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Multiphase flow applications of nonintrusive reduced-order models with Gaussian process emulation

Published online by Cambridge University Press:  16 May 2022

Themistoklis Botsas
Affiliation:
Data Centric Engineering, The Alan Turing Institute, 96 Euston Rd, London NW1 2DB, United Kingdom
Indranil Pan*
Affiliation:
Data Centric Engineering, The Alan Turing Institute, 96 Euston Rd, London NW1 2DB, United Kingdom Department of Chemical Engineering, Imperial College London, Exhibition Rd, South Kensington, London SW7 2BX, United Kingdom School of Mathematics, Statistics & Physics, Newcastle University, Newcastle upon Tyne NE1 7RU, United Kingdom
Lachlan R. Mason
Affiliation:
Data Centric Engineering, The Alan Turing Institute, 96 Euston Rd, London NW1 2DB, United Kingdom Department of Chemical Engineering, Imperial College London, Exhibition Rd, South Kensington, London SW7 2BX, United Kingdom
Omar K. Matar
Affiliation:
Data Centric Engineering, The Alan Turing Institute, 96 Euston Rd, London NW1 2DB, United Kingdom Department of Chemical Engineering, Imperial College London, Exhibition Rd, South Kensington, London SW7 2BX, United Kingdom
*
*Corresponding author. E-mail: i.pan11@imperial.ac.uk

Abstract

Reduced-order models (ROMs) are computationally inexpensive simplifications of high-fidelity complex ones. Such models can be found in computational fluid dynamics where they can be used to predict the characteristics of multiphase flows. In previous work, we presented a ROM analysis framework that coupled compression techniques, such as autoencoders, with Gaussian process regression in the latent space. This pairing has significant advantages over the standard encoding–decoding routine, such as the ability to interpolate or extrapolate in the initial conditions’ space, which can provide predictions even when simulation data are not available. In this work, we focus on this major advantage and show its effectiveness by performing the pipeline on three multiphase flow applications. We also extend the methodology by using deep Gaussian processes as the interpolation algorithm and compare the performance of our two variations, as well as another variation from the literature that uses long short-term memory networks, for the interpolation.

Information

Type
Research Article
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, provided the original article is properly cited.
Copyright
© The Author(s), 2022. Published by Cambridge University Press
Figure 0

Figure 1. Schematic of reduced-order modeling. Spatio-temporal outputs of a simulation (left) are being fed into an encoder and output a latent space (middle). The reconstruction of the original system (right) is the output of the decoder that uses as input the aforementioned latent space. Lower panel shows the interpolation and forecasting in the latent space for reconstruction.

Figure 1

Figure 2. Architecture of a convolutional autoencoder (CAE). The input frames are fed into the encoder, where convolutional (convolve) and pooling (pool) layers are used, in order to produce the latent space. The reverse scheme is used for the decoder, where unpooling (unpool) and upsampling (upsample) layers are used to produce an output as similar as possible to the original input.

Figure 2

Figure 3. Architecture of a VAE. It is similar to the CAE equivalent, with the additional assumption that the latent space is a set of multivariate Gaussian distributions, and can be described as $ z\sim N\left(\mu, {\sigma}^2\right) $.

Figure 3

Figure 4. Schematic of the enhanced reduced-order modeling which features additional steps to Figure 1 involving interpolation of the latent space and (if required) prediction for new parameters. The outputs are fed into the decoder for transformation back to the original space.

Figure 4

Table 1. Evaluation metrics for the PCA, CAE, and VAE models for the advection–diffusion problem.

Figure 5

Figure 5. True and reconstructed frames for the concentration profiles of the VAE-related methods applied to the advection–diffusion problem. The rows correspond to time-steps 11, 21, 31, 41, and 50, respectively.

Figure 6

Figure 6. Residual concentration profile plots of the VAE-related methods applied to the advection–diffusion problem. The rows correspond to time-steps 11, 21, 31, 41, and 50, respectively.

Figure 7

Figure 7. Comparison of the interpolation techniques; GP in (a), DGP in (b), and LSTM in (c), in the latent space for advection–diffusion.

Figure 8

Table 2. Computational cost (in seconds) for all compression and interpolation algorithms.

Figure 9

Table 3. Evaluation metrics for the PCA, CAE, and VAE models.

Figure 10

Figure 8. True and reconstructed frames of the film thickness for the CAE-related methods employed in the falling film problem. The rows correspond to time-steps 11, 21, 31, 41, and 50, respectively.

Figure 11

Figure 9. Residual plots of the film thickness associated with the CAE-related methods used in the falling film problem. The rows correspond to time-steps 11, 21, 31, 41, and 50, respectively.

Figure 12

Table 4. Evaluation metrics for the PCA, CAE, and VAE models.

Figure 13

Figure 10. True and reconstructed frames for the volume fraction of the CAE-related methods used in the polymer precipitation problems. The rows correspond to time-steps 11, 21, 31, 41, and 50, respectively.

Figure 14

Figure 11. Residual volume fraction plots of the CAE-related methods in the polymer precipitation problems. The rows correspond to time-steps 11, 21, 31, 41, and 50, respectively.

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