fluid mechanics as a prominent discipline of application for numerical
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1 1. fluid mechanics as a prominent discipline of application for numerical simulations: experimental fluid mechanics: wind tunnel studies, laser Doppler anemometry, hot wire techniques,... theoretical fluid mechanics: investigations concerning the derivation of turbulence models, e.g. computational fluid mechanics (CFD): numerical simulations many fields of application: aerodynamics: aircraft design, car design,... thermodynamics: heating, cooling,... process engineering: combustion material science: crystal growth astrophysics: accretion disks Page 1 of 13
2 2. Some Small Part of the World... fluids and flows: ideal or real fluids ideal: no resistance to tangential forces compressible or incompressible fluids think of pressing gases and liquids viscous or inviscid fluids think of the different characteristics of honey and water Newtonian and non-newtonian fluids the latter may show some elastic behaviour (e.g. in liquids with particles like blood) laminar or turbulent flows turbulence: unsteady, 3D, high vorticity, vortices of different scales, high transport of energy between scales typically: all require different models Page 2 of 13
3 3. real, incompressible, viscous, Newtonian, laminar starting point: continuum mechanics basic conservation laws (remember heat conduction in the modelling section): conservation of mass and momentum with the transport theorem and Newton s second law, we get mass conservation/continuity equation: ρ + div(ρ u) = 0 t momentum conservation/momentum equations (ρ u) + ( u grad)(ρ u) + (ρ u)div u ρ g divσ = 0 t above quantities: u = (u, v, w) three-dimensional velocity, ρ density, g gravity, σ tension tensor, u div( u) = + v x ( gradp = p, p x + w, y z, p y z ). Page 3 of 13
4 4. 2 What to do with the tensor σ? viscous case: not diagonal due to friction forces Newtonian case: isotrope, Stokes postulate hence: pressure p and viscosity ν appear divσ gradp ν u incompressible case: density is constant ρ + div(ρ u) = 0 div( u) = 0 t (ρ u)div( u) = 0 introducing Reynolds number Re (dimensionless, essentially reciprocal of viscosity and some scaling), we finally get the famous Navier-Stokes equations: 1 u + ( u grad) u + gradp = u + g t Re div u = 0 two coupled PDE, nonlinear involving velocity and pressure, 1. and 2. spatial derivatives Page 4 of 13
5 5. 3 what about boundary conditions? no-slip: The fluid can not penetrate the wall and sticks to it u = 0. free-slip: The fluid can not penetrate the wall but does not stick to it u n = 0, u n = 0. inflow: Both tangential and normal velocitiy components are prescribed u = u inflow. Page 5 of 13
6 6. 4 what about boundary conditions? (continued) outflow: All velocity components do not change in normal direction u = 0. n periodic: Same velocity and pressure at inlet and outlet u in = u out. Page 6 of 13
7 7. The Numerical Treatment Spatial Derivatives discretization scheme: Finite Differences (can be shown to be equivalent to Finite Volumes, here) grid: strictly orthogonal staggered grid spatial derivatives: Laplacian u: standard 5- or 7-point stencil u( x i,j ) u i 1,j + u i,j 1 4u i,j + u i+1,j + u i,j+1 h 2. u( x i,j,k ) u i 1,j,k +u i,j 1,k +u i,j,k 1 6u i,j,k +u i+1,j h 2 Page 7 of 13
8 8. Finite Differences (continued): spatial derivatives (continued): first p derivatives gradp, div u: central differences (x i,j,k ) p 1 i+ 2,j,k p i 1 2,j,k x 1 h derivatives of nonlinear terms ( u grad) u: mixture of central derivatives and Donor-Cell-scheme Page 8 of 13
9 9. explicit Euler scheme (simple, but stability restrictions) u (n+1) = u (n) + dt ( 1 Re u(n) ( u (n) grad ) u (n) + g gradp ) coupling of equations: Chorin s projection method; leads to a Poisson equation for the pressure u (n+ 1 2 ) = u (n) + dt ( 1 Re u(n) ( u (n) grad ) ) u (n) + g, p = 1 dt div u(n+ 1 2 ), u (n+1) = u (n+ 1 2 ) dt gradp. solution of SLE (Poisson-equation for pressure p): SOR MG Page 9 of 13
10 10. geometry representation as a flag field (cf. Marker-and-Cell) flag field: input data (boundary conditions) and output data (computed results) as arrays Page 10 of 13
11 11. modular C-code parallelization: simple data parallelism, domain decomposition straightforward MPI-based parallelization target architectures: (real) parallel computers clusters (NOW) The rest is (some ) programming! Page 11 of 13
12 12. techniques: all the stuff discussed before: isosurfaces orthoslices streamlines streaklines particle tracing... finally some examples for visualized flows: Page 12 of 13
13 13. Studying this simulation cycle for CFD as presented very shortly here will be the topic of next semester s practical Computational Science and Engineering and Visualization. There, you will develop your own simple simulation code and run your own fluid flow simulations, including some pretty pictures and movies to see what you ve done. In addition to that, you will meet again many of the topics discussed in this introductory course during the CSE program in more detail, and related to other topics or applications. For now, that s all see you! Page 13 of 13
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