virtual experiments: numerical computations as a powerful
TRANSCRIPT
Virtual Experiments: Numerical Computations Virtual Experiments: Numerical Computations as a Powerful Tool for Engineers
P Schmitz* 1 4 A Cockx 2 4 S Geoffroy 3 4 and J Gunther 1 4P. Schmitz* 1 4, A. Cockx 2 4, S. Geoffroy 3 4 and J. Gunther 1 4
1 Biochemical Engineering Dpt., 2 Chemical Engineering Dpt.,
3 Mechanical Engineering Dpt. 4 Université de Toulouse;
INSA,UPS,INP; 135 Avenue de Rangueil, F-31077 Toulouse, France
*Corresponding author: [email protected]
135 avenue de Rangueil – 31077 Toulouse cedex 4, France – Tel : 05.61.55.94.35 - www.insa-toulouse.fr
Presented at the COMSOL Conference 2009 Milan
INSA: National Institute of Applied Sciences
In Toulouse• 2100 Students • 500 Graduates each year 500 Graduates each year • More than 500 Foreign Students • 223 Permanent Academic Staff • 10 Engineering Specialities 10 Engineering Specialities • 9 Research Laboratories
RouenStrasbourg
RouenStrasbourg
Toulouse
Lyon
Rennes
Toulouse
Lyon
Rennes
INSA Network
135 avenue de Rangueil – 31077 Toulouse cedex 4, France – Tel : 05.61.55.94.35 - www.insa-toulouse.fr
INSA Network
Virtual Experiments Course
INSA Toulouse Teaching
Secondary Education INSA
Maths,2 3 4 51Year
Physics,Chemistry…
Stage 1 Stage 3Stage 2
BAC
Stage 1Basic
Stage 3Expert
Stage 2Pre-Expert
135 avenue de Rangueil – 31077 Toulouse cedex 4, France – Tel : 05.61.55.94.35 - www.insa-toulouse.fr
Bachelor Master
Virtual Experiments
INSA Toulouse Teaching: Course details
Course
1st Year 2nd year Pre-orientation
4th year Specialization
5th year Engineer
3rd year Pre-orientation
Chemical & Env.
Biochem.Scientific Basis
ICBE Chemic, Bio, Environ
Chemical
Biochem.
Civil Eng.
Mechanical Eng.
Systems Eng.
Basis
Humanities
IC Construction Engineering
IMACS
Civil Eng.
Mechanic Eng
Control Elec
TRAI
TRAI
TRAI
TRAI
Control, Electrical
Physics
Computer Sciences
Humanities
Personal
IMACSMaterial, Compon., Syst.
MIC
Control, Elec
Physics
Computers
NING
NING
NING
NING
135 avenue de Rangueil – 31077 Toulouse cedex 4, France – Tel : 05.61.55.94.35 - www.insa-toulouse.fr
Math, models
Network, Telec.
Personal Options Modeling, Information
Communication.Math, models
Network, Telec.
Virtual Experiments Course
Objective: To initiate student to multiphysics numerical simulation by approaching concrete cases
Outline: - Quick description of Finite Element Method- 4 projects performed by students (about 10h each)4 projects performed by students (about 10h each)
1 N l
2. Application of buoyancy to airship (Aerospace
Adour Technologie)1. Natural convection in a pan(www.nanoscience.info)
Adour Technologie)
3. Hollow fiber cartridge fil
4. Heat exchanger(www.directindustry.fr)
135 avenue de Rangueil – 31077 Toulouse cedex 4, France – Tel : 05.61.55.94.35 - www.insa-toulouse.fr
to filter tap water (Dom source)
2. Application of buoyancy to airshipFA
• Buoyancy force
FG
Buoyancy force • Gravity force due to natural convection
Static of fluid t idoutside
Combined incompressible NS equation and convection diffusion heat transfer equation
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inside
Application of buoyancy to airshipz
Quiescent fluid with gravitational
1st step : buoyancy analysis Pressure around a sphere
• Quiescent fluid with gravitational force
• Pressure map in the fluid obtained with N-S equations
npwith N S equations
• Integrate the pressure to obtain the buoyancy force
• Recover the Archimede law by yvarying properties
dSenpF
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dSe.npF zA
T t d t li
Application of buoyancy to airship
Temperature and streamlines 2nd step : thermal coupling Flow induced by thermal convection
•Coupling N-S and heat transfer with the Boussinesq approximation •Buoyancy force calculated by surface
Re < 40 pressure integration•Weight calculated by volume integration
Discussion on the available force of
dVg)T(F
Discussion on the available force of the airship
135 avenue de Rangueil – 31077 Toulouse cedex 4, France – Tel : 05.61.55.94.35 - www.insa-toulouse.fr
dVg)T(FG
Real Filter Simplified Model
3. Hollow fiber cartridge to filter tap water
• Regular arrangement of cylinders
• The fluid flow is
Hollow fiber module
p
• The fluid flow is calculated on a unit cell of this arrangement
H l’ f f S b di i i iCartridge
Happel’s free surface model *:
• The inner cylinder consists of one single hollow fiber
Sub-divising into sub cells
hollow fiber
• The outer cylinder is a fluid envelope with a free surface used to account for packing
Hollow fiber
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2D modelaccount for packing effect
* Happel, Viscous flow relatives to array of cylinders, AIChe, 1959
Hollow fibers
Hollow fiber cartridge to filter tap water
1st step : Fluid flow without particles•Coupling Navier Stokes and Darcy Brinkman model
•Good agreement with experimental results
750
p
•Discussion on flow rate values
DRextz DRextz
h-1.m
-2] 450
600
ow
rate
In / Out filtration
II MM EE LII MM EE L
J [l
.
