International Journal of Fluid Power Engineering, ISSN:2051-0732, Vol.20, Issue.1 1139
© RECENT SCIENCE PUBLICATIONS ARCHIVES| February 2014|$25.00 | 27703043 |
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Influence of Expansion Ratio of Varied Inclined
Sudden Expansion Step on Hydrodynamics of Non-
Newtonian Fluids Flow
Khudheyer S. Mushatet
College of Engineering, Thiqar
University, Nassiriya, Iraq
Email: khudheyer2004@yahoo.com
Qais A. Rishak
College of Engineering, Basra
University, Basra, Iraq
Email: qais_abd200@yahoo.com
Sarah E. Hamdi
College of Engineering, Thiqar
University, Nassiriya, Iraq
Email: msc_sara_emad@yahoo.com
ABSTRACT
A numerical study has been obtained to investigate the
effect of a channel expansion ratio of varied inclined step
on hydrodynamics behavior of the non-Newtonian fluids
flow. The study covered a range of parameters such step
angle of inclination (
90 30 ) and Prandtle number
(2.5≤ Pr≤ 15) for Re=200. A Fluent software was used to
get the solution of the governing equations while the mesh
was created by using Gambit 2.3. The conducted results
show that the size and strength of recirculation for shear
thinning fluids is increased as expansion ratio increases
and this trend is reflected for shear thickening fluids.
Keywords-non-Newtonian fluids, sudden expansion,
laminar flow
1. INTRODUCTION
Investigation of non-Newtonian fluids flow in a sudden
expansion is still represent one of the target issues for
many researchers in recent years. The flow in such
configuration is considered complex because the variable
viscosity needs a suitable treatment models. Many devices
uses the non-Newtonian fluids flow as polymers and
manufacturing of coated sheets. The author here is still
develop here an a sudden varied inclined step
configuration by investigating the effect of its expansion
ratio on hydrodynamics performance of non-Newtonian
fluid flow. Many researchers studied the Newtonian and
non-Newtonian fluid flow in a sudden expansion. Hawa
and Rusak [1] studied numerically the dynamics of the
incompressible laminar flow in a symmetric long channel
with a sudden expansion. The results showed that the
bifurcation at critical Reynolds number has a pitchfork
nature and grew in parabolic manner near the critical
Reynolds number. Pinho et al. [2] investigated the non-
Newtonian fluid flow inside an axi symmetric sudden
expansion channel. The shear thinning and inelastic with a
viscosity obeying the power law model were used. They
showed that at low Reynolds number, the local loss
coefficient enhanced by more than 100٪ while it was
enhanced by more than 50٪ at higher Reynolds number.
Thiruvengadam et al.[3] investigated the laminar three
dimensional Newtonian flow in a duct with expansion
ratio 2 and aspect ratio of 4. It was found that the
bifurcation induced due to the critical Reynolds number
made the heat transfer and temperature distribution to be a
symmetric in the transverse direction. An experimental
study on the effect of three dimensionality on low
Reynolds number flows past a symmetric sudden
expansion channel was performed by Battaglia and
Papadopoulos [4]. It was found that that the two
dimensional numerical simulation failed to capture the
effect of the expansion when the geometry was defined by
the expansion ratio only. The laminar incompressible non-
Newtonian fluids flow through a sudden expansion
channel was studied by Manica and Bortelli [5]. The
obtained results verified that the bifurcation was appeared
after that of the Newtonian situation for shear-thinning and
the opposite occurs for shear thickening.. The bifurcation
phenomena in a two dimensional symmetric sudden
expansion for different values of Reynolds numbers and
expansion ratios was studied by Drikakis as cited by
Nabavi [6]. It was noticed that the flow tendency to be
asymmetric was increased with increasing the value of
Reynolds number while it was decreased with increasing
the value of expansion ratio. Ternik [7] investigated
numerically the steady laminar flow of shear-thickening
fluid in a 1:3 symmetric sudden expansion channel. The
obtained results showed that the shear thickening trend
lowers the thresh hold of the transition from flow
symmetry to flow asymmetry. Alves et al. [8] made a
numerical study to investigate the three dimensional non-
Newtonian fluids flow in a square sudden contraction.
Their results showed that the increase in the flow rate
resulted multiple flow parameters depending on the
studied fluids besides to the Deborah number. Chiang et
al. [9] investigated the side wall effect on fluid down
stream of a planar sudden expansion for different aspect
ratios. They verified that the symmetry state was obtained
at AR< 3.5 and Re=60 and the flow symmetry beyond this
value was disappeared due to conda effect. Kalaf et al[10]
studied the bifurcation phenomena in a sudden expansion
channel of expansion ratio 1:3. They used a power law
model along with a finite volume method to discretize the
governing equations. The results verified that the non-
Newtonian fluids behavior was similar to that of
Newtonian fluids beyond the critical Reynolds number.
In this study, a numerical investigation has been
conducted to state the impact of expansion ratio on
hydrodynamics of non-Newtonian fluids flow for varied
inclined sudden expansion step. This study is performed