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Numerical Analysis of Roughness Effects on Rankine Viscosity
Measurement
Hila Hashemi, University of California, Berkeley
Jinquan Xu, Mentor, Florida State University
Objective
Collecting research experience on computational science and applied mathematics, including defining a problem, formulating solution strategies, implementing the strategies, and anglicizing the results
Overview
Roughness effects on the pressure loss of micro-scale Rankine Viscometer tubes are numerically investigated;
Surface roughness is explicitly modeled through a set of generated peaks along an ideal smooth surface;
A parametric study is carried out to study the relationship between the roughness and pressure loss quantitatively.
Introduction
Rankine Viscometer; Hagen-Poiseuille law;
Newtonian fluid through a cylindrical tube with an ideal SMOOTH surface;
LQrP
8
4
where vrQ 2 zgP and
0
z
z1
z2
L
g
R
r
p0
p0
p1
p2
R
L = 933.5 mm r = 165.8 m, Re 15.0
Fig. 1 Schematic of a Rankine Viscometer
Introduction (cont.)Rough tube, with roughness
ranging from 0.0~5.0% (Roughness defined as the ratio between the average of the peak heights and the hydraulic diameter.
Fig. 2 Cross-section of a rough micro tube. (Picture courtesy:
Microgroup, Inc.)
Problem Formulation
• Numerical simulation of Newtonian fluid through a cylindrical tube with a rough surface;• Study of the relationship between tube length and pressure loss;• Generic modeling of flow in a short tube.
Fig. 3 A portion of the computational domain and mesh
Boundary Conditions• Inlet: a specified velocity;• Outlet: zero normal gradient;• Rough walls: non-slip BC.
Problem Formulation (cont.)
0 u
uu 2 PDtD
Governing Equations
Solution Technique
Gambit is used for meshing;
The flow equations are solved using the semi-implicit method for pressure-linked equation algorithm implemented in Fluent
Numerical Results And Discussions
0
0.00005
0.0001
0.00015
0.0002
0.00025
0.2 0.4 0.6 0.8 1
Relative length
Pre
ss
ure
dro
p (
Pa
sc
al)
1. The pressure drop is linearly dependant to the relative length of tube which is normalized by a factor of 0.01658 meter;
2. We can study a short tube instead of a long one for expeditious computation.
The relation between tube length and pressure loss
Fig. 4 The relation between thetube length and pressure drop
Smooth tube, Liquid O2, Re= 15, r= 165 μm
Numerical Results And Discussions (cont.)
Fig. 5 The pressure contour of different roughness tube
Liquid O2,
r = 165.8 μm, Re= 15
Influence of roughness on pressure drop and velocity
Numerical Results And Discussions (cont.)
0
0.000005
0.00001
0.000015
0.00002
0.000025
0.00003
0 1 2 3 4 5 6
Roughness (%)
Pre
ss
ure
dro
p (
Pa
sc
al)
Liquid O2,
r = 165.8 μm, Re= 15
Fig. 6 The influence of roughness on pressure drop
Numerical Results And Discussions (cont.)
Liquid O2, r = 165.8 μm, Re= 15
Fig. 7 The velocity vector of different roughness tube
Numerical Results And Discussions (cont.)
5% roughnessLiquid O2, r = 165.8 μm
Fig. 8 The influence of flow velocity on pressure drop
0.00E+00
1.00E-05
2.00E-05
3.00E-05
4.00E-05
5.00E-05
4.00E-05 6.00E-05 8.00E-05 1.00E-04 1.20E-04
Velocity (m/s)
Pre
ss
ure
dro
p (
Pa
sc
al)
Conclusions
• The pressure loss is a linear function of the tube length;
• The roughness affects on the pressure loss in a non-trivial way; The rougher a tube is, the more the fluid pressure drops through the tube;
• It is feasibility to correct the Rankine viscometer measured data through numerical analysis;
• Mesh refinements are needed along the rough boundary.
Reference
1. Patankar SV, Numerical Heat Transfer and Fluid Flow, Hemisphere Publishing Corporation, 1980.
2. Judy J, Maynes D, Webb BW, “Characterization of Frictional Pressure Drop for Liquid Flows through Microchannels,” International Journal of Heat and Mass Transfer, Vol. 45, pp. 3477-89, 2002.
3. Bird RB, Stewart WE, and Lightfoot EN, Transfer Phenomena, 2nd edition. John Wiley and Sons, Inc., 2002.
4. Croce C and D’Agaro P, “Numerical Analysis of Roughness Effect on Microtube Heat Transfer,” Superlattices and Microstructures. 2004. (In press)