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©ZeusNumerix
Defense | Nuclear Power | Aerospace | Infrastructure | Industry
Brief introduction on the importance of
Fluid Mechanics in CFD
Abhishek Jain
abhishek@zeusnumerix.com
Fluid Mechanics in CFD
Perspective
©ZeusNumerix
Some initial thoughts
2
©ZeusNumerix
Fluid Mechanics and its branches
3
Analysis tool Year 1600 1700 1800 1900 2000
Experimental
Theoretical
Computational
Theoretical –
write eqns.
for flow
Experimental
methods
Computational
Fluid dynamics
Validate the
prediction
Hypothesis
Predict the flow
©ZeusNumerix
Theoretical Fluid Dynamics
 Most important branch of fluid dynamics
 Crucial in understanding concepts (Example: Lift =
ρUxΓ)
 Compressible flow in a converging diverging nozzles
 Usually good in predicting trends (Example: δ ~ Re-1/2)
 Can generate a lot of information using simple
assumptions (SR-71 Blackbird was designed completely
using theoretical Fluid Dynamics)
 However, theoretical fluid dynamics requires insight
which requires extensive training and several years of
experience
 The idea is to incorporate as much fluid dynamics as
possible in tools and only manual work is carried out by
some one with some very essential background in fluid
dynamics
©ZeusNumerix
Computing power required to
resolve the flow
6
Method
Scale of
turbulence
Resolution required
Surface
points
Wake
points
Time
steps
Total
operations
Direct Navier
Stokes (DNS)
No modeling 1016 1017 108 1025
Large Eddy
Simulation (LES)
Sub-grid
modeling
1012 109 108 1020
LES with wall
layer
Near wall &
sub-grid
modeling
1010 109 107 1017
Reynolds Navier
Stokes (RANS)
All scales are
modeled
107 107 104 1011
Euler equation
Scales are
absent
107 107 103 1010
Inviscid vortex
based methods
Scales are
absent
102 102 103 105
Computational cost of analysis of a wing of AR=10, Re=5 x 106
©ZeusNumerix
Physics of Flows
7
©ZeusNumerix
8
Physics of Incompressible flow
 Incompressible flow is governed by:
 Conservation of mass (continuity equation)
u/x + v/y + w/z = 0 (1)
 Conservation of momentum (Euler equation)
(u/t + uu/x + vu/y + wu/z) + p/x = 0 (2)
( v/t + uv/x + vv/y + wv/z )+ p/y = 0 (3)
 (w/t + uw/x + vw/y + ww/z) + p/z = 0 (4)
 Density is a constant. Temperature does not take part in the
motion of the flow
 Heat energy of an element, e or temperature, T (if Cp is constant)
is convected as if ‘T’ is an independent attribute of fluid not
related to its motion
©ZeusNumerix
9
 In incompressible flows, the kinetic energy may get converted
in to internal energy (heat), but not vice versa.
 Due to large value of specific heat capacity of liquids
temperature changes due to loss of kinetic energy is not
appreciable
 Thus only four equations (accounting for viscosity) are
adequate for solution of incompressible fluid motion . The
energy equation is required to be coupled with eqn of motion.
It would be in fact wrong to simultaneously solve for them.
Physics of Incompressible flow
©ZeusNumerix
10
Peculiarity of Partial Differential
Equations
 In principle eqns. (2) to (4) ( slide 7)can be used to correct u, v
and w from their guesses (initial condition)
 What can be done so that pressure can be corrected from its
initial condition ? Note that a term p/t does not exist.
 Mathematically, treatment for p must be different from the
treatment to be given to u, v and w
 Interestingly, p/x, p/y and p/z appear in the equations,
but pressure, p does not appear in any of the equations. Thus
the solution does not change if p = p + constant
©ZeusNumerix
11
Physics of Compressible flow
 Compressible flow is governed by:
 Conservation of mass (continuity equation)
/t + (u)/x + (v)/y + (w)/z = 0 (1)
 Conservation of momentum (Euler equation)
(u)/t + (u2)/x + (uv)/y + (uw)/z + p/x = 0 (2)
(v)/t + (uv)/x + (v2)/y + (vw)/z + p/y =
0 (3)
(w)/t + (uw)/x + (vw)/y + (w2)/z + p/z =
0 (4)
 Conservation of energy equation
(E)/t + (u(E+p))/x + (v(E+p))/y + (w(E+p))/z = 0
(5)
©ZeusNumerix
12
E =  (e + ½ u2)
E = internal energy (e) + kinetic energy (½ u2)
 In principle eqns. (1) to (5) can be used to correct , u, v, w and
E (or e) from their guesses (initial condition)
 What can be done so that pressure can be corrected from its
initial condition ? Note that there is no equation for p. This is
where equation of state (EoS) can be used
p = (-1)(E- ½ u2)
 Note that equations do have p as well as p/x, p/y and
p/z. Hence solution depends on pressure, p.
