Section 9: Laminar flows and transition - GAMM 2012
Section 9: Laminar flows and transition - GAMM 2012
Section 9: Laminar flows and transition - GAMM 2012
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<strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> 1<br />
<strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong><br />
Organizers: Suad Jakirlic (TU Darmstadt), Ulrich Rist (Universität Stuttgart)<br />
S9.1: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> I Tue, 13:30–15:30<br />
Chair: Suad Jakirlic, Ulrich Rist S1|01–A2<br />
Transition Prediction <strong>and</strong> Modeling in External Flows Using RANS-based CFD Codes<br />
Andreas Krumbein, Normann Krimmelbein, Cornelia Seyfert (DLR Göttingen)<br />
Besides wind tunnel testing <strong>and</strong> flight tests, CFD simulation based on RANS solvers has become<br />
a st<strong>and</strong>ard design approach in industry for the design of aircraft. For the design point of aircraft<br />
a positive assessment of the numerical results was achieved for many validation <strong>and</strong> application<br />
tests <strong>and</strong> the prediction capabilities of the software tools could be positively evaluated. As<br />
a consequence, high confidence in numerical simulations could be achieved in industry <strong>and</strong> will<br />
eventually allow more simulation <strong>and</strong> less physical testing. However, <strong>and</strong> despite of the progress<br />
that has been made in the development <strong>and</strong> application of RANS-based CFD codes, there is still<br />
the need for improvement, for example, with regard to the capability of a proper capturing of all<br />
relevant physical phenomena. This can only be achieved if capable <strong>and</strong> accurate physical models<br />
are available in the codes. On the one h<strong>and</strong>, the combined use of turbulence <strong>and</strong> <strong>transition</strong> models<br />
is indispensable for <strong>flows</strong> exhibiting separation, because otherwise the close interaction between<br />
the laminar-turbulent <strong>transition</strong> <strong>and</strong> its impact on flow separation is not reproduced. On the other<br />
h<strong>and</strong>, it is not possible to fully exploit the high potential of todays advanced turbulence models<br />
if <strong>transition</strong> is not taken into account. Thus, in modern high-fidelity CFD codes a robust <strong>transition</strong><br />
prediction <strong>and</strong> modeling must be established together with reliable <strong>and</strong> effective turbulence<br />
models.<br />
At DLR, the RANS codes for external <strong>flows</strong>, [1]-[2], have been provided with <strong>transition</strong> prediction<br />
<strong>and</strong> modeling functionalities which can be applied to three-dimensional aircraft configurations.<br />
Two different basic approaches are currently at h<strong>and</strong>: the streamline based <strong>and</strong> the transport<br />
equation approach.<br />
The streamline based approach uses information from the current flow solution along defined<br />
integration paths in order to compute the laminar boundary layers, either using a laminar<br />
boundary-layer method or by direct extraction from the RANS solution. A fully automated, local<br />
linear stability code analyses the laminar boundary layers <strong>and</strong> detects <strong>transition</strong> due to Tollmien-<br />
Schlichting or cross flow instabilities. The stability code, which applies the e N -method, [3]-[4], <strong>and</strong><br />
the two N factor approach, [5], for the determination of the <strong>transition</strong> points, uses a frequency estimator<br />
for the detection of the relevant regions of amplified disturbances for Tollmien-Schlichting<br />
instabilities <strong>and</strong> a wave length estimator for cross flow instabilities. Also separation induced <strong>transition</strong><br />
is covered. Alternatively, different empirical <strong>transition</strong> criteria for streamwise <strong>and</strong> crossflow<br />
<strong>transition</strong> are available <strong>and</strong>, in addition, criteria for attachment-line <strong>and</strong> by-pass <strong>transition</strong>. Using<br />
this approach <strong>transition</strong> is predicted either along spanwise line-in-flight cuts through a wing or<br />
along the boundary-layer edge streamline. The latter is the only possible way in the case of fully<br />
three-dimensional flow about fuselages or nacelles. The streamline approach has been validated<br />
by numerous test cases <strong>and</strong> is the st<strong>and</strong>ard <strong>transition</strong> prediction approach currently used in production<br />
simulation. Here, it is usually applied in parallel mode on large compute cluster systems,<br />
[6].<br />
The transport equation approach, [7], is relatively new <strong>and</strong> based exclusively on local variables<br />
so that it is inherently parallelizable <strong>and</strong>, thus, very well suited for unstructured CFD codes <strong>and</strong>
2 <strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong><br />
large applications which can only be tackled by massively parallel computations. The boundarylayer<br />
quantities are resolved by the RANS computational grid <strong>and</strong> approximated by the modeling<br />
approach reflected by two transport equations. The prediction of the locations of <strong>transition</strong> onset<br />
is based on empirical criteria which can <strong>and</strong> must be evaluated locally. While the original model<br />
formulation was restricted to the prediction of streamwise <strong>transition</strong> mechanisms the model is<br />
currently extended in order to predict crossflow <strong>transition</strong>, [8].<br />
The two different approaches <strong>and</strong> methods will be presented <strong>and</strong> explained, their applicability<br />
ranges are discussed <strong>and</strong> numerical results are compared to a number of validation test cases demonstrating<br />
the prediction accuracy of the different methods. The results from the application of<br />
the methods to large <strong>and</strong> partially very complex, industrial configurations are presented <strong>and</strong> discussed.<br />
Eventually, an outlook is given to the challenges placed by complex aircraft configurations<br />
<strong>and</strong> to the way forward to tackle the still open issues.<br />
[1] Krumbein, A., Automatic Transition Prediction <strong>and</strong> Application to Three-Dimensional Wing<br />
Configurations, Journal of Aircraft, Vol. 44, No. 1, 2007, pp. 119-133; also: AIAA Paper<br />
2006-914, January 2006.<br />
[2] Krimmelbein, N., Radespiel, R., Transition prediction for three-dimensional <strong>flows</strong> using parallel<br />
computation, Computers Fluids, No. 38, Elsevier, 2009, pp. 121-136, doi:10.1016/j.compfluid.2008.<br />
01.004.<br />
[3] Smith, A.M.O., Gamberoni, N., Transition, Pressure Gradient <strong>and</strong> Stability Theory, Douglas<br />
Aircraft Company, Long Beach, Calif. Rep. ES 26388, 1956.<br />
[4] van Ingen, J.L., A suggested Semi-Empirical Method for the Calculation of the Boundary<br />
Layer Transition Region, University of Delft, Dept. of Aerospace Engineering, Delft, The<br />
Netherl<strong>and</strong>s, Rep. VTH-74, 1956.<br />
[5] Rozendaal, R. A., Natural <strong>Laminar</strong> Flow Flight Experiments on a Swept Wing Business<br />
Jet-Boundary-Layer Stability Analysis, NASA CP 3975, March 1986.<br />
[6] Krimmelbein, N., Krumbein, A., Automatic Transition Prediction for Three-Dimensional<br />
Configurations with Focus on Industrial Application, AIAA-2010-4292, 40th AIAA Fluid<br />
Dynamics Conference <strong>and</strong> Exhibit, June 28 July 1, 2010, Chicago, Illinois, USA.<br />
[7] Langtry, R.B., Menter, F.R., Correlation-Based Transition Modeling for Unstructured Parallelized<br />
Computational Fluid Dynamics Codes, AIAA Journal, Vol. 47, No.12, 2009, pp.<br />
2894-2906, DOI: 10.2514/1.42362.<br />
[8] Seyfert, C., Krumbein, A., Correlation-Based Transition Transport Modeling for Three-<br />
Dimensional Aerodynamic Configurations, to be presented as AIAA paper at the 50th<br />
Aerospace Sciences Meeting, 9-12 January <strong>2012</strong>, Nashville, Tennessee, USA.<br />
Preliminary results of the conditional analysis of wall friction during laminarturbulent<br />
<strong>transition</strong> of a rough wall boundary layer<br />
Pavel Jonás, Ondřej Hladík, Oton Mazur, Václav Uruba (Czech Academy of Sciences Praha)<br />
The <strong>transition</strong>al intermittency is investigated in the zero pressure gradient boundary layer developing<br />
on the surface covered with s<strong>and</strong> paper (grits 60). The free stream mean velocity is 5 m/s<br />
<strong>and</strong> the turbulence level is either 0.3 percent or risen by means of the square mesh plane grid to<br />
3 percent <strong>and</strong> the dissipation length parameter 3.8 mm.
<strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> 3<br />
Records (25 kHz, 750000 samples, 16 bit) of the instantaneous wall friction in various locations<br />
are evaluated from the records of the single wall wire CTA output signal. The procedure of the<br />
constant temperature anemometer signal transformation to the wall friction has been developed<br />
formerly <strong>and</strong> presented in [1, 2]. The adjustment of this procedure to rough surface conditions<br />
is based on the mean wall friction distribution which has been determined in advance. This<br />
procedure is described in the paper.<br />
Then the <strong>transition</strong>al intermittency factor distribution is derived by means of the TERA<br />
method [3]. Next the conditional analysis of the wall friction records is done which sorts the wall<br />
friction records in passages with the non-turbulent structure (intermittency factor g = 0) <strong>and</strong><br />
those with the full turbulent structure (g = 1).<br />
Evaluated are the probability density function <strong>and</strong> the conditioned probability density functions<br />
of the wall friction, relevant moments <strong>and</strong> the mean residence time of the wall friction in<br />
laminar <strong>and</strong> turbulent state. Results are compared with analogous characteristics received during<br />
investigations of smooth wall boundary layers.<br />
[1] Jonás, P. - Mazur, O. - Uruba, V. (1999) Statistical characteristics of the wall friction in a<br />
flat plate boundary layer through by-pass <strong>transition</strong>. ZAMM 79, S3, S691-S692.<br />
[2] Jonás, P. - Mazur, O. - Uruba, V. (2002) Problem of the intermittency distributions in<br />
<strong>transition</strong>al boundary layers under <strong>flows</strong> with various scales of turbulence. PAMM, Proc.<br />
Appl. Math. Mech. 1, <strong>Section</strong> 10.5, 298-299.<br />
[3] Zhang, D.H. - Chew, Y.T. - Winoto, S.H.: (1996) Investigation of intermittency measurement<br />
methods for <strong>transition</strong>al boundary, Exp. Thermal <strong>and</strong> Fluid Sci. 12, 433-443.<br />
Velocity <strong>and</strong> shear stress distributions in laminar-turbulent <strong>transition</strong> of unsteady<br />
boundary layer on aerofoil in high accelerating <strong>and</strong> decelerating fluid flow<br />
Decan J. Ivanovic, Vladan M. Ivanović (University of Montenegro, Podgorica)<br />
The corresponding equations of unsteady boundary layer, by introducing the appropriate variable<br />
transformations, momentum <strong>and</strong> energy equations <strong>and</strong> similarity parameters set, being transformed<br />
into generalized form. These parameters are expressing the influence of the outer flow velocity<br />
<strong>and</strong> the flow history in boundary layer, on the boundary layer characteristics. Since the generalized<br />
equation contain summ of terms equal to the number of parameters, it is necessary to limit<br />
the number of parameters for numerical integration. The numerical integration of the generalized<br />
equation with boundary conditions has been performed by means of the difference schemes <strong>and</strong><br />
by using Tridiagonal Algorithm Method with iterations in the two once localized approximation,<br />
where the first unsteady <strong>and</strong> dynamic parameter will remaine, while all others will be let to be<br />
equal to zero, <strong>and</strong> where the derivatives with respect to the first unsteady parameter will be<br />
considered equal to zero. So obtained generalized solutions are used to calculate the distributions<br />
of velocity <strong>and</strong> shear stress in laminar-turbulent <strong>transition</strong> of unsteady incompressible boundary<br />
layer on aerofoil, whose center velocity changes in time as a degree function. It’s found that for<br />
both in confuser <strong>and</strong> in diffuser aerofoil regions the decelerating flow reduces the shear stress <strong>and</strong><br />
favours the separation of flow, which occurring for lower contour values. The accelerating fluid<br />
flow postpones the boundary layer separation, i.e. laminar-turbulent <strong>transition</strong>, <strong>and</strong> vice versa<br />
the separation is occurring for greater contour values of aerofoil. Boundary layer characteristics<br />
are found directly, no further numerical integration of momentum equation.
4 <strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong><br />
Unsteady convective diffusion of a solute in a Hagen-Poiseuille flow through a tube<br />
with permeable wall<br />
Alex<strong>and</strong>ru Dumitrache, Florin Frunzulica (POLITEHNICA University of Bucharest <strong>and</strong> Institute<br />
of Mathematical Statistics <strong>and</strong> Applied Mathematics)<br />
Effects of Interphase Mass Transfer (IMT) on the unsteady convective diffusion in a fluid flow<br />
through a tube surrounded by a porous medium is examined against the background of no IMT.<br />
The three coefficients namely exchange coefficient, convection coefficient, <strong>and</strong> dispersion coefficient<br />
are evaluated asymptotically at large-time using Gill Sankarasubramanian model [1]. The<br />
exchange coefficient exists due to IMT.<br />
The convective diffusion equation <strong>and</strong> the corresponding initial <strong>and</strong> boundary conditions are<br />
used for the beginning<br />
∂C<br />
∂t<br />
+ u(r)∂C<br />
∂x<br />
2 ∂ C 1<br />
= D +<br />
∂x2 r<br />
<br />
∂<br />
r<br />
∂r<br />
∂C<br />
<br />
∂r<br />
(1)<br />
C(0, x, r) = F (x, r) (2)<br />
C(t, ∞, r) = 0 = ∂C<br />
(t, ∞, r) (3)<br />
∂r<br />
−D ∂C<br />
∂r (t, x, r) = KsC at r = ±R. (4)<br />
where D is the molecular diffusivity <strong>and</strong> Ks is the rate of mass transfer of solute at the walls of<br />
the cylinder. The condition (3) means that solute does not reach distances far down stream. The<br />
condition (4) implies that the flux of concentration at the walls is due to a first order chemical<br />
reaction.<br />
Then the dimesionless parameters will be used to transform equation.<br />
The convection <strong>and</strong> dispersion coefficient of solute are studied as a function of slip parameter,<br />
IMT parameter <strong>and</strong> porous parameter. All-time analysis is made analytically when there is no<br />
IMT. The mean concentration distribution is measured at a point inside <strong>and</strong> outside the slug.<br />
The peak of mean concentration is higher than that of pure convection <strong>and</strong> it is further enhanced<br />
with increase of porous parameter (or decrease of particle size).<br />
The results have applications in heat exchangers, petroleum <strong>and</strong> chemical engineering problems,<br />
chromatography <strong>and</strong> biomechanical problems.<br />
[1] R. Sankarasubramanian <strong>and</strong> W. N. Gill, Unsteady convective diffusion with interphase<br />
mass transfer, Proc. Roy. Soc. London A, 333 pp. 115–132, 1973.<br />
On the Optimum Efficiency of a Flapping Foil And Its Application to Valveless Pumps<br />
Markus Müllner (TU Wien)<br />
Several different working principles exist to drive a valveless pump. An efficient pump may be<br />
constructed by placing a flapping foil into a channel. For the case of inviscid flow, the pressure<br />
difference along the channel is equivalent to the thrust force acting on the propulsor. The effect<br />
of the channel walls on the forces is briefly discussed. The focus in this talk is on the determination<br />
of movements of highest propulsive efficiency for a given thrust. In order to treat the
<strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> 5<br />
optimization problem analytically, the case of a slender foil placed in a free stream, flapping in<br />
time-harmonic motion with small deflections, is investigated. Novel results for the heaving- <strong>and</strong><br />
pitching amplitude <strong>and</strong> for the pivot point of the pitching motion are presented as a function<br />
of the reduced frequency σ. A surprising outcome is that for a certain range of the thrust force,<br />
