On the application of an Eulerian granular model towards dilute phase pneumatic conveying

The present study considered the application of a multiphase model with Eulerian approach for the solids phase in dilute-phase conveying, where the results are compared against previously published experimental results based on 42 μm nominal diameter glass particles. In particular, the Favre-Average...

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Main Authors: Heng, Jinliang, New, Tze How, Wilson, P. A.
Other Authors: School of Mechanical and Aerospace Engineering
Format: Article
Language:English
Published: 2019
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Online Access:https://hdl.handle.net/10356/88956
http://hdl.handle.net/10220/48338
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Institution: Nanyang Technological University
Language: English
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spelling sg-ntu-dr.10356-889562023-03-04T17:14:57Z On the application of an Eulerian granular model towards dilute phase pneumatic conveying Heng, Jinliang New, Tze How Wilson, P. A. School of Mechanical and Aerospace Engineering Two-phase Flow DRNTU::Engineering::Mechanical engineering Pneumatic Conveying The present study considered the application of a multiphase model with Eulerian approach for the solids phase in dilute-phase conveying, where the results are compared against previously published experimental results based on 42 μm nominal diameter glass particles. In particular, the Favre-Averaged Drag turbulent dispersion model is studied where it is found to have greater effects on the particle concentration distribution as compared to the gas phase velocity. While certain discrepancies are observed between simulations and published experimental data, the flow characteristics are adequately captured after addressing the underlying cause of inaccuracies. Inaccuracies in the particle concentration distributions along a vertical pipe section result from the difficulty in capturing the transitional zone where the particle rope starts to disperse. On the other hand, particle diameter variations underpin the mismatches along a horizontal pipe section. Interestingly, increasing the particle diameter leads to the successful capturing of the particle concentration distribution along the horizontal pipe section. The accuracy of employing an Eulerian approach for solids phase is demonstrated, provided that effects due to the particle diameter are accounted for. Accepted version 2019-05-23T04:33:05Z 2019-12-06T17:14:34Z 2019-05-23T04:33:05Z 2019-12-06T17:14:34Z 2018 Journal Article Heng, J., New, T. H., & Wilson, P. A. (2018). On the application of an Eulerian granular model towards dilute phase pneumatic conveying. Powder Technology, 327, 456-466. doi:10.1016/j.powtec.2017.12.069 0032-5910 https://hdl.handle.net/10356/88956 http://hdl.handle.net/10220/48338 10.1016/j.powtec.2017.12.069 en Powder Technology © 2017 Elsevier B.V. All rights reserved. This paper was published in Powder Technology and is made available with permission of Elsevier B.V. 42 p. application/pdf
institution Nanyang Technological University
building NTU Library
continent Asia
country Singapore
Singapore
content_provider NTU Library
collection DR-NTU
language English
topic Two-phase Flow
DRNTU::Engineering::Mechanical engineering
Pneumatic Conveying
spellingShingle Two-phase Flow
DRNTU::Engineering::Mechanical engineering
Pneumatic Conveying
Heng, Jinliang
New, Tze How
Wilson, P. A.
On the application of an Eulerian granular model towards dilute phase pneumatic conveying
description The present study considered the application of a multiphase model with Eulerian approach for the solids phase in dilute-phase conveying, where the results are compared against previously published experimental results based on 42 μm nominal diameter glass particles. In particular, the Favre-Averaged Drag turbulent dispersion model is studied where it is found to have greater effects on the particle concentration distribution as compared to the gas phase velocity. While certain discrepancies are observed between simulations and published experimental data, the flow characteristics are adequately captured after addressing the underlying cause of inaccuracies. Inaccuracies in the particle concentration distributions along a vertical pipe section result from the difficulty in capturing the transitional zone where the particle rope starts to disperse. On the other hand, particle diameter variations underpin the mismatches along a horizontal pipe section. Interestingly, increasing the particle diameter leads to the successful capturing of the particle concentration distribution along the horizontal pipe section. The accuracy of employing an Eulerian approach for solids phase is demonstrated, provided that effects due to the particle diameter are accounted for.
author2 School of Mechanical and Aerospace Engineering
author_facet School of Mechanical and Aerospace Engineering
Heng, Jinliang
New, Tze How
Wilson, P. A.
format Article
author Heng, Jinliang
New, Tze How
Wilson, P. A.
author_sort Heng, Jinliang
title On the application of an Eulerian granular model towards dilute phase pneumatic conveying
title_short On the application of an Eulerian granular model towards dilute phase pneumatic conveying
title_full On the application of an Eulerian granular model towards dilute phase pneumatic conveying
title_fullStr On the application of an Eulerian granular model towards dilute phase pneumatic conveying
title_full_unstemmed On the application of an Eulerian granular model towards dilute phase pneumatic conveying
title_sort on the application of an eulerian granular model towards dilute phase pneumatic conveying
publishDate 2019
url https://hdl.handle.net/10356/88956
http://hdl.handle.net/10220/48338
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