Physics of Compressible flow
©ZeusNumerix
13
 There 6 unknown (, u, v, w, e and p) and 5 partial differential
equations + one algebraic equations; i.e. the problem is well
posed.
 Interestingly, compressible CFD prefers to choose internal
energy, e as a variable and hence equation of state is p = (-
1)(E- ½ u2) and not the conventional p = RT
 In compressible flows, internal energy can be converted to
mechanical and kinetic energy and vice versa. Thus
momentum equation can not be considered as conservation of
momentum equation.
 Though not stated explicitly, the second law of
thermodynamics must be obeyed.
Peculiarity of Partial Differential
Equations
©ZeusNumerix
Solving problems using CFD in 6 steps
3
2
Build Computational
Domain
Create suitable
Mesh
Boundary Conditions &
Initial conditions
Solution of discrete
equationsPlot flow FieldInterpret solution
These steps will be discussed in detail in this workshop
©ZeusNumerix
 Identify the computational domain
 Generate the correct type of mesh
 Structured or Unstructured mesh or hybrid mesh
 Set up Simulation
 Assign boundary conditions, initial conditions, etc
 Execute the solver
 Choose accuracy, Viscous/In-viscid, Laminar /
Turbulent, Incompressible / compressible, etc
 Post-process the data
 Organize data and understand results
 Understand the fluid dynamics
 Do the results make any sense? Is the design
correct?
 Note that at every step, good understanding of
theoretical fluid dynamics is essential!
In brief the steps are…
©ZeusNumerix
CFD – Computational Tool
©ZeusNumerix
CFD – The Computational Tools
 CFD tools are required for solving industrial problems
 Emphasis is on economy of solution without sacrificing the
required accuracy
 Advances are in tools is linked to other branches of
technology; e.g. storage devices
 Tools are for getting rid of manual work
 Tools must capture as much physics as possible from first
principle
 They must a part of larger suite of simulation technologies
such as FEM, CEM, etc. being used by the engineering
fraternity
 Measure of success – the ease with which diverse problems
can be solved
©ZeusNumerix
Four important Tools of CFD
0
10
20
30
40
50
60
70
80
Days
CAD Grids Solution Post_processing
0
1
2
3
4
5
6
7
Days
CAD Grids Solution Post_processing
0
20
40
60
80
100
120
140
160
180
Minutes
CAD Grids Solution Post_processing
Source : Catherine M. Maskyumiuk, et. al.
Application of CFD in Aeronautics at NASAAMES Research Centre,
pp 57-67, NASA CP 3291, 1995
 Importance of the tools in
Calendar time spent in a
CFD cycle
 Creating / Repairing Geometry
 Discretising Domain
 Numerical Simulation
 Post-processing the Data
Case #2
Case #3
Case #1
©ZeusNumerix
CAD Geometry
 Importance of Geometry in CFD
 CFD tools can become a commodity in CAE only if CAD data can be read
 Geometry fidelity is an essential element in CFD, Retain the details that matter for
simulation
 Errors in CAD data in the form of gaps, overlaps, non-physical protrusions is expensive
CAD data with gaps, overlaps, etc. geometry ready for meshing
©ZeusNumerix
Sponge analogy: Transform a 2D
domain in to a rectangle (and 3D
domain to a box) by a suitable affine
transformation
Grid Generation
Structured Grids
One-to-one mapping
How to divide the domain into
collection of rectangular blocks?
Assembly of simple shapes : Fill a
given domain with simple shapes such
as triangles so that the given domain is
fully covered
Emphasis is on cells there are grid points
but no continuous lines or what can be
called as grid lines.
