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Multi-fidelity modelling of mixed convection based on experimental correlations and numerical simulations

Published online by Cambridge University Press:  21 November 2016

H. Babaee*
Affiliation:
Department of Mechanical Engineering, MIT Sea Grant College Program, Massachusetts Institute of Technology, Cambridge, MA 02142, USA
P. Perdikaris
Affiliation:
Department of Mechanical Engineering, MIT Sea Grant College Program, Massachusetts Institute of Technology, Cambridge, MA 02142, USA
C. Chryssostomidis
Affiliation:
Department of Mechanical Engineering, MIT Sea Grant College Program, Massachusetts Institute of Technology, Cambridge, MA 02142, USA
G. E. Karniadakis
Affiliation:
Division of Applied Mathematics, Brown University, Providence, RI 02912, USA
*
†Email address for correspondence: babaee@mit.edu

Abstract

For thermal mixed-convection flows, the Nusselt number is a function of Reynolds number, Grashof number and the angle between the forced- and natural-convection directions. We consider flow over a heated cylinder for which there is no universal correlation that accurately predicts Nusselt number as a function of these parameters, especially in opposing-convection flows, where the natural convection is against the forced convection. Here, we revisit this classical problem by employing modern tools from machine learning to develop a general multi-fidelity framework for constructing a stochastic response surface for the Nusselt number. In particular, we combine previously developed experimental correlations (low-fidelity model) with direct numerical simulations (high-fidelity model) using Gaussian process regression and autoregressive stochastic schemes. In this framework the high-fidelity model is sampled only a few times, while the inexpensive empirical correlation is sampled at a very high rate. We obtain the mean Nusselt number directly from the stochastic multi-fidelity response surface, and we also propose an improved correlation. This new correlation seems to be consistent with the physics of this problem as we correct the vectorial addition of forced and natural convection with a pre-factor that weighs differently the forced convection. This, in turn, results in a new definition of the effective Reynolds number, hence accounting for the ‘incomplete similarity’ between mixed convection and forced convection. In addition, due to the probabilistic construction, we can quantify the uncertainty associated with the predictions. This information-fusion framework is useful for elucidating the physics of the flow, especially in cases where anomalous transport or interesting dynamics may be revealed by contrasting the variable fidelity across the models. While in this paper we focus on the thermal mixed convection, the multi-fidelity framework provides a new paradigm that could be used in many different contexts in fluid mechanics including heat and mass transport, but also in combining various levels of fidelity of models of turbulent flows.

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Type
Papers
Copyright
© 2016 Cambridge University Press 
Figure 0

Figure 1.Nusselt number versus effective Reynolds number for mixed convection around a cylinder obtained from the experiments of Hatton et al. (1970) (blue symbols) and our direct numerical simulations (DNS) (red symbols). The black curve suggested by Hatton et al. (1970), corresponds to a correlation obtained from the ‘equivalence’ concept using experimental data from forced and natural convection. The disparity observed is due to parametric space compression, which is here represented by the effective Reynolds number, i.e. $Re_{eff}$ (see the main text for more explanation). In the present study, the experimental correlation is employed as a low-fidelity approximation for the mixed convection, while the high-fidelity approximation is obtained from DNS.

Figure 1

Figure 2.(a) Schematic of mixed convection of flow over a cylinder. The average Nusselt number of mixed convection for flow over a cylinder is expressed as $Nu=f(Re,Ri,\unicode[STIX]{x1D703})$. (b) Multi-fidelity modelling framework.

Figure 2

Figure 3.(a) Quadrilateral mesh for the DNS with nearly 15 000 elements and spectral polynomial $P=4$; (b) close-up view of the mesh near the cylinder; (c) validation of DNS for forced convection around a heated cylinder. Comparison of the experimental correlation with DNS. The same correlation (3.4) is used for estimating the Nusselt number for mixed convection by replacing $Re$ with an effective Reynolds number $Re_{eff}$ from (3.8).