the reduced frequency needs to be infinitely large to obtain maximum efficiency. Unfortunately,<br />
the optimum movements are accompanied by some drawbacks. An important issue is to reduce<br />
the lateral forces acting on the structure. Therefore, foil movements with zero lateral force are<br />
investigated <strong>and</strong> the deficit in efficiency is compared to the optimum foil motion. Furthermore,<br />
instead of the foil, an undulating wave motion is considered. The analytic result for different wave<br />
numbers k is presented <strong>and</strong> the efficiency is compared to the optimum solution of the foil.<br />
S9.2: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> II Tue, 16:00–18:00<br />
Chair: Ulrich Rist, Suad Jakirlic S1|01–A2<br />
Global flow instabilities in plane sudden expansions<br />
Hendrik Christoph Kuhlmann , Daniel Lanzerstorfer (TU Wien)<br />
The three-dimensional linear stability of the two-dimensional, incompressible flow in a plane symmetric<br />
sudden expansion is considered. The geometry is varied systematically, covering expansion<br />
ratios (steps to outlet height) from 0.25 to 0.95. The stability analysis reveals that the primary<br />
symmetry-breaking bifurcation is two-dimensional. The asymmetric flow solution, however, becomes<br />
unstable to different secondary three-dimensional instabilities. The critical modes depend on<br />
the expansion ratio. An energy-transfer analysis is used to underst<strong>and</strong> the nature of the instabilities.<br />
In the limit of vanishing step height, the critical mode is stationary <strong>and</strong> the amplification<br />
process is caused by a shear instability. For high expansion ratios, the basic jet-like flow <strong>and</strong><br />
becomes unstable due to centrifugal forces leading to an oscillatory mode. For intermediate expansion<br />
ratios, an elliptic instability mechanism is identified <strong>and</strong> the instability characteristics<br />
change continuously with the expansion ratio. For an asymmetric geometry the disconnected<br />
primary solution branches are readily shifted to very high Reynolds numbers. The connected twodimensional<br />
solution branch is found to be very similar to the asymmetric flow of the symmetric<br />
channel thus showing the same type of secondary instability.<br />
Connecting the dots: Symmetry Analysis in Linear Stability Theory of a Linear Shear<br />
Flow<br />
Andreas Nold, Martin Oberlack (TU Darmstadt)<br />
A novel self-similar base solution for linear stability analysis of an unbounded linear shear flow<br />
employing symmetry methods is presented. Symmetry analysis is used to derive a full classification<br />
of symmetries of the linearized Navier-Stokes-Equations for two-dimensional perturbations<br />
of a linear shear flow. It is shown that the normal mode approach leading to the Orr-Sommerfeld<br />
equation <strong>and</strong> the Kelvin mode approach are both special classes of self-similar ansatz functions<br />
systematically derived in the framework of symmetry analysis. A third novel class of ansatz<br />
functions is presented. In the viscous case, known solutions of the initial value problem can be<br />
recovered by superposition of the novel self-similar modes. In the inviscid case, a new closed-form<br />
solution of traveling, energy-conserving modes localized in spanwise direction is presented.<br />
An Exact Navier-Stokes Solution for Three-Dimensional, Spanwise-Homogeneous<br />
Boundary Layers<br />
M. O. John, D. Obrist, L. Kleiser (ETH Zürich)
6 <strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong><br />
In some boundary layer <strong>flows</strong> the incompressible Navier-Stokes equations are amenable to exact<br />
similarity solutions. Two such cases are the plane stagnation flow onto a wall (Hiemenz boundary<br />
layer, HBL) <strong>and</strong> the asymptotic suction boundary layer flow (ASBL) over a flat wall. The Hiemenz<br />
solution has been extended to the swept Hiemenz configuration by superposition of a third,<br />
spanwise-homogeneous sweep velocity. This solution, however, becomes singular as the chordwise,<br />
tangential base flow component vanishes. Similarly, the ASBL does not contain any chordwise<br />
velocity.<br />
This work presents a generalized three-dimensional similarity solution, using a novel similarity<br />
coordinate. The HBL <strong>and</strong> ASBL are shown to be two limits of this solution which describes threedimensional<br />
spanwise-homogeneous impinging boundary layers at arbitrary wall-normal suction<br />
velocities.<br />
Further extensions may consist of oblique impingement, or different boundary suction directions,<br />
such as slip walls or stretching walls.<br />
Near critical laminar flow past an expansion ramp<br />
A. Kluwick, S. Braun, R. Szeywerth (TU Wien)<br />
Steady two-dimensional laminar <strong>flows</strong> past an expansion ramp are known to exist up to a critical<br />
ramp angle αc in the limit as the Reynolds number tends to infinity. The theory of viscousinviscid<br />
interaction combined with a local bifurcation analysis is used to study the evolution of<br />
three-dimensional unsteady perturbations if |α − αc| ≪ 1 for both sub- <strong>and</strong> supercritical conditions.<br />
Special emphasis is placed on the effects of controlling devices <strong>and</strong> the phenomenon of<br />
bubble bursting.<br />
Asymptotic description of incipient separation bubble bursting<br />
Stefan Braun, Stefan Scheichl, Alfred Kluwick (TU Wien)<br />
The appearance of short laminar separation bubbles in high Reynolds number wall bounded <strong>flows</strong><br />
due to appropriate adverse pressure gradient conditions is usually associated with minor effects on<br />
global flow properties (e.g. lift force). However, localized reverse flow regions are known to react<br />
very sensitively to perturbations <strong>and</strong> in further consequence may trigger the laminar-turbulent<br />
<strong>transition</strong> process or even cause global separation. The present investigation of marginally separated<br />
boundary layer <strong>flows</strong> is based on a high Reynolds number asymptotic approach. Special<br />
emphasis is placed on solutions of the corresponding model equations which blow up within finite<br />
time indicating the ejection of a vortical structure <strong>and</strong> the emergence of shorter spatio-temporal<br />
scales reminiscent of the early <strong>transition</strong> scenario (‘bubble bursting’). Among others, an adjoint<br />
operator method is used to formulate the consequential evolution equations of the viscous-inviscid<br />
interaction process beyond blow up. Recent analytical <strong>and</strong> numerical findings regarding this new<br />
stage will be presented.<br />
Cauchy Problems <strong>and</strong> Breakdown in the Theory of Marginally Separated Flows<br />
Mario Aigner, Stefan Braun (TU Wien)<br />
Flow separation can be viewed as one of the trigger events of laminar-turbulent boundary layer<br />
<strong>transition</strong>. Thus, intensive investigations have been carried out as to when <strong>and</strong> how laminar boundary<br />
layers break down. In the special case of marginal separation, i.e. the formation of short<br />
laminar separation bubbles, high Reynolds number asymptotic theory yields integro-differential<br />
equations governing the essential flow behavior. Since <strong>transition</strong>, which can be associated with<br />
”bubble bursting”, is an inherent time dependent phenomenon, initial value problems (IVPs) were<br />
formulated, using appropriate time scales within the according asymptotic setting. We will present<br />
further considerations of these problems in planar <strong>and</strong> three-dimensional flow cases regarding
<strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> 7<br />
the general ill-posedness, using analytical <strong>and</strong> numerical techniques to depict the spatio-temporal<br />
manifestation of short-scale instabilities. To regularize such disturbances, higher order asymptotic<br />
terms comprising the streamline curvature in the boundary layer region are taken into account.<br />
