary condition is applied at the flow exist. The water surface (top wall)
is set as a symmetry boundary condition. No-slip boundary condition is applied on the pipe
surface and the scour bed. Gravity acts in the negative y-direction.
Figure3: Comparison of the horizontal logarithmic velocity-inlet (𝑼𝟎) in the total water depth between
present numerical investigation and experimental work of Dudley RD [25].
2.2 Governing equations
The continuity and the momentum equations for the present case are as given below:
Continuity equation:
0u
x y
(2)
X-component of the momentum equation:
2 2
2 2
u u u uu
x y x x y
(3)
Abbod Ali et. al. /IRICT (2014) 561-574 565
Y-component of the momentum equation:
2 2
2 2u g
x y y x y
(4)
2.3 Turbulence modeling
Turbulence models of two-equation k and Large Eddy Simulation (LES) models are used
in the present research and their results are compared with experimental data from the
literature.
2.3.1 k- 𝜺 models
Two-equation k- 𝜀 models, turbulent kinetic energy k and turbulent dissipation 𝜀, are the
simplest and the most widely used models among all turbulence models that aim to study the
effect of turbulence in the flow. Two-equation model signifies that it includes two extra
transport equations to represent turbulence properties of the flow. There are three different
models that are derived from k- 𝜀 model standard k- 𝜀 model, Realizable k- 𝜀 model and
Renomalization Group model (RNG). Despite of having the two general equations, these
turbulence models use the different ways to calculate the principle form of the eddy viscosity
equation
2.3.2 Large Eddy Simulation (LES)
A large-eddy simulation (LES) model explicitly calculates the large-eddy field and
parameterizes the small eddies. The large eddies in the atmospheric boundary layer are
believed to be much more important and insensitive to the parameterization scheme for the
small eddies. In large-eddy simulation (LES), the large three-dimensional unsteady turbulent
motions are directly resolved while the smaller scale motions are modeled. In terms of
Abbod Ali et. al. /IRICT (2014) 561-574 566
computational effort LES lies between RANS and DNS, and it can be expected more accurate
and reliable than Reynolds-stress models for flows where large-scale unsteadiness is significant
[26-30].
2.3.2.1 Smagorinsky-Lilly model
The first SGS model developed was the Smagorinsky-Lilly model, which was developed
by Smagorinsky. It models the eddy viscosity as:
2 2
2T s g ij jj s g
v C A S S C A S (5)
Where g
the grid is size and s
C is a constant. This method assumes that the energy
production and dissipation of the small scales are equilibrium.
2.4 Numerical methods
The commercial CFD software FLUENT 14.0 [31] which is based on Finite Volume Method
(FVM) is used to solve the Large Eddy Simulations (LES) equations for an incompressible
flow. The transport governing equations are discretized using the second order upwind spatial
discretization method. The Pressure-Implicit with Splitting of Operators (PISO) scheme was
used for the coupling of the pressure and the velocity fields. The under-relaxation factor of all
the components, such as velocity components and pressure correction is kept at 0.3. The scaled
residuals of 1×10-6 are set as the convergence criteria for the continuity and momentum
equations. Transient model based on implicit scheme with a time step were used in the current
numerical study. The typical wall treatment function y+ (= yUτ/ν) value of the first node in all
turbulence model near the bed profile is less than 1
Abbod Ali et. al. /IRICT (2014) 561-574 567
2.5 Simulation cases
A total of 7 cases were simulated in the present study, see Table 1. In the first part of this
study, the effect of different turbulence models such as standard k-ε model and Large Eddy
Simulation (LES) model on horizontal velocity and kinetic energy square root has been
investigated. For studying this effect, we have adopted the domain proposed by Jensen e
al.[23] to validate the results of Mao et al. [22]. This domain is of 0.5 m length and 0.1 m
height with pipe diameter of 0.03 m. Turbulence models were tested for scour gap at time 0
min, 1 min, 6 min, 30 min, and 300 min and four positions (X/D = -3.0, 1.0, 4.0, and 8.0) in-
front and behind the pipe. Qualitatively the results of a particular turbulence model were same
for all scour gaps, so, the results of Cases (1-2) for scour gap at time 0 min are presented.
Consequently, the turbulence model that reproduces a similar result as of experimental
investigation of Jensen et al. is chosen for all further simulation cases in the current study.
In the second part of this paper, a parametric study has been carried out by using five bed profiles
suggested by Mao [22] at 0 min, 1 min, 6 min, 30 min, and 300 min. Five simulation cases (7-
11) were run to obtain the drag coefficient d
C and lift coefficient l
C around the pipe with
different gaps at position X/D=0 using LES turbulence model.
Table 1: Simulation cases
2.6 Mesh independence and time step test
The computational mesh constructed by FLEUNT is based on the square grid. The grid used in
this simulation is a variable 0.001m grid along a scoured bed wall and around the cylinder
Abbod Ali et. al. /IRICT (2014) 561-574 568
region by which the finer mesh is required near solid boundaries including the bed's surface
and cylinder in order to solve the flow details near the solid regions. Accurate representation
of flow near the wall region leads to a successful prediction of the turbulent core of the flow
away from the wall and an accurate calculation of the bottom shear stress. Then, the finer
square grids near the scour bed and around cylinder are expended linearly to a coarse grid of
0.009 m towards the upper boundary (Fig. 2). In addition, the wall treatment functions is
applied by which in the current study Enhanced wall treatment with 𝑦+ are applied near solid
region such as bed scoured. Different wall treatment functions were tested and results showed
no differences can be produced especially with using 𝑦+< 1. Mesh independence is carried
out using five different types of grids having cell number of 40,000, 82,500, 130,225,
223404, and 315,623. A fine grid is used near the bed. The domain with 223,404 cells is
selected throughout this study, because it shows reasonable accuracy and the lowest deviations
of the velocity profile and turbulent kinetic energy (TKE) for turbulence models compared to
Jensen laboratory data. Four different time step sizes (∆t = 0.0002, 0.002, 0.02, and 0.2) were
tested and 0.002 is used throughout this current numerical study as there were no deviations
observed below this value of time step. The number of iterations for this study are kept
between 3000-3500.