Figure 3

Figure 4.(a,d,g) The local (solid lines: DNS) and the average (dashed lines: DNS) Nusselt number. (b,e,h) Mixed convection at $Re=40$ and $Ri=1$. The circles correspond to experimental correlation at the effective Reynolds number. (c,f,i) Forced convection at the effective Reynolds number, i.e. $Re_{eff}$, which is function of $\unicode[STIX]{x1D703}$. The simulations have been performed for three different angles of aiding flow ($\unicode[STIX]{x1D703}=0^{\circ }$), cross-flow ($\unicode[STIX]{x1D703}=90^{\circ }$) and opposing flow ($\unicode[STIX]{x1D703}=180^{\circ }$).

Figure 4

Figure 5.Instantaneous temperature contours for mixed convection around a heated cylinder at different points in the parametric space obtained from DNS (high-fidelity) model. The figure is organized with Richardson number $Ri$ increasing from 0 to 1 from left to right, and $\unicode[STIX]{x1D703}$ increasing from 0 to $180^{\circ }$ from bottom to top. The nine samples are chosen from the training set with closest points to the set $Ri^{s}\times \unicode[STIX]{x1D703}^{s}\times Re^{s}$ with $Ri^{s}=\{0.0,0.5,1.0\}$, and $\unicode[STIX]{x1D703}^{s}=\{0.0,90.0,180.0\}$ and $Re^{s}=\{40.0\}$.

Figure 5

Figure 6.Correlation of Nusselt number ($Nu^{LF}$) obtained from a low-fidelity model – see (3.9) – with high-fidelity ($Nu^{LF}$) DNS. Shown are: (a) 300 points uniformly distributed in the parametric space; (b) only points with the aiding convection $\unicode[STIX]{x1D703}<90^{\circ }$. These results demonstrate that the low-fidelity model is more accurate for the aiding-convection case and less accurate for the opposing-convection case.

Figure 6

Figure 7.Comparison of the $L_{2}$ error (a) mean; (b) standard deviation of Gaussian regression and multi-fidelity methods as a function of number of training points. The $L_{2}$ error is obtained by an ensemble average over one hundred models with each model construed by randomly sampling the design space. The smaller standard deviation of the multi-fidelity model demonstrates that it is more robust compared with respect to the sampling points compared to the single level Gaussian processes regression.

Figure 7

Figure 8.Correlation of Nusselt number obtained from (a) low-fidelity ($Nu^{LF}$) (b,c,d) ($Nu^{MF}$) multi-fidelity models with different number of training points. In the multi-fidelity (b,c,d), all $N_{LF}=1100$ points are used. These plots show that as the number of high-fidelity observations increases, the multi-fidelity model becomes more accurate.

Figure 8

Figure 9.(a) Averaged Nusselt number computed from the multi-fidelity response surface constructed from 300 high-fidelity and 1100 low-fidelity training points at $Re=30$. (b) Relative error percentage of the low-fidelity model in the Nusselt number computed by ${\mathcal{E}}=(N^{MF}-N^{LF})/N^{MF}\times 100$. The larger error corresponds to high Richardson number with opposing convection while small error is observed in two regimes: (i) dominant forced-convection flow, i.e. $Ri\ll 1$ and (ii) aiding convection i.e. $\unicode[STIX]{x1D703}<90^{\circ }$.

Figure 9

Figure 10.Nusselt number comparisons between multi-fidelity, high-/low-fidelity versus angle $\unicode[STIX]{x1D703}$ at $Re=30$ and $Ri=1$: (a,b) show that the prediction improves by simultaneously increasing number of training points in both, whereas (c,d) show the effect of improving the number of low-fidelity samples. The extra five (DNS) data denoted by symbols were not used in any of the training and they are independent DNS to verify the accuracy of the multi-fidelity prediction.

Figure 10

Figure 11.Nusselt number for mixed convection around a cylinder versus effective Reynolds number: (a) suggested by Hatton et al. (1970); (b) modified $Re_{eff}^{m}$ obtained from the multi-fidelity model. Shown are correlation (red curve), mean of the reference multi-fidelity model (black curve), multi-fidelity samples (blue symbols) and independent DNS samples (the same as the five cases considered in figure 10) (red symbols).