Evidence for well-posedness of this modified problem will be given in terms of a dispersion relation<br />
<strong>and</strong> numerical solutions of the full problem, especially by performing backward in time<br />
calculations. Even though the regularized IVPs admit limiting steady states in their time evolution,<br />
the phenomenon of finite time blow-up, which can be interpreted as ”bubble bursting”, is<br />
still present. As a consequence, the inevitable breakdown of the according flow description leads<br />
to the emergence of a new asymptotic structure of shorter spatio-temporal scales (yielding a so<br />
called nonlinear triple deck stage). Deeper insight into this next stage of the bursting process is<br />
still to be gained <strong>and</strong> we will conclude by presenting some first attempts in solving this problem.<br />
S9.3: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> III Wed, 13:30–15:30<br />
Chair: Andreas Krumbein, Suad Jakirlic S1|01–A2<br />
Transition Modelling for Aerodynamic Flow Simulations with a Near-Wall Reynolds-<br />
Stress Model<br />
Axel Probst (DLR Göttingen), Ulrich Rist (Universität Stuttgart), René-Daniel Cécora, Rolf Radespiel<br />
(TU Braunschweig)<br />
Transition from laminar to turbulent flow plays a significant role in modern aircraft designs. Numerical<br />
simulations of <strong>flows</strong> around flying aircrafts still mostly rely on RANS (Reynolds-averaged<br />
Navier-Stokes) approaches which use semi-empirical closures to model turbulent flow. The most<br />
general level of RANS closures is achieved by modelling the six individual transport equations<br />
of the Reynolds-stress tensor (Reynolds-stress model, RSM). To account for near-wall turbulence<br />
effects additional low-Reynolds number damping functions can be applied which locally alter the<br />
model calibration.<br />
Our present approach uses the ε h -based near-wall RSM [1] in an extended formulation which<br />
is combined with an e N -<strong>transition</strong>-prediction method within the finite-volume flow solver DLR-<br />
TAU. Due to its DNS-based calibration the model is able to accurately predict the anisotropic<br />
Reynolds-stress <strong>and</strong> dissipation-rate profiles down to the wall. However, the damping terms were<br />
found to delay or even suppress <strong>transition</strong> in the low-disturbance environments of flying aircrafts.<br />
The simulation method is therefore extended by a novel approach to incorporate the usually neglected<br />
Reynolds-stress contributions by the unstable <strong>transition</strong>al modes into the RANS solution<br />
[2]. To derive realistic input quantities at turbulence onset a linear-stability eigenfunction analysis<br />
of the incoming laminar boundary layer is performed. It provides the wall-normal shapes of the<br />
<strong>transition</strong>al Reynolds stresses which are derived from the amplitudes <strong>and</strong> phase shifts of the most<br />
amplified Tollmien-Schlichting or crossflow wave at the end of linear amplification. Closure of<br />
the yet missing magnitudes is obtained by an additional calibration based on DNS results of an<br />
adverse-pressure-gradient flow.<br />
The talk provides a detailed overview on both the near-wall Reynolds-stress closure <strong>and</strong> the<br />
linear-stability-based <strong>transition</strong> model. To demonstrate the validity of the approach, computations<br />
of different 2D <strong>and</strong> 3D flow cases are presented, such as generic boundary layers, airfoil<br />
<strong>flows</strong> <strong>and</strong> a flow-through nacelle near stall. Moreover, a recent extension for combined Tollmien-<br />
Schlichting/crossflow <strong>transition</strong> scenarios is addressed.<br />
[1] Jakirlić, S., Hanjalić, K., A new approach to modelling near-wall turbulence energy <strong>and</strong> stress<br />
dissipation, J. Fluid Mechanics, 459 (2002), 139 – 166.
8 <strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong><br />
[2] Probst, A., Radespiel, R., Rist, U., Linear-Stability-Based Transition Modeling for Aerodynamic<br />
Flow Simulations with a Near-Wall Reynolds-Stress Model, to appear in: AIAA Journal<br />
(<strong>2012</strong>).<br />
An investigation of the separate flow <strong>and</strong> stall delay for horizontal-axis wind tubine<br />
Florin Frunzulica (POLITEHNICA University of Bucharest), Razvan Mahu (TENSOR SRL,<br />
Bucharest), Horia Dumitrescu (Institute of Mathematical Statistics <strong>and</strong> Applied Mathematics<br />
Bucharest)<br />
The flow characteristics <strong>and</strong> stall delay phenomenon of a stall regulated wind turbine rotor due to<br />
blade rotation in steady state non-yawed conditions are investigated. An incompressible Reynoldsaveraged<br />
Navier-Stokes solver is applied to carry out the separate flow cases at high wind speeds<br />
from 11 m/s to 25 m/s with an interval of 2 m/s. The objective of the present research effort is<br />
to validate a first-principles based approach for modeling horizontal-axis wind turbines (HAWT)<br />
under stalled flow conditions using NREL/ Phase VI rotor data. The computational results are<br />
compared with the predicted values derived by a new stall-delay model <strong>and</strong> blade element momentum<br />
(BEM) method.<br />
An insight into the rotational stall delay<br />
Horia Dumitrescu, Vladimir Cardos (Institute of Statistical Mathematics <strong>and</strong> Applied Mathematics<br />
Bucharest)<br />
Blade element <strong>and</strong> momentum methods (BEM) are the traditional design approach to calculate<br />
drag <strong>and</strong> lift forces of wind turbine rotor blades. The major disadvantage of these theories is<br />
that the airflow is reduced to axial <strong>and</strong> circumferential flow components. Disregarding radial flow<br />
components leads to underestimation of lift <strong>and</strong> thrus. Therefore, correction models for rotational<br />
effects are often used in the case of the stall controlled rotors at a constant rotation speed. At<br />
inboard locations, there is a strong interaction between the fast rotating flow of wake <strong>and</strong> the 3-D<br />
boundary layer close to the blade surface rotating with an angular velocity smaller than that of<br />
the fluid. This behaviour is visible from the streamlines over the blade surface during operation in<br />
deep stall. The knowledge extracted from the physical mechanism of 3-D rotational effects can be<br />
then used to develop an improved BEM model for the design of stall control-wind turbine rotor<br />
blades. In this study the pressure fields generated by the wake <strong>and</strong> blade are superimposed <strong>and</strong><br />
the main contributions for the rise of the three-dimensional <strong>and</strong> rotational effects are described.<br />
Analytical <strong>and</strong> Numerical Modelling of the Safe Turn Manoeuvres of Agricultural<br />
Aircraft<br />
Bosko Rasuo (University of Belgrade)<br />
In this paper, a theoretical study of the turn manoeuvre of an agricultural aircraft is presented.<br />
The manoeuvre with changeable altitude is analyzed, together with the, effect of the load factors<br />
on the turn manoeuvre characteristics during the field-treating flights. The mathematical model<br />
used describes the procedure for the correct climb <strong>and</strong> descent turn manoeuvre. For a typical<br />
agricultural aircraft, the numerical results <strong>and</strong> limitations of the climb, horizontal <strong>and</strong> descending<br />
turn manoeuvre are given. The problem of turning flight with changeable altitude is described<br />
by the system of differential equations which describe the influence of the normal <strong>and</strong> tangential<br />
load factors on velocity, the path angle in the vertical plane <strong>and</strong> the rate of turn, as a function of<br />
the bank angle during turning flight. The system of differential equations of motion was solved<br />
on a personal computer with the Runge-Kutta-Merson numerical method. Some analytical <strong>and</strong><br />
numerical results of this calculation are presented in this paper.
<strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> 9<br />
Ariel treating has become an integral part of modern agriculture. However, agricultural flying<br />
has been plagued by a great number of accidents. The manoeuvres of an agricultural aircraft<br />
are divided into those carried out while entering or leaving the spraying line. Despite low height<br />
of the aeroplane while spraying, this part of the flight is considered to be the safest because<br />
of an appreciable flight velocity. Upon completing a spraying run, the aircraft enters the turn<br />
manoeuvre procedure.<br />
The low altitude of the turn manoeuvre procedure <strong>and</strong> the vicinity of terrain are main causes<br />
of numerous accidents. The pilots assert that the procedure is the most dangerous manoeuvre<br />
<strong>and</strong> most of the accidents occur when these manoeuvres are performed, due to low altitude <strong>and</strong><br />
the possibility of stall during the manoeuvres. There are many secondary factors that influence<br />
the safety of agricultural flying <strong>and</strong> some of them will be treated in this paper.<br />
In this paper a criterion has been established for determining the margin of the speed over the<br />
stalling speed (safety speed) after the agricultural aeroplane increases its height above the ground<br />
by a given amount. The required altitude may be different for different types of aeroplanes <strong>and</strong><br />
will depend on their capability to perform rolling <strong>and</strong> turning manoeuvres. The minimum margin<br />
of velocity allowed is determined from the requirements of the rolling manoeuvre.<br />
A numerical study of vortex structures behind an harbor seal vibrissa<br />
Daniel Matz, Albert Baars (Bionik Innovations Centrum)<br />
Harbor seals (Phoca vitulina) use whiskers (vibrissa) to detect prey by their trailing wake. These<br />
whiskers are not circular cylinders, but show wavy elliptical structures in spanwise direction.<br />
This geometry is found to substantially reduce vortex shedding in the wake of the vibrissa in<br />
comparison to circular cylinders <strong>and</strong> elliptical structures. In this work we want to contribute to<br />
the question, to what extent wave length <strong>and</strong> amplitude of the shape are optimized for reduction<br />
of self induced oscillations. Therefore, numerical flow simulations at Re = 230 are performed to<br />
investigate the influence of amplitude <strong>and</strong> wavelength on vortex structures, drag <strong>and</strong> lift coefficient,<br />
as well as the Strouhal number. The 3D calculations are carried out with a finite volume<br />
code with discretization of second order in space <strong>and</strong> time. The block structured grids consists of<br />
around 1 · 10 7 volumes. For the basic geometry the amplitude of the lift coefficient range lower by<br />
a factor of 120 in comparison to a cylinder <strong>and</strong> a factor of 30 in comparison to an ellipse. This is in<br />
accordance with literature. The separated shear layer in the wake of the vibrissa forms complex<br />
3D flow pattern, which show a periodical structure in spanwise direction. For overflow length<br />
greater than 800 this structure gets unstable <strong>and</strong> deforms in spanwise direction. This influences<br />
the temporal progression of drag <strong>and</strong> lift coefficient.<br />
S9.4: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> IV Wed, 16:00–18:00<br />
Chair: Martin Oberlack / Florian Kummer, Stefan Braun S1|01–A2<br />
A discontinuous Galerkin solver for steady incompressible <strong>flows</strong> based on the SIM-<br />
PLE algorithm<br />
Benedikt Klein, Florian Kummer (TU Darmstadt)<br />
For the numerical simulation of incompressible <strong>flows</strong> the finite volume method (FVM) <strong>and</strong> the<br />
continuous finite element method (FEM) are widely used. Besides, a newer method, the discontinuous<br />
Galerkin method (DGM), which has got favorable properties of both the FVM <strong>and</strong> the<br />
FEM, is becoming more popular. The DGM provides a convergence order of O(∆x k+1 ), where k<br />
is the order of the approximating polynomials.<br />
When simulating incompressible <strong>flows</strong> one has to deal with certain difficulties, like the nonlinearity<br />
in the momentum equation, a strong coupling between velocity <strong>and</strong> pressure <strong>and</strong> the lack
10 <strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong><br />
of an explicit equation for the pressure. The well-known SIMPLE algorithm, which was originally<br />
proposed by Patankar <strong>and</strong> Spalding [1], has shown to be very efficient in the context of the FVM<br />
<strong>and</strong> the FEM [2]. For the SIMPLE algorithm, by introducing an iterative process the discrete<br />
equations are linearized <strong>and</strong> decoupled. An equation for the pressure, more precisely speaking,<br />
for the pressure correction is derived on the discrete level.<br />
Using a discontinuous Galerkin discretization of the momentum <strong>and</strong> continuity equation [3],<br />
we present how the SIMPLE algorithm can be adapted to the DGM. Various test cases are carried<br />
out, which show the expected convergence rate of k + 1.<br />
[1] S.V. Patankar <strong>and</strong> D.B Spalding, A calculation procedure for heat, mass <strong>and</strong> momentum<br />
transfer in three-dimensional parabolic <strong>flows</strong>, Int. J. Heat Mass Transfer 15 (1972), 1787 –<br />
1806.<br />
[2] V. Haroutunian, M.S. Engelman <strong>and</strong> I. Hasbani, Segregated finite element algorithms for the<br />
numerical solution of large-scale incompressible flow problems, Int. J. Numer. Meth. Fl. 17<br />
(1993), 323 – 348.<br />
[3] K. Shahbazi, P.F. Fischer <strong>and</strong> C.R. Ethier, A high-order discontinuous Galerkin method for<br />
the unsteady incompressible Navier-Stokes equations, J. Comput. Phys. 222 (2007), 391 –<br />
407.<br />
Energy conserving incompressible <strong>flows</strong> on collocated <strong>and</strong> distorted grids<br />
Julius Reiss (TU Berlin)<br />
An energy preserving finite difference scheme for incompressible, constant density <strong>flows</strong> is presented.<br />
It is based on the idea of the skew-symmetric formulation of the non–linear transport term<br />
of the Navier–Stokes Equation<br />
∂tuα + 1<br />
2 (div (uuα) + u · grad (uα)) + (gradp)α = 0<br />
div(u) = 0<br />
with u = (u1, u2, u3), <strong>and</strong> α = 1, 2, 3. In contrast to established schemes collocated Euclidean grids<br />
can be used while exactly preserving the energy <strong>and</strong> momentum conservation, yet avoiding the<br />
odd–even decoupling of the Laplacian of the pressure Poisson equation. The essential idea is to use<br />
different discretizations for the different derivatives in the above equations. High order derivatives<br />
in space <strong>and</strong> time can be used. The generalization to transformed grids is discussed <strong>and</strong> full<br />
conservation for arbitrary transformations in two dimensions <strong>and</strong> for restricted transformations<br />
in three dimensions is found.<br />
On a reduced mixed s-v least-squares finite element formulation for the incompressible<br />
Navier-Stokes equations<br />
Alex<strong>and</strong>er Schwarz, Jörg Schröder (Universität Duisburg-Essen)<br />
In the present work a mixed finite element based on a least-squares approach is proposed. Here,<br />
we consider a formulation for Newtonian fluid flow, which is described by the incompressible<br />
Navier-Stokes equations. First, a div-grad first-order system is derived resulting in a three-field<br />
approach with stresses, velocities, <strong>and</strong> pressure as unknowns. Following the idea in [1], this threefield<br />
formulation can be transformed into a reduced stress-velocity (s-v) two-field approach. The<br />
L2-norms of the residuals of the derived equations yield then the least-squares functional, which is
<strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> 11<br />
the basis for the associated minimization problem. Besides some numerical advantages, as e.g. an<br />
inherent symmetric structure of the system of equations <strong>and</strong> an error estimator, it is known that<br />
least-squares methods have also a drawback concerning accuracy, especially when lower-order<br />
elements are used, see e.g. [2,3]. Therefore, the main focus of the presentation is on performance<br />
<strong>and</strong> implementation aspects of triangular mixed finite elements with different interpolation order.<br />
In order to approximate the stresses, shape functions related to the edges are chosen. These<br />
vector-valued functions are used for the interpolation of the rows of the stress tensor <strong>and</strong> belong<br />
to a Raviart-Thomas space, which guarantees a conforming discretization of the Sobolev space<br />
H(div). Furthermore, st<strong>and</strong>ard polynomials associated to the vertices of the triangle are used for<br />
the continuous approximation of the velocities. The talk closes with some numerical examples,<br />
which focus on well-known benchmark problems for incompressible Newtonian fluid flow <strong>and</strong><br />
demonstrate the performance of the mixed finite element formulation.<br />
[1] Z. Cai, B. Lee, P. Wang, Least-squares methods for incompressible Newtonian fluid flow:<br />
