Uncertainty propagation through a point model for steady-state two-phase pipe flow

Uncertainty propagation is used to quantify the uncertainty in model predictions in the presence of uncertain input variables. In this study, we analyze a steady-state point-model for two-phase gas-liquid flow. We present prediction intervals for holdup and pressure drop that are obtained from knowl...

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Main Authors: Andreas Strand, Ivar Eskerud Smith, Tor Erling Unander, Ingelin Steinsland, Leif Rune Hellevik
Format: Article
Language:English
Published: MDPI AG 2020-02-01
Series:Algorithms
Subjects:
Online Access:https://www.mdpi.com/1999-4893/13/3/53
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spelling doaj-74d7dca8ce254e4faef0cac5b3684e462020-11-25T03:02:16ZengMDPI AGAlgorithms1999-48932020-02-011335310.3390/a13030053a13030053Uncertainty propagation through a point model for steady-state two-phase pipe flowAndreas Strand0Ivar Eskerud Smith1Tor Erling Unander2Ingelin Steinsland3Leif Rune Hellevik4Department of Structural Engineering, Faculty of Engineering, Norwegian University of Science and Technology, 7491 Trondheim, NorwaySINTEF Multiphase Flow Laboratory, 7491 Trondheim, NorwaySINTEF Multiphase Flow Laboratory, 7491 Trondheim, NorwayDepartment of Mathematical Sciences, Faculty of Information Technology and Electrical Engineering, Norwegian University of Science and Technology, 7491 Trondheim, NorwayDepartment of Structural Engineering, Faculty of Engineering, Norwegian University of Science and Technology, 7491 Trondheim, NorwayUncertainty propagation is used to quantify the uncertainty in model predictions in the presence of uncertain input variables. In this study, we analyze a steady-state point-model for two-phase gas-liquid flow. We present prediction intervals for holdup and pressure drop that are obtained from knowledge of the measurement error in the variables provided to the model. The analysis also uncovers which variables the predictions are most sensitive to. Sensitivity indices and prediction intervals are calculated by two different methods, Monte Carlo and polynomial chaos. The methods give similar prediction intervals, and they agree that the predictions are most sensitive to the pipe diameter and the liquid viscosity. However, the Monte Carlo simulations require fewer model evaluations and less computational time. The model predictions are also compared to experiments while accounting for uncertainty, and the holdup predictions are accurate, but there is bias in the pressure drop estimates.https://www.mdpi.com/1999-4893/13/3/53two-phase flowunit celluncertainty quantificationsensitivity analysismonte carlopolynomial chaos
collection DOAJ
language English
format Article
sources DOAJ
author Andreas Strand
Ivar Eskerud Smith
Tor Erling Unander
Ingelin Steinsland
Leif Rune Hellevik
spellingShingle Andreas Strand
Ivar Eskerud Smith
Tor Erling Unander
Ingelin Steinsland
Leif Rune Hellevik
Uncertainty propagation through a point model for steady-state two-phase pipe flow
Algorithms
two-phase flow
unit cell
uncertainty quantification
sensitivity analysis
monte carlo
polynomial chaos
author_facet Andreas Strand
Ivar Eskerud Smith
Tor Erling Unander
Ingelin Steinsland
Leif Rune Hellevik
author_sort Andreas Strand
title Uncertainty propagation through a point model for steady-state two-phase pipe flow
title_short Uncertainty propagation through a point model for steady-state two-phase pipe flow
title_full Uncertainty propagation through a point model for steady-state two-phase pipe flow
title_fullStr Uncertainty propagation through a point model for steady-state two-phase pipe flow
title_full_unstemmed Uncertainty propagation through a point model for steady-state two-phase pipe flow
title_sort uncertainty propagation through a point model for steady-state two-phase pipe flow
publisher MDPI AG
series Algorithms
issn 1999-4893
publishDate 2020-02-01
description Uncertainty propagation is used to quantify the uncertainty in model predictions in the presence of uncertain input variables. In this study, we analyze a steady-state point-model for two-phase gas-liquid flow. We present prediction intervals for holdup and pressure drop that are obtained from knowledge of the measurement error in the variables provided to the model. The analysis also uncovers which variables the predictions are most sensitive to. Sensitivity indices and prediction intervals are calculated by two different methods, Monte Carlo and polynomial chaos. The methods give similar prediction intervals, and they agree that the predictions are most sensitive to the pipe diameter and the liquid viscosity. However, the Monte Carlo simulations require fewer model evaluations and less computational time. The model predictions are also compared to experiments while accounting for uncertainty, and the holdup predictions are accurate, but there is bias in the pressure drop estimates.
topic two-phase flow
unit cell
uncertainty quantification
sensitivity analysis
monte carlo
polynomial chaos
url https://www.mdpi.com/1999-4893/13/3/53
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AT ingelinsteinsland uncertaintypropagationthroughapointmodelforsteadystatetwophasepipeflow
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