The Finite Volume Method: Basic Principles and Examples
Transcription
The Finite Volume Method: Basic Principles and Examples
The Finite Volume Method: Basic Principles and Examples Mainak Chowdhury Indian Institute of Technology,Kanpur, KANPUR (UP) - 208016. Email: [email protected] Under the guidance of Dr. Gautam Biswas IIT Kanpur Mainak Chowdhury (IIT Kanpur) December 15, 2009 1 / 49 Overview 1 Introduction 2 Diffusion: The steady case 3 Diffusion: The non-steady case 4 Diffusion and Convection 5 Acknowledgements Mainak Chowdhury (IIT Kanpur) December 15, 2009 2 / 49 Outline 1 Introduction 2 Diffusion: The steady case 3 Diffusion: The non-steady case 4 Diffusion and Convection 5 Acknowledgements Mainak Chowdhury (IIT Kanpur) December 15, 2009 3 / 49 What is finite volume method and what does it solve? A finite volume method (FVM) is a prescription for spatial discretization of a continuous system of differential equations. The basic idea of FVM is that volume integrals of divergence terms can be represented as surface integrals. (Divergence theorem) The quantities at the surface can be approximated using different interpolation techniques from discrete data(control variables). Mainak Chowdhury (IIT Kanpur) December 15, 2009 4 / 49 What is finite volume method and what does it solve? A finite volume method (FVM) is a prescription for spatial discretization of a continuous system of differential equations. The basic idea of FVM is that volume integrals of divergence terms can be represented as surface integrals. (Divergence theorem) The quantities at the surface can be approximated using different interpolation techniques from discrete data(control variables). Ok. . . what kind of equations are we talking about? Mainak Chowdhury (IIT Kanpur) December 15, 2009 4 / 49 The Conservation Equation Consider a control volume n δΩ v Figure: Definition of a control volume Then for a conserved scalar U, ∂ ∂t R Ω UdΩ + H ∂Ω (U(~v .~n) − κ∇(U).~n)dS = Mainak Chowdhury (IIT Kanpur) R Ω QV dΩ + H ∂Ω (Q~S .~n)dS December 15, 2009 5 / 49 The Conservation Equation Consider a control volume n δΩ v Figure: Definition of a control volume Then for a conserved scalar U, ∂ ∂t R Ω UdΩ + H ∂Ω (U(~v .~n) − κ∇(U).~n)dS = R Ω QV dΩ + H ∂Ω (Q~S .~n)dS This equation is the fundamental equation of many flow problems where U is typically the momentum, energy, or density The problem is steady when the time derivative is zero and non steady otherwise. Mainak Chowdhury (IIT Kanpur) December 15, 2009 5 / 49 Outline 1 Introduction 2 Diffusion: The steady case 3 Diffusion: The non-steady case 4 Diffusion and Convection 5 Acknowledgements Mainak Chowdhury (IIT Kanpur) December 15, 2009 6 / 49 A 1-D steady diffusion problem Let us consider a special case of conservation equation in one dimension. dU d (κ ) + QV = 0 dx dx Mainak Chowdhury (IIT Kanpur) (1) December 15, 2009 7 / 49 A 1-D steady diffusion problem Let us consider a special case of conservation equation in one dimension. dU d (κ ) + QV = 0 dx dx Let us see how we can solve this equation. Mainak Chowdhury (IIT Kanpur) (1) December 15, 2009 7 / 49 A 1-D steady diffusion problem Let us consider a special case of conservation equation in one dimension. dU d (κ ) + QV = 0 dx dx Let us see how we can solve this equation. (1) Node δx₂ δx₁ Uw x₁ Up x₂ Ue x Δx Control volume Discretize the domain: Here the points xi divide the domain of definition into several control volumes Mainak Chowdhury (IIT Kanpur) December 15, 2009 7 / 49 A 1-D steady diffusion problem (Contd.) Integrate the diffusion equation over each control volume: This yields Z x2 d dU ( (κ ) + QV )dx = 0 (2) dx x1 dx This can be simplified as dU dU (κ )x2 − (κ )+ dx dx x1 Z x2 QV dx = 0 (3) x1 Assume an interpolation profile: A linear function between nodes will lead to the following equation κx2 Ue − Up Up − Uw − κx1 + QV ∆x = 0 δx2 δx1 (4) where QV represents the average value of QV over the control volume. Mainak Chowdhury (IIT Kanpur) December 15, 2009 8 / 49 A 1-D steady diffusion problem (Contd.) Source term linearization: If we assume QV = QVc + QVp Up (5) the equation corresponding to each control volume becomes ap Up = ae Ue + aw Uw + b (6) ap = ae + aw − QVp ∆x κx2 ae = δx2 κx1 aw = δx1 b = QVc ∆x (7) where Mainak Chowdhury (IIT Kanpur) (8) (9) (10) December 15, 2009 9 / 49 Some issues regarding aforementioned scheme Choice of the interpolating function Positivity of coefficients Boundedness of the iterations: A sufficient condition is that P |anb | ≤1 ap where anb stands for coefficients of neighbouring terms to point p. Choice of control nodes(structured/unstructured) Mainak Chowdhury (IIT Kanpur) December 15, 2009 10 / 49 Some issues regarding aforementioned scheme Choice of the interpolating function Positivity of coefficients Boundedness of the iterations: A sufficient condition is that P |anb | ≤1 ap where anb stands for coefficients of neighbouring terms to point p. Choice of control nodes(structured/unstructured) But is the above system of equations completely determined? Mainak Chowdhury (IIT Kanpur) December 15, 2009 10 / 49 The Boundary Conditions They can be specified in a variety of ways: Dirichlet Neumann A combination of the above The boundary conditions enter the linear equations as source terms. Mainak Chowdhury (IIT Kanpur) December 15, 2009 11 / 49 The Boundary Conditions They can be specified in a variety of ways: Dirichlet Neumann A combination of the above The boundary conditions enter the linear equations as source terms. Together with the boundary conditions, the linear system of equations is completely determined and is solvable by sparse matrix or iterative techniques. Mainak Chowdhury (IIT Kanpur) December 15, 2009 11 / 49 Extension to 2 dimensions Let us consider the Laplace equation in two dimensions: ∂2φ ∂2φ + =0 ∂x 2 ∂y 2 (11) The control volume is now C j+1 D C' j+1/2 D' j B A j-1/2 B' A' j-1 i i+1 i+1/2 i-1/2 i-1 Figure: The Control Volume ABCD Mainak Chowdhury (IIT Kanpur) December 15, 2009 12 / 49 Solving the Laplace equation Consider the integral: Z Z ( ABCD ∂2φ ∂2φ + )dxdy = 0 ∂x 2 ∂y 2 By Green’s theorem, the above expression is equivalent to I ∂φ ∂φ ( dy − dx) = 0 ∂x ∂y The line integral is over the boundary of ABCD and can be approximately evaluated as the length of each segment times the value of the partial derivative at the midpoint of the segment. Mainak Chowdhury (IIT Kanpur) December 15, 2009 13 / 49 Solving the Laplace equation