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Lagrangian approach for modal analysis of fluid flows

Published online by Cambridge University Press:  15 October 2021

Vilas J. Shinde*
Affiliation:
Department of Mechanical and Aerospace Engineering, The Ohio State University, Columbus, OH 43210, USA
Datta V. Gaitonde
Affiliation:
Department of Mechanical and Aerospace Engineering, The Ohio State University, Columbus, OH 43210, USA
*
†Email address for correspondence: shinde.33@osu.edu

Abstract

Common modal decomposition techniques for flow-field analysis, data-driven modelling and flow control, such as proper orthogonal decomposition and dynamic mode decomposition, are usually performed in an Eulerian (fixed) frame of reference with snapshots from measurements or evolution equations. The Eulerian description poses some difficulties, however, when the domain or the mesh deforms with time as, for example, in fluid–structure interactions. For such cases, we first formulate a Lagrangian modal analysis (LMA) ansatz by a posteriori transforming the Eulerian flow fields into Lagrangian flow maps through an orientation and measure-preserving domain diffeomorphism. The development is then verified for Lagrangian variants of proper orthogonal decomposition and dynamic mode decomposition using direct numerical simulations of two canonical flow configurations at Mach 0.5, i.e. the lid-driven cavity and flow past a cylinder, representing internal and external flows, respectively, at pre- and post-bifurcation Reynolds numbers. The LMA is demonstrated for several situations encompassing unsteady flow without and with boundary and mesh deformation as well as non-uniform base flows that are steady in Eulerian but not in Lagrangian frames. We show that application of LMA to steady non-uniform base flow yields insights into flow stability and post-bifurcation dynamics. LMA naturally leads to Lagrangian coherent flow structures and connections with finite-time Lyapunov exponents. We examine the mathematical link between finite-time Lyapunov exponents and LMA by considering a double-gyre flow pattern. Dynamically important flow features in the Lagrangian sense are recovered by performing LMA with forward and backward (adjoint) time procedures.

Information

Type
JFM Papers
Copyright
© The Author(s), 2021. Published by Cambridge University Press
Figure 0

Figure 1.Schematic representation of a fluid element in the Lagrangian frame of reference, where the deforming flow trajectories lead to Lyapunov exponents and a data matrix for LMA over a finite time.

Figure 1

Figure 2.Flow recirculation patterns inside the lid-driven cavity at Mach number $M_\infty =0.5$ and pre- and post-critical Reynolds numbers. (a) Steady flow velocity $|\boldsymbol {u}|$ at $Re_L=7000$ and (b) time-averaged flow velocity $|\bar {\boldsymbol {u}}|$ at $Re_L=15\,000$. Streamlines display the flow recirculation patterns.

Figure 2

Figure 3.Lid-driven cavity flow at $M_\infty =0.5$ and $Re_L=15\,000$ with forced bottom surface/mesh deformation. (a) Instantaneous flow velocity magnitude with contours on a deformed domain. The inset shows a closer view of the deformed domain ($\boldsymbol {\chi }$). (b) Skin-friction coefficient on the bottom surface with/without deformation.

Figure 3

Figure 4.Compressible flow past a cylinder, in terms of the streamwise velocity $u_1$, at Mach number $M_\infty =0.5$ and Reynolds numbers $Re_D=40$ and $Re_D=100$. (a) Steady flow at $Re_D=40$. (b) The pressure coefficient $C_p$ is compared with the DNS profile of Canuto & Taira (2015) (dashed line.) (c) Unsteady instantaneous flow at $Re_D=100$. (d) Time-mean flow at $Re_D=100$.

Figure 4

Figure 5.Leading POD and DMD modes of the streamwise velocity for the lid-driven cavity at $Re_L=15\,000$ in the Eulerian frame of reference. (a) POD modes $\varPhi _2^{u_1}$, $\varPhi _3^{u_1}$, $\varPhi _4^{u_1}$ and $\varPhi _5^{u_1}$. (b) DMD modes $\phi _1^{u_1}$, $\phi _2^{u_1}$ and $\phi _3^{u_1}$. (c) POD modal energies and (d) DMD eigenvalues corresponding to the spatial modes.