linear stationary problems, SIAM J. Numer. Anal. 42 (2004), 843–859.<br />
[2] O. Kayser-Herold, Least-squares methods for the solution of fluid-structure interaction problems,<br />
PhD Thesis, Technische Universität Braunschweig (2006).<br />
[3] A. Schwarz, J. Schröder, A mixed least-squares formulation of the Navier-Stokes equations<br />
for incompressible Newtonian fluid flow, Proc. Appl. Math. Mech. 11 (2011), submitted.<br />
Allocation of the particle concentration for the SPH-method depending on the gradients<br />
of flow parameters<br />
Anika Stein, Olaf Wünsch (Universität Kassel), Markus Rütten (DLR Göttingen), Jens Kuenemund,<br />
Stefan Saalfeld (Universität Göttingen)<br />
The Smoothed Particle Hydrodynamics method (SPH) is a Lagrangian, mesh free method to<br />
discretize partial differential equations like the Navier-Stokes-Equation by interpolating flow properties<br />
directly at a set of particles. It was first developed 1977 by [1] <strong>and</strong> [2] for astrophysical<br />
Problems. Today it is applied more <strong>and</strong> more for mechanical problems. It is comfortable to use<br />
for fluid <strong>and</strong> multiphase flow problems, large deformation problems <strong>and</strong> free surface <strong>flows</strong> because<br />
it is possible to allocate different properties to each particle. Moreover the differential set of the<br />
Momentum-Equation is particularly suitable for complex rheological problems like polymer melts,<br />
[3]. All the information about the flow like velocity, temperature, viscosity <strong>and</strong> so on are recorded<br />
at each particle for a optional number of departed time steps. It brings a lot of advantages as<br />
described above, but another outcome of that are costs in memory <strong>and</strong> a rising need of calculation<br />
power, the more particles are inside a domain. Taking in account that in some areas of a flow field<br />
nearly nothing happens <strong>and</strong> in some areas the gradients of flow parameters are very high, it is<br />
not the best choice to use the same particle concentration at those different regions. In this paper<br />
a method is presented to optimise this number of particles according to the gradients of the flow<br />
parameters. The functional principle of this operation is to generate particles at domains with<br />
highly alternate flow properties <strong>and</strong> to turn them out where they are not needed. This algorithm<br />
is able to generate more accurate solutions, which is shown by different examples like a leaked<br />
tank or a breaking dam. Finally the influence of the procedure is discussed.<br />
[1] R. A. Ginglod <strong>and</strong> J. J. Monaghan, Smoothed particle hydrodynamics theory <strong>and</strong> application<br />
to non-spherical stars, Mon. Not. R. Astron. Soc. 181, 375 (1977)
12 <strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong><br />
[2] L. B. Lucy, A numerical approach to the testing of the fission hypothesis, Astron. J. 83, 1013<br />
(1977)<br />
[3] M. Ellero, Smoothed Particle Dynamics Methods for the Simulation of Viscoelastic Fluids,<br />
Dissertation, Universität Berlin,(2004), urn:nbn:de:kobv:83-opus-7658<br />
Internal flow analysis for slow moving small droplets in contact with rough surfaces<br />
Raheel Rasool, Roger A. Sauer, Muhammad Osman (RWTH Aachen)<br />
Motivated by the self-cleaning phenomena, internal fluid flow behavior for slow moving small<br />
droplets in contact with rough surfaces is analyzed. The shape of the droplet is first computed<br />
using the Young-Laplace equation. For this purpose a Finite Element (FE) model [1], in which<br />
contact constraints are enforced through Penalty <strong>and</strong> Augmented Lagrange Multiplier methods,<br />
is used. The flow field within the droplet is then analyzed through the Stokes flow model, constituting<br />
a decoupled approach. Similar to the membrane deformation model, the formulation for<br />
the flow analysis is also expressed in the framework of FE analysis. Both, stabilized (Pressure<br />
Stabilizing/Petrov-Galerkin PSPG) <strong>and</strong> Galerkin FE formulations are considered. The motion<br />
of the fluid inside the droplet is governed by the slip condition enforced on the membrane of<br />
the droplet. Numerical examples for droplets rolling steadily on smooth <strong>and</strong> rough surfaces are<br />
presented.<br />
[1] M. Osman <strong>and</strong> R.A. Sauer, A two-dimensional computational droplet contact model, Proc.<br />
Appl. Math. Mech., 11 (2011), 103-104.<br />
Pattern formation <strong>and</strong> mixing in three-dimensional film flow<br />
Thilo Pollak, Christian Heining, Nuri Aksel (Universität Bayreuth)<br />
The effect of inertia on gravity-driven free surface flow over different three-dimensional periodic<br />
corrugations is considered analytically, numerically <strong>and</strong> experimentally. In the case of high bottom<br />
undulations the results predict complex free surface structures especially in cases where the<br />
topography is not fully flooded by the liquid film. The investigation of the flow field shows a rich<br />
variety of pattern formation phenomena depending on the interplay between the geometry of the<br />
topography <strong>and</strong> the inertia of the film. Finally, we show how the complex topographical structure<br />
enhances the laminar mixing within the film.<br />
S9.5: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> V Thu, 13:30–15:30<br />
Chair: Ulrich Rist S1|01–A2<br />
Modelling study of turbulent-to-laminar <strong>transition</strong>al features of a strongly heated<br />
pipe flow<br />
S. Jakirlic (TU Darmstadt), R. Jester-Zuerker (Voith Hydro Holding GmbH Co. KG-tts, Heidenheim)<br />
A flow in a circular pipe subjected to increasingly enhanced wall heating is computationally investigated<br />
by means of a differential, near-wall second-moment closure model based on the solution<br />
of transport equations for second moments of the fluctuating velocities <strong>and</strong> temperature, u ′′<br />
i u′′<br />
j <strong>and</strong><br />
u ′′<br />
i<br />
θ respectively. Both Reynolds stress model <strong>and</strong> heat flux model represent wall-topography free<br />
formulations with quadratic pressure-strain term <strong>and</strong> pressure-temperature-gradient correlation.
<strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> 13<br />
The transport equations for the turbulent stress tensor <strong>and</strong> the turbulent heat flux are solved in<br />
conjunction with the equation governing a novel length-scale determining variable, the so-called<br />
homogeneous dissipation rate, Jakirlic <strong>and</strong> Hanjalic (2002, J. Fluid Mech., 539:139-166). Such an<br />
approach offers a number of important advantages: proper near-wall shape of the dissipation rate<br />
profile was obtained without introducing any additional term <strong>and</strong> the correct asymptotic behaviour<br />
of the stress dissipation components by approaching the solid wall is fulfilled automatically<br />
without necessity for any wall geometry-related parameter. In order to account for the influence<br />
of the temperature field <strong>and</strong> associated fluid property variation on the velocity field, the Favreaveraged<br />
equations for mass, momentum <strong>and</strong> energy are solved. The temperature dependence on<br />
viscosity <strong>and</strong> heat conductivity is defined via a power-law formulations, while Pr<strong>and</strong>tl number<br />
P r <strong>and</strong> specific heat at constant pressure Cp were kept constant. Density is evaluated from the<br />
equation for ideal gas.<br />
The flow configuration considered presently, representing a vertical circular tube with air flowing<br />
in upward direction, was experimentally investigated by Shehata <strong>and</strong> McEligot (1998, Int. J.<br />
Heat <strong>and</strong> Mass Transfer, 41:4297-4313) <strong>and</strong> by means of DNS by Satake et al. (2000, Int. J. Heat<br />
<strong>and</strong> Fluid Flow, 21:526-534) <strong>and</strong> Bae et al. (2006, Physics of Fluids, 18(075102)). After a portion<br />
of a fully-developed pipe flow (length = 4D, with D being the pipe diameter) with constant wall<br />
temperature Θw the air enters a 30D-long pipe subjected to intensive heating (with negligible<br />
buoyancy effects). The thermal boundary conditions correspond to a constant heat flux. Three<br />
different heating rates were considered q +<br />
i = 0.0018, 0.0035 <strong>and</strong> 0.0045. According to the reference<br />
data originators, these values relate to the turbulent, sub-turbulent <strong>and</strong> laminarizing regimes. In<br />
the latter case some laminarization phenomena have been observed. The influence of strong heating<br />
of a gas flow (as, e.g., encountered in gas combustors <strong>and</strong> similar high-temperature reactors) is<br />
primarily manifested through a severe variation of the fluid properties (density, viscosity) leading<br />
consequently to important structural changes. The most important changes are concentrated in<br />
the immediate wall vicinity. The strongest modification of flow structure, deviating substantially<br />
from the equilibrium conditions, occurs in the inner part of the temperature layer. Accordingly,<br />
the density decrease <strong>and</strong> viscosity increase led to the thermal boundary layer growth <strong>and</strong><br />