The integral form of the Laplace equation applied to ABCD yields ∂φ ∂φ ∂φ ∂φ |i,j− 1 ∆yAB − |i,j− 1 ∆xAB + |i+ 1 ,j ∆yBC − | 1 ∆xBC 2 2 2 ∂x ∂y ∂x ∂y i+ 2 ,j ∂φ ∂φ ∂φ ∂φ + |i,j+ 1 ∆yCD − |i,j+ 1 ∆xCD + + |i− 1 ,j ∆yDA − | 1 ∆xDA = 0 2 2 2 ∂x ∂y ∂x ∂y i− 2 ,j Estimating the derivatives at the intermediate points: One way of doing this is to assign the average value of the partial derivative over the control volume to its central point. This yields the following expressions ∂φ 1 |i,j− 1 ≈ 2 ∂x AreaA0 B 0 C 0 D 0 ∂φ 1 | 1 ≈ ∂y i,j− 2 AreaA0 B 0 C 0 D 0 Mainak Chowdhury (IIT Kanpur) Z Z Z Z ∂φ 1 ( )dxdy = ∂x AreaA0 B 0 C 0 D 0 I ∂φ 1 ( )dxdy = − ∂y AreaA0 B 0 C 0 D 0 φdy I December 15, 2009 φdx 14 / 49 Solving the Laplace equation The right hand side of the last equation can be approximated as I φdy ≈ φi,j−1 ∆yA0 B 0 + φB ∆yB 0 C 0 + φi,j ∆yC 0 D 0 + φA ∆yD 0 A0 A0 B 0 C 0 D 0 Similarly I A0 B 0 C 0 D 0 φdx ≈ φi,j−1 ∆xA0 B 0 + φB ∆xB 0 C 0 + φi,j ∆xC 0 D 0 + φA ∆xD 0 A0 The area A0 B 0 C 0 D 0 can be approximated as |A~0 B 0 x A~0 D 0 | = ∆xAB ∆yj−1,j − ∆yAB ∆xj−1,j Mainak Chowdhury (IIT Kanpur) December 15, 2009 15 / 49 Solving the Laplace equation Assume Distance between coordinate lines constant locally Intermediate value is the average of node values at the corners,i.e., 1 φA = (φi−1,j−1 + φi−1,j + φi,j + φi,j−1 ) 4 The above assumptions give a linear equation in the unknowns at a node and its surrounding nodes Thus, we have gi,j φi,j + gi−1,j+1 φi−1,j+1 + gi,j+1 φi,j+1 + gi+1,j+1 φi+1,j+1 + gi−1,j φi−1,j + gi+1,j φi+1,j + gi−1,j−1 φi−1,j−1 + gi,j−1 φi,j−1 + gi+1,j−1 φi+1,j−1 = 0 The g’s depend on the geometry of the mesh, more specifically on the ∆x’s and ∆y ’s. Mainak Chowdhury (IIT Kanpur) December 15, 2009 16 / 49 Some observations The finite volume method in 2 dimensions presented so far, offers an unifying framework to deal with differential equations, irrespective of the grid coordinate system By allowing flexibility in the choice of the coordinate system, the boundary conditions can be more accurately represented, than in finite difference methods. Mainak Chowdhury (IIT Kanpur) December 15, 2009 17 / 49 Simulations: The 2D Laplace equation Consider the Laplace equation : ∇2 φ = 0 defined on the following: θ=π/2 r=1 r=0.1 θ=0 Figure: The domain of definition The boundary condition is given by: φ= Mainak Chowdhury (IIT Kanpur) sin(θ) r December 15, 2009 18 / 49 The exact solution The exact solution corresponding to the above conditions is given by: φ= sin(θ) r It is plotted below: "EXACT_LAPLACE.OUT" using 1:2:3 10 8 6 4 2 0 1 0.8 0 Mainak Chowdhury (IIT Kanpur) 0.6 0.2 0.4 0.4 0.6 0.2 0.8 1 0 December 15, 2009 19 / 49 A contour plot of the solution 9.5 9 8.5 8 7.5 7 6.5 6 5.5 5 4.5 4 3.5 3 2.5 2 1.5 1 0.5 1 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0.1 0.2 Mainak Chowdhury (IIT Kanpur) 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1 December 15, 2009 20 / 49 Numerical Solutions The following figures were obtained for a grid obtained from triangulation of the solution region. 