Un-structured Grids
A good mesh is half the solution – Kordulla (Frontiers of CFD 2002)
©ZeusNumerix
0
10
20
30
40
50
60
70
80
0thdimension
1D
Axisymmetric
2DSingleBody
2DUnsteady
2DMulti-Body
3DSingleBody
3DMulti-Body
0
10
20
30
40
50
60
70
80
90
100
Viscosity
HeatTransfer
Compressibility
Non-Newtonian
Conjugateheattransfer
ReactiveFlows
PhaseChangemodelling
Turbulencemodelling
Writing a Two Dimensional problem
constitutes CFD of one year duration
Reactive Flows pose a greater challenge than
viscosity or compressibility alone
Modeling turbulence and phase change
are a research fields
Three Dimensional Problems
are very complex to solve
Numerical Algorithms for
Differential Eqns.
Normally taught in
universities
©ZeusNumerix
Advection of massless particle from one point to another obeys two
differential equation
Position = Position |t =0 + (t) velocity
D(colour)/Dt = C 2(color concentration)
Post-processing
The purpose of computing is insight, not numbers
©ZeusNumerix
How useful is CFD?
©ZeusNumerix
Universal Challenge-Reduce Development
Cost
Where We Need to be
Current design methods: more than 70 % of project cost goes for Test-Fail-Fix cycle
Can we carry out “Test-Fail-Fix cycle” with virtual parts, sub-systems, systems?
©ZeusNumerix
CFD is one of the Key Enabling
Technologies
 The Technology Readiness Level (TRL) of
CFD has moved from TRL 1 to TRL 7
 The current Requirements
• CFD now works for “real” problems
• CFD is an engineering tool for designers and NOT ONLY for
CFD scientist
• Turnaround times is compatible with the design cycle (say)
o Conceptual design (1-2 months)
o Preliminary design (4-6 months)
o Detail design (6-9 months)
• It must produce required accuracy
• The cost must be reasonable
©ZeusNumerix
CFD as a process for engineering design
 CFD needs provide
 Flow field analysis
 Structural and thermal loads
 Approach - Use best tool available
 Use Multiple customized
 Get solutions from many software developed strategic partners, in-house,
commercial of-the-shelf, or government laboratories
 Always use hierarchical physical models (e.g. laminar flames first then
turbulent flames
 Validate and calibrate periodically
 Emphasize getting engineering solutions and not very
accurate solution
 CFD results must make sense
•
•
©ZeusNumerix
CFD Validation
 Validation is essential
 Ensure that analysis results are sufficiently reliable and accurate for intended
purposes
 Must Provide necessary confidence to the designer
 It should offer to quantify
 Code accuracy
 Code sensitivities
 Validation is a learning process for application engineers
 It is important to know what not to do
 Validation process depend on end application and the
intended use of CFD
©ZeusNumerix
Current status
 Now CFD is defined as a process of understanding flow field
 Most time consuming process are (a) CAD repair and (b)
mesh generation. Lots of benefit are possible from
automating the CAD repair and mesh generation
 Current problems size is around 20 to 30 million cells.
Complete aircraft, missile, rocket, etc can be analysed
 Turn around time for a drag polar on high performance
computers could be 24 hours
©ZeusNumerix
Technology Needs
 Extensive use of CFD requires quality data for validation.
The quality data sources are:
 Analytical solutions
 Very high fidelity simulations (e.g. DNS)
 Benchmark experiments
 Subcomponent Component tests and system tests
 Validation is industry specific. Validation
for aerospace applications can not be
derived form automobile industry
 Validation is continuous process
©ZeusNumerix
Recommended texts
 Introduction to Computational Fluid Dynamics, A.W. Date, Cambridge
 Computational Fluid Dynamics, Anderson, JD
 An introduction to Computational Fluid Dynamics, W. Malasekara, H. K.
Versteeg
 Computational Methods for Fluid Dynamics, J. H. Ferziger & M. Peric,
Spinger
 Computational Gas Dynamics, Cubert B. Laney, Cambridge university Press
 Handbook of Computational Fluid Mechanics, Roger Peyret
 Numerical Computation of Internal and External Flows (2 volumes), C.
Hirsch, John Wiley & Sons
 Numerical Simulation in Fluid Dynamics – A practical Introduction, Michael
Griebel, et.al., Siam
 Numerical Methods for Conservation Laws, RJ Le Veque, Birkhauser Verlag
 Principles of Computational Fluid Dynamics, Pieter Wesseling, Spinger
 Riemann Solvers and Numerical Methods for Fluid Dynamics, Toro, E.F.,
Springer
©ZeusNumerix
Thank You!