viscous sublayer thickening (relative to the boundary layer thickness reduction) causing the flow<br />
acceleration, which, if sufficiently strong, can suppress turbulence resulting in flow laminarization.<br />
The model results obtained follow closely the experimental <strong>and</strong> DNS findings manifested especially<br />
through the laminar-like profiles of the velocity <strong>and</strong> temperature fields. The behaviour of<br />
Reynolds stress components is in accordance with a severe suppression of the turbulence intensity<br />
due to local acceleration caused by a strong viscosity increase.<br />
Numerical <strong>and</strong> experimental investigations of thermal convection in an inclined narrow<br />
gap<br />
O. Sommer (TU Chemnitz), H. G. Heil<strong>and</strong> (SUVIS GmbH, Chemnitz), G. Wozniak (TU Chemnitz)<br />
The knowledge of the fluid behaviour in inclined cavities is of fundamental importance as far as<br />
heat <strong>and</strong> mass transfer are concerned. The interest in this subject is particulary increasing due<br />
to the rapid process in microtechnologies. We therefore studied the flow- <strong>and</strong> temperature field of<br />
such <strong>flows</strong> numerically as well as experimentally using CFD <strong>and</strong> PIV/ T, respectively. We present<br />
<strong>and</strong> discuss the numerical <strong>and</strong> experimental results of our investigations <strong>and</strong> explain the applied<br />
techniques.<br />
Gas exchange of almost leak-tight display cases<br />
Johannes Strecha, Herbert Steinrück (TU Wien)
14 <strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong><br />
A requirement for display cases for art objects is to be leak tight. However, due to design constraints<br />
there a are tiny gaps resulting in a gas exchange between the interior of the show case <strong>and</strong><br />
its environment. Usually the leak-tightness is being quantified by the so-called air exchange rate,<br />
the ratio of the gas volume exchanged between display-case <strong>and</strong> environment per unit time <strong>and</strong><br />
the volume of the display-case. Commonly the concentration of a tracer-gas in the display-case is<br />
monitored to calculate the air exchange rate. For this purpose a certain tracer-gas exchange-law is<br />
assumed, usually a linear exchange-law. We present experimental results that disqualify a linear<br />
exchange law <strong>and</strong> find that it is a special case, not applicable in general.<br />
We review the gas exchange mechanism through the gaps Taking hydro static pressure differences<br />
due to temperature <strong>and</strong> concentration differences of the tracer gas <strong>and</strong> diffusion into<br />
account a non linear exchange model is derived <strong>and</strong> validated experimentally.<br />
We conclude that in general the tracer-gas concentration has a significant influence on the gas<br />
exchange <strong>and</strong> therefore the assumption of a linear exchange-law is discouraged. Instead we suggest<br />
the introduction of two parameters: one that characterizes the air-exchange in the diffusion-driven<br />
limit <strong>and</strong> one that takes the influence of hydrostatic pressure into account. Strategies to identify<br />
these parameters will be presented <strong>and</strong> demonstrated.<br />
Non isothermal simulation of non-Newtonian flow in the shot sleeve of semi- solid<br />
die casting processes<br />
Roudouane Laouar, Olaf Wünsch (Universität Kassel)<br />
This work deals with a numerical study of the flow of metal in the semi-solid state in the shot sleeve<br />
of horizontal die casting machine during the injection process. With the discovery of shear thinning<br />
<strong>and</strong> the thixotropic behavior of partially solidified alloys under vigorous agitation, a new era in<br />
forming technology was started, namely semi-solid metal (SSM) processing. The new technology<br />
promises several important advantages in comparison with the traditional die casting processes.<br />
In the semi-solid state, metallic alloys consists of solid particles suspended in a liquid Newtonian<br />
matrix <strong>and</strong> consequently modeling approaches known from classical suspension rheology can be<br />
applied. In the equilibrium state, semi-solid alloys are shear-thinning <strong>and</strong> different descriptions in<br />
form of material equation are used in literature. In the present work, the Herschel-Bulkley model,<br />
which contains a yield stress <strong>and</strong> a shear-thinning viscosity, was used in order to demonstrate<br />
the effect of the nonlinear viscosity to the flow pattern in the shot sleeve. The used numerical<br />
model, which considers the problem as two-dimensional, is based on the conservation equations<br />
of mass <strong>and</strong> momentum, <strong>and</strong> describes the free surface using the volume-of-fluid method. The<br />
motion of plunger is simulated by using a layering dynamic mesh method. The numerical results<br />
are obtained by using a CFD code that is based in the finite volume method. The influence of<br />
different parameters as yield stress, the power law index <strong>and</strong> the temperature in the flow dynamics<br />
is to be discussed. A comparison between a Herschel-Bulkley fluid <strong>and</strong> a shear-thinning fluid with<br />
no yield stress limit is presented.<br />
Simulating of a pressing process of a viscoelastic polymer melt<br />
Ammar Al-Baldawi, Olaf Wünsch (Universität Kassel)<br />
A well known <strong>and</strong> often used method to obtain anisotropic polymer films is the so-called pressing<br />
process. Here, films are squeezed under high temperatures, pressure <strong>and</strong> deformation rates. To<br />
simulate such a process, the polymeric matrix is treated as a non-Newtonian, viscoelastic melt.<br />
Experimental investigations of it predict a shear thinning <strong>and</strong> elongational hardening/softening<br />
behavior. The modeling of this behavior is done with a generalized Maxwell Model. Where the<br />
generalization is obtained using a Phan-Thien <strong>and</strong> Tanner anisotropic molecule movement tensor<br />
for high deformation rates [1,2].
<strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> 15<br />
Simulating this process leads to a hyperbolic equation set of mass conservation, momentum<br />
balance <strong>and</strong> material model. Therefore, the simulation needs to be stabilized; here the DEVSS<br />
method is used. Furthermore, the ALE method is used to interpolate between the Euler <strong>and</strong><br />
Lagrange description method in connection with a cell-layering method to obtain big changes in<br />
the calculation domain.<br />
In this work we present some simulations to show the difference between the classical approaches<br />
using a generalized Newtonian viscosity to model the polymeric matrix <strong>and</strong> the viscoelastic<br />
model. Here, the major difference is shown to be the pressure field <strong>and</strong> its influence on the velocity<br />
field <strong>and</strong> the extra stress tensor. For this end we use a flow type parameter to show the elongation<br />
types in the regions <strong>and</strong> the differences [1].<br />
[1] A. Al-Baldawi, O. Wünsch, Some new aspects of the invariants of the rate of deformation<br />
tensor <strong>and</strong> their application on viscoelastic polymer melts, Accepted for publication in<br />
Technische Mechanik (2011)<br />
[2] O. Wünsch, <strong>Laminar</strong> Fluid Flow with Complex Material Behavior in Devices of Mechanical<br />
Engineering, Int. Journal of Emerging Multidisciplinary Fluid Sciences, 1-4, 255-267 (2009)<br />
S9.6: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> VI Thu, 16:00–18:00<br />
Chair: Suad Jakirlic S1|01–A2<br />
Direct numerical simulation of MHD duct flow at high Reynolds number<br />
Dmitry Krasnov (TU Ilmenau), Oleg Zikanov (University of Michigan), Thomas Boeck (TU Ilmenau)<br />
Evolution of turbulent flow of an incompressible, electrically conducting fluid is studied numerically<br />
in a square duct subjected to a uniform magnetic field B. The magnetic field is applied in<br />
the vertical (wall-normal) direction, the walls are perfectly insulating. The governing equations<br />
are the Navier-Stokes system with the additional Lorentz force term j × B, where j is the electric<br />
current. There are two governing parameters, the Reynolds number Re = UqL/ν <strong>and</strong> the Hartmann<br />
number Ha = BL σ/ρν, which characterizes the strength of the applied magnetic field B.<br />
Here Uq are the mean flux velocity, L is the duct half-width <strong>and</strong> σ is the electrical conductivity.<br />
The Joule dissipation selectively damps out fluctuations of velocity perpendicular to the magnetic<br />
field that can result into anisotropy of turbulent eddies. For strong magnetic fields the<br />
anisotropy can evolve into 2D structures stretched along the direction of the magnetic field. Two<br />
major ingredients are necessary to achieve the 2D states: (i) the Reynolds number Re should<br />
be large, that amounts to intensive turbulent fluctuations <strong>and</strong> (ii) the interaction parameter<br />
N = Ha 2 /Re should exceed 1, which also means strong magnetic fields.<br />
In our simulations Re = 100000 <strong>and</strong> Ha = 0 ... 400. For the present study a series of DNS was<br />
performed at the grid resolution of 2048 × 769 × 769 points that amounts to more than 1 billion<br />
