A simple model for predicting the pressure drop and film thickness of non-Newtonian annular flows in horizontal pipes

A model of two-phase non-Newtonian horizontal annular flows, which predicts film thickness and pressure gradient from flowrates only, is presented. In the model, the gas and non-Newtonian liquid flows are calculated separately based on the independent governing equations. The shear stress balance at...

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Main Authors: Li, Haiwang, Wong, Teck Neng, Skote, Martin, Duan, Fei
Other Authors: School of Mechanical and Aerospace Engineering
Format: Article
Language:English
Published: 2013
Online Access:https://hdl.handle.net/10356/106838
http://hdl.handle.net/10220/17776
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Institution: Nanyang Technological University
Language: English
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spelling sg-ntu-dr.10356-1068382023-03-04T17:21:37Z A simple model for predicting the pressure drop and film thickness of non-Newtonian annular flows in horizontal pipes Li, Haiwang Wong, Teck Neng Skote, Martin Duan, Fei School of Mechanical and Aerospace Engineering A model of two-phase non-Newtonian horizontal annular flows, which predicts film thickness and pressure gradient from flowrates only, is presented. In the model, the gas and non-Newtonian liquid flows are calculated separately based on the independent governing equations. The shear stress balance at the gas–liquid interface is calculated in order to link two phases together. The non-Newtonian fluid is assumed as a power-law shear-thinning liquid. The logarithmic velocity distribution is chosen to calculate the turbulent velocity profile in the gas core. The influences of entrainment and aeration are included in the model. The pressure drop, film thickness, void fraction, the frictional multiplier, and Lockhart–Martinelli parameter are predicted. The analytical model is compared with the published experimental investigations, and the results show that the model can predict the film thickness and pressure gradient simultaneously based on the flowrates of liquid and gas. The frictional multiplier and Lockhart–Martinelli parameter are calculated at the same time, and the predicted values are comparable with the experimental data. The difference between the analytical model and the experiments is lower than 10%. ASTAR (Agency for Sci., Tech. and Research, S’pore) Accepted version 2013-11-19T04:43:36Z 2019-12-06T22:19:26Z 2013-11-19T04:43:36Z 2019-12-06T22:19:26Z 2013 2013 Journal Article Li, H., Wong, T. N., Skote, M., & Duan, F. (2013). A simple model for predicting the pressure drop and film thickness of non-Newtonian annular flows in horizontal pipes. Chemical Engineering Science, 102,121-128. 0009-2509 https://hdl.handle.net/10356/106838 http://hdl.handle.net/10220/17776 10.1016/j.ces.2013.07.046 175149 en Chemical engineering science © 2013 Elsevier Ltd. This is the author created version of a work that has been peer reviewed and accepted for publication by Chemical Engineering Science, Elsevier Ltd. It incorporates referee’s comments but changes resulting from the publishing process, such as copyediting, structural formatting, may not be reflected in this document. The published version is available at: [http://dx.doi.org/10.1016/j.ces.2013.07.046]. application/pdf
institution Nanyang Technological University
building NTU Library
continent Asia
country Singapore
Singapore
content_provider NTU Library
collection DR-NTU
language English
description A model of two-phase non-Newtonian horizontal annular flows, which predicts film thickness and pressure gradient from flowrates only, is presented. In the model, the gas and non-Newtonian liquid flows are calculated separately based on the independent governing equations. The shear stress balance at the gas–liquid interface is calculated in order to link two phases together. The non-Newtonian fluid is assumed as a power-law shear-thinning liquid. The logarithmic velocity distribution is chosen to calculate the turbulent velocity profile in the gas core. The influences of entrainment and aeration are included in the model. The pressure drop, film thickness, void fraction, the frictional multiplier, and Lockhart–Martinelli parameter are predicted. The analytical model is compared with the published experimental investigations, and the results show that the model can predict the film thickness and pressure gradient simultaneously based on the flowrates of liquid and gas. The frictional multiplier and Lockhart–Martinelli parameter are calculated at the same time, and the predicted values are comparable with the experimental data. The difference between the analytical model and the experiments is lower than 10%.
author2 School of Mechanical and Aerospace Engineering
author_facet School of Mechanical and Aerospace Engineering
Li, Haiwang
Wong, Teck Neng
Skote, Martin
Duan, Fei
format Article
author Li, Haiwang
Wong, Teck Neng
Skote, Martin
Duan, Fei
spellingShingle Li, Haiwang
Wong, Teck Neng
Skote, Martin
Duan, Fei
A simple model for predicting the pressure drop and film thickness of non-Newtonian annular flows in horizontal pipes
author_sort Li, Haiwang
title A simple model for predicting the pressure drop and film thickness of non-Newtonian annular flows in horizontal pipes
title_short A simple model for predicting the pressure drop and film thickness of non-Newtonian annular flows in horizontal pipes
title_full A simple model for predicting the pressure drop and film thickness of non-Newtonian annular flows in horizontal pipes
title_fullStr A simple model for predicting the pressure drop and film thickness of non-Newtonian annular flows in horizontal pipes
title_full_unstemmed A simple model for predicting the pressure drop and film thickness of non-Newtonian annular flows in horizontal pipes
title_sort simple model for predicting the pressure drop and film thickness of non-newtonian annular flows in horizontal pipes
publishDate 2013
url https://hdl.handle.net/10356/106838
http://hdl.handle.net/10220/17776
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