3 November 2014 31

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Fluid Mechanics in CFD Perspective

  • 1. ©ZeusNumerix Defense | Nuclear Power | Aerospace | Infrastructure | Industry Brief introduction on the importance of Fluid Mechanics in CFD Abhishek Jain abhishek@zeusnumerix.com Fluid Mechanics in CFD Perspective
  • 3. ©ZeusNumerix Fluid Mechanics and its branches 3 Analysis tool Year 1600 1700 1800 1900 2000 Experimental Theoretical Computational Theoretical – write eqns. for flow Experimental methods Computational Fluid dynamics Validate the prediction Hypothesis Predict the flow
  • 4. ©ZeusNumerix Theoretical Fluid Dynamics  Most important branch of fluid dynamics  Crucial in understanding concepts (Example: Lift = ρUxΓ)  Compressible flow in a converging diverging nozzles  Usually good in predicting trends (Example: δ ~ Re-1/2)  Can generate a lot of information using simple assumptions (SR-71 Blackbird was designed completely using theoretical Fluid Dynamics)  However, theoretical fluid dynamics requires insight which requires extensive training and several years of experience  The idea is to incorporate as much fluid dynamics as possible in tools and only manual work is carried out by some one with some very essential background in fluid dynamics
  • 5. ©ZeusNumerix Computing power required to resolve the flow 6 Method Scale of turbulence Resolution required Surface points Wake points Time steps Total operations Direct Navier Stokes (DNS) No modeling 1016 1017 108 1025 Large Eddy Simulation (LES) Sub-grid modeling 1012 109 108 1020 LES with wall layer Near wall & sub-grid modeling 1010 109 107 1017 Reynolds Navier Stokes (RANS) All scales are modeled 107 107 104 1011 Euler equation Scales are absent 107 107 103 1010 Inviscid vortex based methods Scales are absent 102 102 103 105 Computational cost of analysis of a wing of AR=10, Re=5 x 106
  • 7. ©ZeusNumerix 8 Physics of Incompressible flow  Incompressible flow is governed by:  Conservation of mass (continuity equation) u/x + v/y + w/z = 0 (1)  Conservation of momentum (Euler equation) (u/t + uu/x + vu/y + wu/z) + p/x = 0 (2) ( v/t + uv/x + vv/y + wv/z )+ p/y = 0 (3)  (w/t + uw/x + vw/y + ww/z) + p/z = 0 (4)  Density is a constant. Temperature does not take part in the motion of the flow  Heat energy of an element, e or temperature, T (if Cp is constant) is convected as if ‘T’ is an independent attribute of fluid not related to its motion
  • 8. ©ZeusNumerix 9  In incompressible flows, the kinetic energy may get converted in to internal energy (heat), but not vice versa.  Due to large value of specific heat capacity of liquids temperature changes due to loss of kinetic energy is not appreciable  Thus only four equations (accounting for viscosity) are adequate for solution of incompressible fluid motion . The energy equation is required to be coupled with eqn of motion. It would be in fact wrong to simultaneously solve for them. Physics of Incompressible flow
  • 9. ©ZeusNumerix 10 Peculiarity of Partial Differential Equations  In principle eqns. (2) to (4) ( slide 7)can be used to correct u, v and w from their guesses (initial condition)  What can be done so that pressure can be corrected from its initial condition ? Note that a term p/t does not exist.  Mathematically, treatment for p must be different from the treatment to be given to u, v and w  Interestingly, p/x, p/y and p/z appear in the equations, but pressure, p does not appear in any of the equations. Thus the solution does not change if p = p + constant
  • 10. ©ZeusNumerix 11 Physics of Compressible flow  Compressible flow is governed by:  Conservation of mass (continuity equation) /t + (u)/x + (v)/y + (w)/z = 0 (1)  Conservation of momentum (Euler equation) (u)/t + (u2)/x + (uv)/y + (uw)/z + p/x = 0 (2) (v)/t + (uv)/x + (v2)/y + (vw)/z + p/y = 0 (3) (w)/t + (uw)/x + (vw)/y + (w2)/z + p/z = 0 (4)  Conservation of energy equation (E)/t + (u(E+p))/x + (v(E+p))/y + (w(E+p))/z = 0 (5)
  • 11. ©ZeusNumerix 12 E =  (e + ½ u2) E = internal energy (e) + kinetic energy (½ u2)  In principle eqns. (1) to (5) can be used to correct , u, v, w and E (or e) from their guesses (initial condition)  What can be done so that pressure can be corrected from its initial condition ? Note that there is no equation for p. This is where equation of state (EoS) can be used p = (-1)(E- ½ u2)  Note that equations do have p as well as p/x, p/y and p/z. Hence solution depends on pressure, p. Physics of Compressible flow