Figure 5

Figure 6.Leading LPOD and LDMD modes of the streamwise velocity for the lid-driven cavity at $Re_L=15\,000$ in the Lagrangian frame of reference. The modes are presented using the identity map (reference grid) $\boldsymbol {\chi }_0(\tau _0)$ at time $\tau =\tau _0$. (a) LPOD modes $\varPhi _1^{\mathcal {U}_1}$, $\varPhi _2^{\mathcal {U}_1}$, $\varPhi _3^{\mathcal {U}_1}$ and $\varPhi _4^{\mathcal {U}_1}$. (b) LDMD modes $\phi _1^{\mathcal {U}_1}$, $\phi _2^{\mathcal {U}_1}$ and $\phi _3^{\mathcal {U}_1}$. (c) LPOD modal energies and (d) LDMD eigenvalues, indicating the values corresponding to the spatial modes.

Figure 6

Figure 7.Leading LPOD and LDMD modes of the absolute velocity and temperature for flow past a cylinder at $Re_D=100$ and $M_\infty =0.5$. The modes are displayed on the identity map (reference grid) $\boldsymbol {\chi }_0(\tau _0)$ at time $\tau =\tau _0$. (a) First LPOD mode $\varPhi _1^{|\boldsymbol {\mathcal {U}}|}$ and (b) second LPOD mode $\varPhi _2^{|\boldsymbol {\mathcal {U}}|}$ of the absolute velocity. (c) Real part of LDMD mode $\text {Re}(\phi _1^{|\boldsymbol {\mathcal {U}}|})$ with $St_D=0.13$ and (d) real part of LDMD mode $\text {Re}(\phi _2^{|\boldsymbol {\mathcal {U}}|})$ with $St_D=0.33$ for the absolute velocity. (e) First LPOD mode $\varPhi _1^\intercal$ and ( f) second LPOD mode $\varPhi _2^\intercal$ of the temperature. (g) Imaginary part of LDMD mode $\text {Im}(\phi _1^{\intercal })$ with $St_D=0.13$ and (h) imaginary part of LDMD mode $\text {Im}(\phi _2^{\intercal })$ with $St_D=0.33$ for the temperature.

Figure 7

Figure 8.Leading LPOD and LDMD modes of the streamwise velocity for the lid-driven cavity at $Re_L=15\,000$ subjected to forced bottom surface deformation at $St_L=1.0$. The modes are presented using the identity map (reference grid) $\boldsymbol {\chi }_0(\tau _0)$ at time $\tau =\tau _0$. (a) LPOD modes $\varPhi _2^{\mathcal {U}_1}$, $\varPhi _3^{\mathcal {U}_1}$, $\varPhi _4^{\mathcal {U}_1}$ and $\varPhi _6^{\mathcal {U}_1}$. (b) LDMD modes $\phi _1^{\mathcal {U}_1}$, $\phi _2^{\mathcal {U}_1}$, $\phi _3^{\mathcal {U}_1}$ and $\phi _4^{\mathcal {U}_1}$. (c) LPOD modal energies and (d) LDMD eigenvalues, indicating the values corresponding to the spatial modes.

Figure 8

Figure 9.Leading modes of the steady-state streamwise flow velocity for the lid-driven cavity at $Re_L=7000$ in the Lagrangian frame of reference. (a) LPOD modes $\varPhi _1^{\mathcal {U}_1}$, $\varPhi _2^{\mathcal {U}_1}$, $\varPhi _8^{\mathcal {U}_1}$ and $\varPhi _{17}^{\mathcal {U}_1}$. (b) LDMD modes $\phi _1^{\mathcal {U}_1}$, $\phi _2^{\mathcal {U}_1}$ and $\phi _3^{\mathcal {U}_1}$. (c) LPOD modal energies and (d) LDMD eigenvalues, indicating the values corresponding to the spatial modes.

Figure 9

Figure 10.Leading modes of the steady-state streamwise flow velocity for the flow past a cylinder at $Re_D=40$ in the Lagrangian frame of reference. (a) LPOD modes $\varPhi _2^{\mathcal {U}_1}$, $\varPhi _3^{\mathcal {U}_1}$, $\varPhi _4^{\mathcal {U}_1}$ and $\varPhi _5^{\mathcal {U}_1}$. (b) LDMD modes $\phi _1^{\mathcal {U}_1}$ and $\phi _2^{\mathcal {U}_1}$. (c) LPOD modal energies and (d) LDMD eigenvalues, indicating the values corresponding to the spatial modes.