1.0 (solution variable - Analytical Solution) 0.24 0.18 0.8 1.0 (solution variable - Analytical Solution) 0.16 0.8 0.12 0.12 0.08 0.6 0.06 0.6 0.04 0.00 0.4 0.6 0.4 0.00 0.4 0.12 0.2 0.2 0.8 0.18 0.0 0.0 0.2 0.4 0.6 0.8 1.0 0.0 0.0 0.2 0.4 0.6 0.8 1.0 0.12 (a) Number of unknowns 448, RMS er- (b) Number of unknowns 3985, RMS ror ≈0.0316 error ≈ 0.0134 Figure: The above plots show the error of the numerical solutions on an unstructured grid. Mainak Chowdhury (IIT Kanpur) December 15, 2009 21 / 49 Numerical Solutions The following figures were obtained for a cylindrical grid in the solution region,with uniformly distributed ρ and θ. "DIFF21X21.OUT" using 1:2:3 0 -0.005 -0.01 -0.015 -0.02 -0.025 -0.03 -0.035 -0.04 -0.045 -0.05 "DIFF51X51.OUT" using 1:2:3 0 -0.001 -0.002 -0.003 -0.004 -0.005 -0.006 -0.007 1 1 0.8 0 0.6 0.2 0.4 0.4 0.6 0.2 0.8 1 0 0.8 0 0.6 0.2 0.4 0.4 0.6 0.2 0.8 1 0 (a) Number of unknowns 400, RMS er- (b) Number of unknowns 2500, RMS ror ≈0.0138 error ≈ 0.0015 Figure: The above plots show the error of the numerical solutions on a cylindrical grid. Mainak Chowdhury (IIT Kanpur) December 15, 2009 22 / 49 Observations Structure of the problem is important Finite Volume method offers a simple way of exploiting this structure. Requires coordinate transformation in finite difference methods. Mainak Chowdhury (IIT Kanpur) December 15, 2009 23 / 49 Outline 1 Introduction 2 Diffusion: The steady case 3 Diffusion: The non-steady case 4 Diffusion and Convection 5 Acknowledgements Mainak Chowdhury (IIT Kanpur) December 15, 2009 24 / 49 The time dependent 1 D diffusion with source term Retaining the time derivative in the conservation equation we get, d dU ∂U (κ ) + QV = dx dx ∂t (12) This may be rewritten as ∂U = φ(U, x) (13) ∂t The right hand side includes effects of the source term and the diffusion term. Mainak Chowdhury (IIT Kanpur) December 15, 2009 25 / 49 Temporal discretization of RHS Integrating the RHS, we have Z t+∆t φ = (f φt+∆t + (1 − f )φt )∆t t for 0≤f ≤1 I I I f=1:Fully implicit scheme f=0.5:Crank-Nicholson scheme f=0:Fully explicit scheme Explicit schemes:More stringent restrictions on time steps, no iteration required Implicit schemes:Less severe time step restrictions, requires iterations to arrive at the result Mainak Chowdhury (IIT Kanpur) December 15, 2009 26 / 49 Temporal discretization of the transient terms Consider the following integral Z Z t1 t0 ∂U dtdx ∂t This may be approximated as (U t1 − U t0 )∆x Forward Euler t1 = t + ∆t, t0 = t Backward Euler t1 = t, t0 = t − ∆t Mainak Chowdhury (IIT Kanpur) December 15, 2009 27 / 49 Temporal discretization of the transient terms(contd.) A second order scheme: 3 1 U t1 = U t − U t−∆t 2 2 3 1 U t0 = U t−∆t − U t−2∆t 2 2 Mainak Chowdhury (IIT Kanpur) (14) (15) December 15, 2009 28 / 49 Simulations: 1D Transient Diffusion Consider the following transient diffusion problem: ∂φ = ∇2 φ ∂t (16) with boundary conditions φ = 1 at x = 0 (17) φ = 0 at x = ∞ (18) φ = 0 at t = 0 (19) The exact analytical solution to the above is √ φ(x, t) = 1 − erf (x/2 t) Mainak Chowdhury (IIT Kanpur) December 15, 2009 29 / 49 Explicit scheme with 90% of allowed time step 1.0 solution variable analytical value 0.8 0.6 0.4 0.2 0.0 0 Mainak Chowdhury (IIT Kanpur) 10 20 30 40 50 December 15, 2009 30 / 49 Explicit scheme with 110% of allowed time step 1.0 solution variable analytical value 0.8 0.6 0.4 0.2 0.0 0 Mainak Chowdhury (IIT