  • 12. ©ZeusNumerix 13  There 6 unknown (, u, v, w, e and p) and 5 partial differential equations + one algebraic equations; i.e. the problem is well posed.  Interestingly, compressible CFD prefers to choose internal energy, e as a variable and hence equation of state is p = (- 1)(E- ½ u2) and not the conventional p = RT  In compressible flows, internal energy can be converted to mechanical and kinetic energy and vice versa. Thus momentum equation can not be considered as conservation of momentum equation.  Though not stated explicitly, the second law of thermodynamics must be obeyed. Peculiarity of Partial Differential Equations
  • 13. ©ZeusNumerix Solving problems using CFD in 6 steps 3 2 Build Computational Domain Create suitable Mesh Boundary Conditions & Initial conditions Solution of discrete equationsPlot flow FieldInterpret solution These steps will be discussed in detail in this workshop
  • 14. ©ZeusNumerix  Identify the computational domain  Generate the correct type of mesh  Structured or Unstructured mesh or hybrid mesh  Set up Simulation  Assign boundary conditions, initial conditions, etc  Execute the solver  Choose accuracy, Viscous/In-viscid, Laminar / Turbulent, Incompressible / compressible, etc  Post-process the data  Organize data and understand results  Understand the fluid dynamics  Do the results make any sense? Is the design correct?  Note that at every step, good understanding of theoretical fluid dynamics is essential! In brief the steps are…
  • 16. ©ZeusNumerix CFD – The Computational Tools  CFD tools are required for solving industrial problems  Emphasis is on economy of solution without sacrificing the required accuracy  Advances are in tools is linked to other branches of technology; e.g. storage devices  Tools are for getting rid of manual work  Tools must capture as much physics as possible from first principle  They must a part of larger suite of simulation technologies such as FEM, CEM, etc. being used by the engineering fraternity  Measure of success – the ease with which diverse problems can be solved
  • 17. ©ZeusNumerix Four important Tools of CFD 0 10 20 30 40 50 60 70 80 Days CAD Grids Solution Post_processing 0 1 2 3 4 5 6 7 Days CAD Grids Solution Post_processing 0 20 40 60 80 100 120 140 160 180 Minutes CAD Grids Solution Post_processing Source : Catherine M. Maskyumiuk, et. al. Application of CFD in Aeronautics at NASAAMES Research Centre, pp 57-67, NASA CP 3291, 1995  Importance of the tools in Calendar time spent in a CFD cycle  Creating / Repairing Geometry  Discretising Domain  Numerical Simulation  Post-processing the Data Case #2 Case #3 Case #1
  • 18. ©ZeusNumerix CAD Geometry  Importance of Geometry in CFD  CFD tools can become a commodity in CAE only if CAD data can be read  Geometry fidelity is an essential element in CFD, Retain the details that matter for simulation  Errors in CAD data in the form of gaps, overlaps, non-physical protrusions is expensive CAD data with gaps, overlaps, etc. geometry ready for meshing
  • 19. ©ZeusNumerix Sponge analogy: Transform a 2D domain in to a rectangle (and 3D domain to a box) by a suitable affine transformation Grid Generation Structured Grids One-to-one mapping How to divide the domain into collection of rectangular blocks? Assembly of simple shapes : Fill a given domain with simple shapes such as triangles so that the given domain is fully covered Emphasis is on cells there are grid points but no continuous lines or what can be called as grid lines. Un-structured Grids A good mesh is half the solution – Kordulla (Frontiers of CFD 2002)
  • 20. ©ZeusNumerix 0 10 20 30 40 50 60 70 80 0thdimension 1D Axisymmetric 2DSingleBody 2DUnsteady 2DMulti-Body 3DSingleBody 3DMulti-Body 0 10 20 30 40 50 60 70 80 90 100 Viscosity HeatTransfer Compressibility Non-Newtonian Conjugateheattransfer ReactiveFlows PhaseChangemodelling Turbulencemodelling Writing a Two Dimensional problem constitutes CFD of one year duration Reactive Flows pose a greater challenge than viscosity or compressibility alone Modeling turbulence and phase change are a research fields Three Dimensional Problems are very complex to solve Numerical Algorithms for Differential Eqns. Normally taught in universities
  • 21. ©ZeusNumerix Advection of massless particle from one point to another obeys two differential equation Position = Position |t =0 + (t) velocity D(colour)/Dt = C 2(color concentration) Post-processing The purpose of computing is insight, not numbers
  • 23. ©ZeusNumerix Universal Challenge-Reduce Development Cost Where We Need to be Current design methods: more than 70 % of project cost goes for Test-Fail-Fix cycle Can we carry out “Test-Fail-Fix cycle” with virtual parts, sub-systems, systems?