Figure 10

Figure 11.Leading adjoint modes of the steady-state streamwise flow velocity for the flow past a cylinder at $Re_D=40$ in the Lagrangian frame of reference. (a) Adjoint LPOD modes $\hat {\varPhi }_2^{\mathcal {U}_1}$, $\hat {\varPhi }_3^{\mathcal {U}_1}$, $\hat {\varPhi }_4^{\mathcal {U}_1}$ and $\hat {\varPhi }_5^{\mathcal {U}_1}$. (b) Adjoint LDMD modes $\hat {\phi }_1^{\mathcal {U}_1}$ and $\hat {\phi }_2^{\mathcal {U}_1}$. (c) Adjoint LPOD modal energies and (d) adjoint LDMD eigenvalues, indicating frequencies associated with the spatial modes.

Figure 11

Figure 12.Comparison between the FTLE, LPOD and LDMD modes of the double-gyre flow. (a) Forward FTLE and (b) backward FTLE reference data from Finn & Apte (2013). The first (c) forward (${\varPhi }_1^{|\boldsymbol {\mathcal {U}}|}$, with a single contour level of value $1$) and (d) adjoint ($\hat {\varPhi }_1^{|\boldsymbol {\mathcal {U}}|}$) LPOD modes, as well as the only stationary (e) forward (${\phi }_1^{|\boldsymbol {\mathcal {U}}|}$) and ( f) adjoint ($\hat {\phi }_1^{|\boldsymbol {\mathcal {U}}|}$) LDMD modes for the double-gyre flow.

Figure 12

Figure 13.Modal energies/frequencies and higher-rank Lagrangian POD/DMD modes of the double-gyre flow. (a) LPOD modal energies, (b) LDMD eigenvalues and modal frequencies, (c) LPOD mode $\varPhi _2^{|\boldsymbol {\mathcal {U}}|}$, (d) LPOD mode $\varPhi _3^{|\boldsymbol {\mathcal {U}}|}$, (e) LPOD mode $\varPhi _4^{|\boldsymbol {\mathcal {U}}|}$, ( f) real part of LDMD mode $\phi _2^{|\boldsymbol {\mathcal {U}}|}$, (g) real part of LDMD mode $\phi _3^{|\boldsymbol {\mathcal {U}}|}$, and (h) imaginary part of LDMD mode $\phi _4^{|\boldsymbol {\mathcal {U}}|}$.

Figure 13

Table 1.Pseudo-algorithm for computing Lagrangian POD modes using a set of Eulerian snapshots.

Figure 14

Figure 14.Computational domain of the two-dimensional lid-driven cavity. The inset displays a small region of mesh $\texttt{M}_{\texttt{2}}$ with uniform discretization in either direction.

Figure 15

Table 2.Mesh details for the lid-driven cavity at the Reynolds number $Re_L=15\,000$ and Mach number $M_\infty =0.5$, mesh sensitivity of the time-averaged and root-mean-squared ($rms$) drag and lift coefficients, and the Strouhal number with its higher harmonics.

Figure 16

Figure 15.Grid convergence of the results for the lid-driven cavity at $Re_L=15\,000$. (a) Time-averaged flow velocity components along the cavity centrelines and (b) the skin-friction coefficient on the bottom wall of the cavity for the four grids $\texttt{G}_1$, $\texttt{G}_2$, $\texttt{G}_3$ and $\texttt{G}_4$.

Figure 17

Figure 16.Computational domain with mesh $\texttt{M}_1$ to simulate flow past a cylinder of diameter $D$. The outer boundary is placed at $40D$ from the centre. The inset shows the near-wall mesh structure.

Figure 18

Table 3.Details of the computational meshes $\texttt{M}_1$ and $\texttt{M}_2$, mesh sensitivity to drag and lift coefficients and Strouhal number for $Re_D=100$ and $M_\infty =0.5$ for the flow past a cylinder.