points as a problem size. The numerical method is based on highly conservative finite-difference<br />
discretization of the second order, the flow solver is hybrid-parallel (both MPI <strong>and</strong> Open MP<br />
interfaces).<br />
As Ha increases the flow transforms from nearly isotropic turbulence at Ha = 0 to a spatial<br />
anisotropy at Ha > 200. At Ha = 300 the core flow becomes essentially laminar, the turbulence<br />
remains small-scale near the side walls, but becomes large-scale, weak, <strong>and</strong> strongly anisotropic<br />
towards the core flow. Finally, at Ha = 400 the fluctuations die out <strong>and</strong> the flow becomes laminar.<br />
The quasi-2D structures have been identified in a clear-cut way by applying the so-called
16 <strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong><br />
lambda-2 criterion. The results of the lambda-2 visualization at Ha = 300 <strong>and</strong> 350 show a region<br />
with clearly expressed 2D structures stretched along the magnetic field. We have also found<br />
transformation of the mean velocity similar to our previous study on channel flow under spanwise<br />
magnetic field. This behavior is observed in the cross-section perpendicular to the magnetic field<br />
for a range Ha ≈ 100 ... 200. During this transformation the classical log-layer almost disappears<br />
<strong>and</strong> is replaced by a linear dependence.<br />
Visualisation of the Ludford column<br />
André Thess (TU Ilmenau), Oleg Andreev (Forschungszentrum Dresden-Rossendorf)<br />
The formation of TTaylor columnsïn rotating <strong>flows</strong> is well known: When a liquid <strong>flows</strong> over a<br />
truncated cylinder in a rotating systems, a stagnant region forms above the cylinder. It has been<br />
known for quite some time that an analogous phenomenon, the LLudford columnëxists when a<br />
liquid metal <strong>flows</strong> across a truncated cylinder under the influence of a magnetic field parallel<br />
to the axis of the cylinder. Since liquid metals are opaque, it is impossible to visualise Ludford<br />
columns. Using an electrolyte instead of a liquid metal <strong>and</strong> a high magnetic field created by<br />
a superconducting magnet we visualise for the first time the Ludford column <strong>and</strong> discuss their<br />
properties. We discuss further ways in which optical flow measurement can be applied to better<br />
underst<strong>and</strong> magnetohydrodynamic <strong>flows</strong>.<br />
Separation of magnetic particles in channel <strong>flows</strong> by BEM<br />
J. Ravnik, M. Hriberek (University of Maribor), F.Vogel, P. Steinmann (Universität Erlangen-<br />
Nürnberg)<br />
In-line separation of suspensions can become difficult in in case of particles with comparable values<br />
of densities. For <strong>flows</strong> in micro devices in such cases gravitational settling is inefficient, <strong>and</strong> other<br />
separation techniques must be applied. In case of magneto active particles, the action of Kelvin<br />
magnetic force in a non-uniform magnetic field could be used in order to achieve a higher degree of<br />
particles separation. The contribution therefoe deals with Euler-Lagrangian formulation of dilute<br />
two-phase <strong>flows</strong>. The Boundary element based computational algorithm solves the incompressible<br />
Navier-Stokes equations written in velocity-vorticity formulation. The nonuniform magnetic field<br />
was defined analytically for the case of a set of long thin wires. The particle trajectories were<br />
computed by applying the 4th order Runge-Kutta method. The computed test case consisted of<br />
a narrow channel with laminar flow of suspension under Re=1-10. Particle trajectories under the<br />
influence of a nonuniform magnetic field were computed for the case of magnetite <strong>and</strong> aluminium<br />
particles suspended in water. The efficiency of separation on basis of particle trajectories for different<br />
values of Re number <strong>and</strong> magnetic field strength was performed, clearly indicating superior<br />
separation of magneto active particles.<br />
Experimental investigation of the electrokinetic flow in microchannels with internal<br />
electrodes<br />
Carsten Gizewski, Peter Ehrhard (TU Dortmund)<br />
In microfluidic devices, electrokinetic phenomena can be engaged to manipulate liquids, particles,<br />
or cells. In general, electrokinetic phenomena are related to the existence of electrical double<br />
layers (EDL), which are present e.g. where solid walls are in contact with electrolytes. Due to<br />
surface charges of the solid, ions of opposite charge are attracted <strong>and</strong> lead to a thin electrically<br />
non-neutral zone the EDL. The application of an electrical field, consequently, leads to forces<br />
onto the fluid inside the EDL, capable of driving a flow within the microchannel. This particular<br />
flow is termed electroosmotic. If further, the electrodes are placed inside the microchannel, due
<strong>Section</strong> 9: <strong>Laminar</strong> <strong>flows</strong> <strong>and</strong> <strong>transition</strong> 17<br />
to small distances, strong inhomogeneous electrical fields can be induced, which in turn cause<br />
complex flow fields. This is true despite low applied electrode potentials of a few Volts. Numerical<br />
simulations of various authors have shown the potential for pumping <strong>and</strong> mixing of such complex<br />
<strong>flows</strong> in microchannels with internal electrodes.<br />
We focus on the electroosmotic flow within rectangular microchannels of 100 x 200 µm cross<br />
section. In each microchannel eight pairs of electrodes are placed onto the top <strong>and</strong> bottom glass<br />
covers, whereas the offset of the electrodes is chosen differently in each of the microchannels. Due<br />
to the limited optical access through the glass covers, only the two velocity components which<br />
are tangential to the glass cover are accessible by means of the micro-particle-image velocimetry<br />
(µPIV). The expected electroosmotic flow, however, features vortices which cannot be recognized<br />
within this velocity plane. Therefore, a number of two-dimensional, two-component velocity<br />
fields are measured at different heights of the microchannel. From an integration of the continuity<br />
equation, subsequently, the third velocity component, which is normal to the glass cover, can<br />
be determined at reasonable accuracy. A further difficulty arises from the fact that the microparticles,<br />
used for µPIV, are not electrically neutral. Hence, in addition to drag forces from the<br />
electroosmotic flow, they experience electrophoretic forces. Hence, the particle movement appears<br />
to be a superposition of electroosmotic <strong>and</strong> electrophoretic effects.<br />
Flow characterization in a bioaffinity enrichment system for detection of relevant<br />
microorganisms in food<br />
A. Osorio Nesme, R. Benning, A. Delgado, (Universität Erlangen-Nürnberg)<br />
In food industry the quality assurance <strong>and</strong> consumer protection represent essential requirements<br />
for preserving high product ratings <strong>and</strong> competitiveness. Decreases in food quality or risks to<br />
consumers health must be properly detected in time to avoid image damage to the companies<br />
or risks from the product liability. In particular, the detection of microorganisms is of great<br />
importance. In general, this can be carried out by the routine microbiological diagnostic, whose<br />
negative results can be obtained only after 24 (Staphylococcus aureus) or 48 hours (Bacillus<br />
cereus). Furthermore, the confirmation of positive samples can take up to 144 hours. From the<br />
perspective of the current state of art, this analysis time could be for the microorganisms S.<br />
aureus <strong>and</strong> B. cereus significantly reduced by means of the development <strong>and</strong> combination of new<br />
analytical techniques. In the present study, a new system for direct detection of S. aureus <strong>and</strong><br />
B. cereus (spores) through bioaffinity enrichment is introduced by means of a fully automated<br />
selective-microarray device (microporous columns) for milk <strong>and</strong> whey. The system consists of<br />
a monolithic column with a microporous structure, in which biological receptors (monoclonal<br />
antibodies or aptamers) are immobilized on the surface. These receptors have a specific interaction<br />
with the microorganisms (bioaffinity). The matrix (milk) <strong>flows</strong> through the monolithic column,<br />
allowing the microorganisms to come in contact with the receptors <strong>and</strong> get bound to the column<br />
surface. It has been found that the amount of microorganisms captured during the process depends<br />
not only on the binding kinetics but also on the flow characteristics. High flow rates signify<br />
less residence time of the microorganism in the column <strong>and</strong> therefore less probability of getting<br />
captured. The flow velocity <strong>and</strong> flow distribution along the column have a direct impact on the<br />
binding process (microorganism enrichment). An important part of the present work consists of<br />
the optimization of the column geometry by means of numerical simulations. The influence of the<br />
inlet form of the monolithic column on both flow <strong>and</strong> pressure distribution is investigated.