  • 24. ©ZeusNumerix CFD is one of the Key Enabling Technologies  The Technology Readiness Level (TRL) of CFD has moved from TRL 1 to TRL 7  The current Requirements • CFD now works for “real” problems • CFD is an engineering tool for designers and NOT ONLY for CFD scientist • Turnaround times is compatible with the design cycle (say) o Conceptual design (1-2 months) o Preliminary design (4-6 months) o Detail design (6-9 months) • It must produce required accuracy • The cost must be reasonable
  • 25. ©ZeusNumerix CFD as a process for engineering design  CFD needs provide  Flow field analysis  Structural and thermal loads  Approach - Use best tool available  Use Multiple customized  Get solutions from many software developed strategic partners, in-house, commercial of-the-shelf, or government laboratories  Always use hierarchical physical models (e.g. laminar flames first then turbulent flames  Validate and calibrate periodically  Emphasize getting engineering solutions and not very accurate solution  CFD results must make sense • •
  • 26. ©ZeusNumerix CFD Validation  Validation is essential  Ensure that analysis results are sufficiently reliable and accurate for intended purposes  Must Provide necessary confidence to the designer  It should offer to quantify  Code accuracy  Code sensitivities  Validation is a learning process for application engineers  It is important to know what not to do  Validation process depend on end application and the intended use of CFD
  • 27. ©ZeusNumerix Current status  Now CFD is defined as a process of understanding flow field  Most time consuming process are (a) CAD repair and (b) mesh generation. Lots of benefit are possible from automating the CAD repair and mesh generation  Current problems size is around 20 to 30 million cells. Complete aircraft, missile, rocket, etc can be analysed  Turn around time for a drag polar on high performance computers could be 24 hours
  • 28. ©ZeusNumerix Technology Needs  Extensive use of CFD requires quality data for validation. The quality data sources are:  Analytical solutions  Very high fidelity simulations (e.g. DNS)  Benchmark experiments  Subcomponent Component tests and system tests  Validation is industry specific. Validation for aerospace applications can not be derived form automobile industry  Validation is continuous process
  • 29. ©ZeusNumerix Recommended texts  Introduction to Computational Fluid Dynamics, A.W. Date, Cambridge  Computational Fluid Dynamics, Anderson, JD  An introduction to Computational Fluid Dynamics, W. Malasekara, H. K. Versteeg  Computational Methods for Fluid Dynamics, J. H. Ferziger & M. Peric, Spinger  Computational Gas Dynamics, Cubert B. Laney, Cambridge university Press  Handbook of Computational Fluid Mechanics, Roger Peyret  Numerical Computation of Internal and External Flows (2 volumes), C. Hirsch, John Wiley & Sons  Numerical Simulation in Fluid Dynamics – A practical Introduction, Michael Griebel, et.al., Siam  Numerical Methods for Conservation Laws, RJ Le Veque, Birkhauser Verlag  Principles of Computational Fluid Dynamics, Pieter Wesseling, Spinger  Riemann Solvers and Numerical Methods for Fluid Dynamics, Toro, E.F., Springer

Editor's Notes

  1. E=Hydraulics-pipe flows, channel flows, intuitive relations Theoretical=Formulation of equations CFD=to start with Laplace eqn , human agents computing in 1900 etc Cycle continues If theoretical and computational solution do not match with experimental, we need to modify theoretical formulations For simple flows the cycle has stabilized For complex flows : like unsteady, hypersonic or combustion, multi-phase, bio-flows etc formulations are still evolving