Figure 4: Mesh independence test for Mean U x m s at location X/D= -3.0 for different types
of grids cell numbers, ---- Jensen , ---- 40000, ○ 82500, ----130225, ---- 223404, × 315623.
3 Results and discussion
Current numerical study has been carried out in two major sections. First section deals with
the effect of turbulence models such as standard k-ε model and Large Eddy Simulation
(LES) model on horizontal velocity profile and kinetic energy square root while the second
one deals with the effect of scour gap on drag d
C and lift l
C coefficients. A large number
of simulations have been run to study the effect of turbulence models on unsteady horizontal
velocity profile and turbulent kinetic energy square root, and the results are discussed in
section 3.1. The LES turbulence model identified using above study is used for further
investigation of effect of scour gap on d
C , l
C which is discussed in section 3.
Abbod Ali et. al. /IRICT (2014) 561-574 569
3.1 Effect of different turbulence models
Cases 1-7 are used to predict the horizontal velocity profile (Ux) and the turbulent kinetic
energy (TKE) at some axial length (i.e., X/D= -3.0,1.0,4.0, and 8.0) using different type
turbulence models and the results are presented in Fig.5 and Fig.6 respectively. For
comparisons, the experimental results reported in Jensen et al. [2] are also presented in the
figure. Note that, the location the axial position covers the front and rear part of the pipe (or
obstruction). Referring to Fig.5a tp 5b, which is presented at X/D= -3.0, 1.0, 4.0 and 8.0
respectively, the standard k-ɛ turbulence model prediction is much closer to experimental data
at various water depth; some of them overlap each other. Nearly the same can be said for the
LES model but some deviation seen at some of water depths; for example, at water depths
below 0.03m and those between 0.05 to 0.06 m at X/D = 4.0 (Fig. 5d ). TKE is well predicted
by standard k-ɛ and horizontal velocity profile (Ux) and the turbulent kinetic energy (TKE).
Figure 5: Unsteady horizontal velocity (𝑈𝑥) at different positions, (a) 𝑋/𝐷 = −3.0, (b) 𝑋/𝐷 = 1.0, (c) 𝑋/
㪈 = 4.0, and (d) 𝑋/𝐷 = 8.0with different turbulent models — standard 𝑘-𝜀, ο ELS and Red Jensen.
Abbod Ali et. al. /IRICT (2014) 561-574 570
Figure 6: Turbulent Kinetic Energy (TKE) at different positions, (a) 𝑋/𝐷 = −3.0, (b) 𝑋/𝐷 = 1.0, (c) 𝑋/𝐷 =
4.0, and (d) 𝑋/𝐷 = 8.0with different turbulent models — standard 𝑘-𝜀, ο ELS and Red Jensen.
Abbod Ali et. al. /IRICT (2014) 561-574 571
3.2 Effect of scouring depth
Fig .10 shows the drag and lift coefficients respectively for five different gap phases. When
the flow approaches to cylinder, the cylinder is subjected to different forces such as lift and
drag that cause the formation of gap scouring. As it is seen in the figure, the lift and drag
coefficients decrease as the gap becomes deeper. In addition, it is noticed that the pipe
subjects to negative lift coefficients as long as the bed erosion comes into action and it
remains throughout the scour process. The negative lift can be elaborated by the strong
suction (or gap) below and behind the cylinder and the angle attack of the approaching flow
(the position of the stagnation point). As a result of lift coefficient elimination, the drag coefficient is reduced with time as well. A reduction of 26.3% in Cd and 48.3 % in Cl was
observed between the time phases of 10 min and 300 min.
Figure 7: Bed profiles during the development of scouring
Abbod Ali et. al. /IRICT (2014) 561-574 572
Figure 8: Effect on (a) drag coefficient (𝐶𝑑) and lift coefficient (𝐶𝑙) at cylinder surface of different
time phases.
4. Conclusions and future work
Two dimensional (2D) CFD analyses were carried to investigate fluid flow over an
obstruction under different bed profiles using a number of turbulence models. Unsteady
horizontal velocity profile and the kinetic energy square root at few axial directions are
examined. The effect of scour depth on the drag coefficient, the lift coefficient of the
obstruction body were numerically investigated. The conclusions of the current study are as
follows:
The standard k-ε model and LES both can predict accurate results in comparison to other
turbulence models when compared to experimental data for unsteady horizontal velocity and
turbulent kinetic energy square root but it consumes time and needs a high performance
computer to perform the scouring simulation.
The drag and lift coefficients decrease as the gap under the pipe increases. A reduction of
26.3% in Cd and 48.3% in Cl was observed between the time phases of 10 min and 300 min.
Acknowledgement
The financial support by the high impact research Grants of the University of Malaya
(UM.C/625/1/HIR/61, account no. H-16001-00-D000061) and Exploratory Research Grant
Scheme (ERGS: ER013-2013A) are gratefully acknowledged.
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