Kanpur) 10 20 30 40 50 December 15, 2009 31 / 49 Implicit scheme with the same time step 1.0 solution variable analytical value 0.8 0.6 0.4 0.2 0.0 0 Mainak Chowdhury (IIT Kanpur) 10 20 30 40 50 December 15, 2009 32 / 49 Outline 1 Introduction 2 Diffusion: The steady case 3 Diffusion: The non-steady case 4 Diffusion and Convection 5 Acknowledgements Mainak Chowdhury (IIT Kanpur) December 15, 2009 33 / 49 The steady state equation With no source terms the conservation equation reads, for any volume Ω, I (U(~v .~n) − κ∇(U).~n)dS = 0 ∂Ω Using divergence theorem, ∇.(U~v − κ∇(U)) = 0 In 1 D , the above equation reduces to d 2U d(Uv ) −κ 2 =0 dx dx Mainak Chowdhury (IIT Kanpur) December 15, 2009 34 / 49 Solving the steady state equation Node δx₂ δx₁ Uw x₁ Up x₂ Ue x Δx Control volume Integrating the equation over the control volume and using central differencing for the diffusion term, we get vx2 Ux2 − vx1 Ux1 = ae (Ue − Up ) − aw (Up − Uw ) Mainak Chowdhury (IIT Kanpur) December 15, 2009 (20) 35 / 49 Interpolation schemes for estimating the LHS Central Difference Upwind Differencing Hybrid Differencing Power Law Assume the general equation to be hp Up = hw Uw + he Ue (21) hp = hw + he + vx2 − vx1 (22) with Mainak Chowdhury (IIT Kanpur) December 15, 2009 36 / 49 The coefficient values in the different interpolation schemes Scheme Central Differencing Upwind Differencing Hybrid Differencing Power Law Mainak Chowdhury (IIT Kanpur) hw aw + vx1 /2 aw + max(vx1 , 0) he ae − vx2 /2 ae + max(0, −vx2 ) max(vx1 , (aw + vx1 /2), 0) max(0, −vx2 , (ae − vx2 /2) aw max(0, (1 − 0.1|Pe1 |)5 ) ae max(0, (1 − 0.1|Pe2 |)5 ) +max(vx1 , 0) +max(−vx2 , 0) December 15, 2009 37 / 49 Some issues in the choice of an interpolation scheme Conservativeness: The interpolation scheme should give the same value of the flux at the same face of adjacent volumes Boundedness: This means that the value at any node should not blow up. Transportiveness:This represents the ability of the interpolation scheme to address the relative strengths of diffusion and convection in the interpolation process. Accuracy Mainak Chowdhury (IIT Kanpur) December 15, 2009 38 / 49 A closer look at conservativeness Linear Interpolation Control Volume Volume Face Control node (a) A Linear Interpolation Quadratic Interpolation Control Volume Volume Face Control node (b) A Quadratic Interpolation Figure: A Comparison of Linear vs Quadratic interpolation However, not all quadratic schemes suffer from this problem. QUICK interpolation is one of the most widely used today. Mainak Chowdhury (IIT Kanpur) December 15, 2009 39 / 49 A closer look at boundedness A sufficient condition which will ensure converging solution ( [Versteeg et al]) is that P |anb | ≤ 1 for all nodes p |ap | < 1 for at least one node (23) (24) All coefficients should have the same sign to ensure that increase in any neighbouring node leads to increase of value at a particular node. Mainak Chowdhury (IIT Kanpur) December 15, 2009 40 / 49 A closer look at transportiveness Define the Peclet number as Pe = vxi L κxi (25) where L is the length of the domain of interest. A high |Pe | indicates strong convection over diffusion, low value indicates the converse. Central Differencing tends to