150
300
Numerical data
Flo/ Out t at o
Out / In filtration
135 avenue de Rangueil – 31077 Toulouse cedex 4, France – Tel : 05.61.55.94.35 - www.insa-toulouse.fr
rr
[%]
0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.90
Experimental data
Packing density
Hollow fiber cartridge to filter tap water
2nd step : Fluid flow with particles2nd step : Fluid flow with particles
•Coupling Navier Stokes and Darcy Brinkman model
DRextz DRextz
•Particles follow the streamlines
•Using moving mesh ALE to In / Out filtration
II MM EE LII MM EE L
model cake formation/ Out t at o
Out / In filtration
135 avenue de Rangueil – 31077 Toulouse cedex 4, France – Tel : 05.61.55.94.35 - www.insa-toulouse.fr
rr
Hollow fiber cartridge to filter tap water
2nd step : Fluid flow with particles2nd step : Fluid flow with particles
At what time should we replace the filter cartridge?
0,12t=10 II
0,12
len
ght
[m]
0,06
0,08
0,10t=20t=30
t len
ght
[m]
0,06
0,08
0,10t=0t=10t=20t=30
t
Fib
re l
0,00
0,02
0,04
(a)
50 40 30 20 10 0
Fib
re l
0,00
0,02
0,04
(c)
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Cake height [µm]
50 40 30 20 10 0OO Cake height [µm]
50 40 30 20 10 0OO
4. Heat Exchanger
• heated cylinder cooled by a laminar fluid flow heated cylinder cooled by a laminar fluid flow • external flow normal to the axis of the circular
cylinder
• fluid-thermal coupling :combined incompressible NS equation and convection diffusion heat transfer equation
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1st step : circular cylinder in a cross flow,
Heat Exchanger
Re < 40 Re > 40
p y ,isothermal condition
Stagnation point,Rise in pressure
St d fl U t d flSteady flow• Two symmetric vortex
Unsteady flow• Karman vortex street observed with a
repeating pattern of swirling vortices. • Period of the vortex shedding
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M. Schäfer & S. Turek, ‘Benchmark computations of laminar flow around cylinder’, E.H. Hirschel (editor), Flow Simulation with High-Performance Computers II, 547–566, 1996.
Comparison with literature results
2nd step : introduction of thermal coupling fl d h t d li d
Heat Exchanger
1.5Temperature and streamlines
flow around a heated cylinder
0.5
1
ln(N
u)
Numerical Data
Hilpert Correlation
01 1.5 2 2.5 3 3.5
ln(Re)
Hilpert Correlation
Re < 40
• Maximum of the local heat flux at the stagnation point
• Total heat flux calculated by integration of the normal local
• Several fluids studied Correlations of the overall average Nusselt
number obtained• Very good agreement between numerical
135 avenue de Rangueil – 31077 Toulouse cedex 4, France – Tel : 05.61.55.94.35 - www.insa-toulouse.fr
integration of the normal local heat flux on the whole cylinder Nusselt number
Very good agreement between numerical results and Hilpert Correlation
Conclusions
COMSOL Multiphysics: a useful tool for teachersCOMSOL Multiphysics: a useful tool for teachers
-To illustrate physical phenomenaex: buoyancyex: buoyancy
fluid flow / porous media flow convection heat transfer
To approach techniques of numerical simulation-To approach techniques of numerical simulationgeometry,mesh, boundary conditions, solver, postprocessing
In order to initiate future engineers to
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gmultiphysics numerical simulation
Thank youy
135 avenue de Rangueil – 31077 Toulouse cedex 4, France – Tel : 05.61.55.94.35 - www.insa-toulouse.fr
Natural Convection in a pan