Hostname: page-component-77f85d65b8-6bnxx Total loading time: 0 Render date: 2026-03-27T23:36:45.549Z Has data issue: false hasContentIssue false

On the dispersion of entropy waves in turbulent flows

Published online by Cambridge University Press:  17 September 2020

Markus Weilenmann
Affiliation:
Department of Mechanical and Process Engineering, ETH Zürich, 8092 Zürich, Switzerland
Yuan Xiong
Affiliation:
Department of Mechanical and Process Engineering, ETH Zürich, 8092 Zürich, Switzerland
Nicolas Noiray*
Affiliation:
Department of Mechanical and Process Engineering, ETH Zürich, 8092 Zürich, Switzerland
*
Email address for correspondence: noirayn@ethz.ch

Abstract

Predicting and controlling entropy-wave-driven combustion instabilities is challenging, because the production, advection and dispersion of entropy waves in practical systems is difficult to model. The present paper aims to shed new light on this problem by considering a highly turbulent configuration with experiments and large eddy simulations. In this configuration, the decay of entropy waves is not only governed by the shear dispersion of an idealized turbulent pipe flow, as assumed in the recent studies on the topic, but also enhanced by the highly three-dimensional dispersion due to large-scale coherent structures. A novel post-processing approach for background-oriented schlieren (BOS) thermometry is proposed and enables the measurement of entropy waves with high spatio-temporal resolution for wide ranges of entropy wave amplitudes and frequencies. Instantaneous BOS snapshots are arranged in a panoramic coordinate frame using velocity data. This work, therefore, contributes to filling the knowledge gap in experimental data on entropy waves. The new dataset is accompanied with large eddy simulations to further elucidate the mechanisms dominating the amplitude decay of the entropy waves. It is shown that shear dispersion models that are only based on mean profiles of the axial velocity significantly underestimate the decay in the present configuration, where the entropy waves are formed by periodically injecting hot air pockets in the main stream. It is shown that the turbulent nature of the coherent hot pockets plays a key role in the dispersion enhancement.

Information

Type
JFM Rapids
Creative Commons
Creative Common License - CCCreative Common License - BY
This is an Open Access article, distributed under the terms of the Creative Commons Attribution licence (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted re-use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright
© The Author(s), 2020. Published by Cambridge University Press
Figure 0

Figure 1. (a) Top view of the experimental set-up including optical diagnostics. (b) Side view of the set-up. (c and d), respectively, show vertical and horizontal sections depicting the periodically pulsed hot air injection and the rotating disk.

Figure 1

Figure 2. (a) Phase-averaged velocity $\langle u_x \rangle$ from PIV data. (b) Instantaneous displacement fields $\boldsymbol {\delta }_{e}(\boldsymbol {x},t)$. (c) The instantaneous snapshots are placed within a panorama, using (2.3). In the overlapping areas, the displacement fields are averaged. The convective wavelength $\lambda_c$ is the ratio of the mean bulk velocity $\bar{u}$ to the pulsed-jet frequency $f$. (d) Resulting phase-averaged displacement field $\tilde {\boldsymbol {\delta }}_{e}(\boldsymbol {\chi })$ representing one acoustic cycle (here $f=240\,{\rm Hz}$ and $T_j=519$ K).

Figure 2

Figure 3. (a) Cut through the unstructured tetrahedral LES mesh, and imposed bulk velocity at the inlet of the pulsed hot jet-in-cross-flow versus time. The velocity inlet in the LES was set in order to match the siren mass flow rate measured in the experiments. (b) Magnification of the mesh cut at the siren injection. (c) Isocontours of dispersing entropy waves at $720$ Hz.

Figure 3

Figure 4. Panels (a and c), respectively, show $\tilde {T}(\boldsymbol {\chi })$ for pulsed-jet frequency of $240$ and $480\,{\rm Hz}$. From top to bottom, the jet exit temperature $T_j$ is set to $321$, $367$, $414$, $469$ and $519\,{\rm K}$. Panels (b and d) show the corresponding phase-averaged Mie scattering intensity.

Figure 4

Figure 5. Temperature (a), axial velocity (b) and total pressure (c) in the central plane of the computational domain. The markers in (b) indicate the streamwise locations (3 cm upstream and 2 cm downstream of the jet) used for the extraction of the velocity field shown in figure 7.

Figure 5

Figure 6. (a) Time trace of the cross-section-averaged temperature fluctuations at $0.1$ m downstream of the jet for the simulation with $T_j=514$ K and $f=720$ Hz. The dashed line is the Fourier component at the pulsed-jet frequency $f$. (b) Fourier coefficient amplitudes from LES and experiments as a function of $St$. For the experimental data, the markers and their colours, respectively, define $f$ and $T_j$. (c) Rate of change of $\tilde {T}$ with respect to $St$, as function of $\tilde {T}$.

Figure 6

Figure 7. Processing of LES data for $T_j=514$ K and $f=720$ Hz. (a) $\tilde {T}_1$, same processing as for the experimental data; $\tilde {T}_2$, superposition of $\tilde {T}_1$ and acoustically induced $\tilde {T}_a$; $\tilde {T}_3$, cross-section averaged coherent temperature fluctuation amplitudes; $\tilde {T}_4$, expected decay based on the $\bar {u}_x$ profiles (LES) shown in (b) for $x=-0.03$ m and in (c) for $x=0.02$ m. The dotted red lines indicate the $\lambda _b$ corresponding to the test conditions.