  2. Multi scale : DNS, : no assumption, only continuum LES : sufficiently large to reduce computation , but smallest size is such that unsteadyness of the given type of flow is captured. E.g in case of flow in weather prediction, the size could be several meters, and in case of flow around a wing, the size would be of the micron order. LES with wall layer: walls constrain fluctuations ( V, V’) RANS: I recognise my computiing power. Now instead of fluctuations, I only model the effect of fluctuations. E.g Kinetic energy ( u’2+v’2+w’2 ) this is 1 eqn turbulence model rate at which K is destroyed : epsilon ( as K cannot be growing always . So it has to be balanced with growth) Current flavour : RANS Next 5 years : LES with wall layer Eulers eqn are used in Aerospace only : as no viscosity , only compressibility matters Incompressible/Invsicid =Laplace : outdated Kolmogorov scales – smallest scale in continuum
  3. Fluid= gas+liquid Conservation of mass = conservation of volume ( rho is constant) More correctly it should be (u/x + v/y + w/z) = 0 In eulerian : there is another problem Lagrangian: cell moves with flow. Deform yes, but volume remains In euler: I draw in volume space, flow moves across Then why eulerian: permits conservation . Temperature is like color, no role in flow Thus fluid mechanics separated from Heat transfer where conduction and radiation are considered. Convection is only used thru empirical formulae. Now with CFD : heat+fluid flow together Now CpT (energy per unit volume) is variable along with mass, momentum Earlier T was only measured and hence variable but that is only the effect.
  4. How do I get pressure guess. There was no way how to guess better p Another issue: the eqn only shows gradient of p, but not the absolute value of p. This would create both mathematical anamoly and physical meaninglessness. In fact , in incompressible flow , there is at least some semblance of meaning. But in compressible flow this will be very crucial. In fact , only about 30 years ago, a hack was developed by Patankar of IITB , along with Spalding at UK SIMPLE : algorithm will be explained by next lectures ;
  5. P=RT is standard eqn of state. But we do not have T as variable. We consider energy i.e e internal energy Thus It is reduced to p = (-1)(E- ½ u2) Kg/m3 ( ) (
  6. Special methods to take care of 2nd law. So ensure entropy is not negative. Shock results in entropy growth Incompressile flow methods cannot handle this. That is why separate ays for compressible, and incompressible One may ask: Is incompressible a special case of compressibel? NO The model is different. In deed even the physics is. Sound and matter move at drastically different speeds. If compressible is made a special case into incompressible : assumptions will be violated Perhaps , computers with very high capacity may be able to use models that capture these radical differences.
  7. Iggest headache: interpretation Common mistake: e.g presuure differene But user may use absolute values. Say 10 values of pr at inlet, 10 values of pr at outlet. In fact equations govern only the gradient. So absolute value may be floating ( subtract pr) Another mistake Habit of listing the variables and their beautiful plots In fact ranges of values given to visualizer will show gradients where values may be ( in absolute terms) very much same ( contour plot of density: interpret density) ( incompressible flow should not show any variation, let alone beautiful plot )
  8. Examples : whether viscocity needed if only lift : inviscid solution is fine if drag also needed: viscosity is a must. May be RANS Academically : cavity: how many vortices, whether separation etc In industry : different concersm Academic problem of Driven cavity : 2-d, 3-d If I need Cl, Cd , Cm of 0.001 level accuracy, why go for fine mesh e.G : an industrial problem: Centre of pressure : every time different. In 3-d , no centre of pressure. So could not give load for structural analysis which takes data of load only as CP.
  9. CFD ready cad : negotiate the correct geometry : e.g landing gear, angle of tail deflection . Cl, Cd, Cm : Many permutations for arriving at the angle of attack, tail deflections . Add to that flap deflection, landing gear deflection, aileron deflection. The user has to agree. Currently Automobile: CAD repair : months Solution: days Postprocessing : days Similarly Wing : days But aircraft: solution may take long Business cycles : intermediate sign offs
  10. Not flow field but only analysis Not the pressure distribution all over but the loads on body