break down with high |Pe | as it gives equal priority to “upstream” and “downstream” flows Upwind differencing or power law schemes try to accommodate this information Mainak Chowdhury (IIT Kanpur) December 15, 2009 41 / 49 A 2D convection and diffusion problem Consider the problem of diffusion in the annular region of the following: ω φ=0 y x r=3 The equation for φ in the annular region is 2y Mainak Chowdhury (IIT Kanpur) ∂φ ∂φ 1 ∂2φ ∂2φ − 2x = ( + ) ∂x ∂y Pe ∂x 2 ∂y 2 (26) December 15, 2009 42 / 49 Solution The exact solution to the above problem in the annular region is φ = 1 − log (x 2 + y 2 )/(2log 3) (27) It is plotted below: 0.9 Analytical Solution 1.4 0.8 1.2 0.7 Analytical Solution 1.0 0.6 0.8 0.5 0.6 0.4 0.4 0.3 0.2 0.2 0.0 0.0 0.2 0.4 0.6 0.8 1.0 1.2 1.4 0.1 Figure: Exact Solution Consider the problem in the region R. This becomes a 2D problem . Mainak Chowdhury (IIT Kanpur) December 15, 2009 43 / 49 The numerical errors from the Finite Volume Method The following plots were obtained from applying a finite volume method to a Cartesian grid (21X21) 0.00018 1.2 0.00012 1.0 0.00006 0.8 0.00000 0.6 0.6 0.4 0.12 0.2 0.18 0.0 0.0 0.2 0.4 0.6 0.8 1.0 1.2 0.24 (Analytical Solution - solution variable) 1.4 0.01 1.2 0.00 1.0 0.1 0.8 0.2 0.6 0.3 0.4 0.4 0.2 0.0 0.0 1.4 0.2 0.4 0.6 0.8 1.0 1.2 0.3 (a) Pe = 0.05 0.02 1.4 0.5 (Analytical Solution - solution variable) 0.00024 (Analytical Solution - solution variable) (Analytical Solution - solution variable) 1.4 0.6 (b) Pe = 20 Figure: The above plots illustrate the sensitivity of the numerical solutions to high Pe. Note the false diffusion Mainak Chowdhury (IIT Kanpur) December 15, 2009 44 / 49 Summary-Why FVM? Conservativeness: I I Conservativeness is explicitly enforced In sharp contrast to finite-difference and finite-element methods Handling unstructured geometries: I I I Suitable for representing complicated geometries. Easier incorporation of mixed boundary conditions over complicated boundaries Formulation stays the same Mainak Chowdhury (IIT Kanpur) December 15, 2009 45 / 49 Outline 1 Introduction 2 Diffusion: The steady case 3 Diffusion: The non-steady case 4 Diffusion and Convection 5 Acknowledgements Mainak Chowdhury (IIT Kanpur) December 15, 2009 46 / 49 Acknowledgements I would like to thank Dr. G. Biswas, for his insightful comments and helpful suggestions. I would also like to thank all members of the organising team of the 8th Winter Academy for giving us this unique opportunity to learn and interact with our fellow students from India and abroad. Mainak Chowdhury (IIT Kanpur) December 15, 2009 47 / 49 Bibliography H.K. Versteeg and W. Malalasekera. An introduction to Computational Fluid Dynamics: The Finite Volume Method Longman Scientific & Technical C.A.J. Fletcher. Computational Techniques for Fluid Dynamics Springer-Verlag J. Blazek. Computational Fluid Dynamics: Principles and Appications Elsevier CFD-Wiki www.cfd-online.com/Wiki FiPy http://www.ctcms.nist.gov/fipy/ Mainak Chowdhury (IIT Kanpur) December 15, 2009 48 / 49 End Thank you for your kind attention. Mainak Chowdhury (IIT Kanpur) December 15, 2009 49 / 49 End Thank you for your kind attention. Questions? Mainak Chowdhury (IIT Kanpur) December 15, 2009 49 / 49