Parameters influencing dilute‐phase pneumatic conveying through pipe systems: a computational study by the Euler/Lagrange approach

The present contribution summarizes research related to the numerical computation of pneumatic conveying systems applying the Euler/Lagrange approach. For that purpose, a rigorous modelling of the particulate phase was aspired, including the relevant fluid dynamic forces, particle‐wall collisions wi...

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Authors: Laín Beatove, Santiago, Sommerfeld, Martin
Format: article
Status:Published version
Publication Date:2014
Country:Colombia
Institution:Universidad Autónoma de Occidente
Repository:RED: Repositorio Educativo Digital UAO
Language:English
OAI Identifier:oai:red.uao.edu.co:10614/12166
Online Access:http://hdl.handle.net/10614/12166
https://doi.org/10.1002/cjce.22105
Access Level:Open access
Keyword:Control neumático
Pneumatic control
Pneumatic conveying
Numerical calculation (CFD)
Euler/Lagrange approach
Horizontal pipe/bend/vertical pipe
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oai_identifier_str oai:red.uao.edu.co:10614/12166
network_acronym_str CO
network_name_str Colombia
repository_id_str
dc.title.none.fl_str_mv Parameters influencing dilute‐phase pneumatic conveying through pipe systems: a computational study by the Euler/Lagrange approach
title Parameters influencing dilute‐phase pneumatic conveying through pipe systems: a computational study by the Euler/Lagrange approach
spellingShingle Parameters influencing dilute‐phase pneumatic conveying through pipe systems: a computational study by the Euler/Lagrange approach
Laín Beatove, Santiago
Control neumático
Pneumatic control
Pneumatic conveying
Numerical calculation (CFD)
Euler/Lagrange approach
Horizontal pipe/bend/vertical pipe
title_short Parameters influencing dilute‐phase pneumatic conveying through pipe systems: a computational study by the Euler/Lagrange approach
title_full Parameters influencing dilute‐phase pneumatic conveying through pipe systems: a computational study by the Euler/Lagrange approach
title_fullStr Parameters influencing dilute‐phase pneumatic conveying through pipe systems: a computational study by the Euler/Lagrange approach
title_full_unstemmed Parameters influencing dilute‐phase pneumatic conveying through pipe systems: a computational study by the Euler/Lagrange approach
title_sort Parameters influencing dilute‐phase pneumatic conveying through pipe systems: a computational study by the Euler/Lagrange approach
dc.creator.none.fl_str_mv Laín Beatove, Santiago
Sommerfeld, Martin
author Laín Beatove, Santiago
author_facet Laín Beatove, Santiago
Sommerfeld, Martin
author_role author
author2 Sommerfeld, Martin
author2_role author
dc.subject.none.fl_str_mv Control neumático
Pneumatic control
Pneumatic conveying
Numerical calculation (CFD)
Euler/Lagrange approach
Horizontal pipe/bend/vertical pipe
topic Control neumático
Pneumatic control
Pneumatic conveying
Numerical calculation (CFD)
Euler/Lagrange approach
Horizontal pipe/bend/vertical pipe
description The present contribution summarizes research related to the numerical computation of pneumatic conveying systems applying the Euler/Lagrange approach. For that purpose, a rigorous modelling of the particulate phase was aspired, including the relevant fluid dynamic forces, particle‐wall collisions with wall roughness and inter‐particle collisions. For the validation of the computations, experiments of Huber and Sommerfeld were selected for the conveying through a 80 mm stainless steel pipe with 5 m horizontal pipe, bend and 5 m vertical pipe. The majority of the computations were done for the same pipe system; however, in this instance, consisting of 150 mm stainless steel pipes. In these cases the average conveying velocity was 27 m/s and the particle mass loading was 0.3 (mass flow rate of particles/mass flow rate of air). For this configuration the influence of wall roughness, inter‐particle collisions, particle size, and mass loading on the resulting particle concentration distribution, the secondary flow as well as the pressure drop in the different pipe elements was analyzed. Moreover, a segregation parameter was defined which describes the location of the maximum particle concentration throughout the pipe system. The secondary flow intensity (SFI) was used to characterize the influence of the particle phase on the developing structure of the secondary flow
publishDate 2014
dc.date.none.fl_str_mv 2014-11
2020-03-25T18:04:22Z
2020-03-25T18:04:22Z
dc.type.none.fl_str_mv Artículo de revista
http://purl.org/coar/resource_type/c_6501
Text
info:eu-repo/semantics/article
http://purl.org/redcol/resource_type/ARTREF
info:eu-repo/semantics/publishedVersion
format article
status_str publishedVersion
dc.identifier.none.fl_str_mv 0008-4034
http://hdl.handle.net/10614/12166
https://doi.org/10.1002/cjce.22105
ISSN:1939-019X
Universidad Autónoma de Occidente
Repositorio Educativo Digital
identifier_str_mv 0008-4034
ISSN:1939-019X
Universidad Autónoma de Occidente
Repositorio Educativo Digital
url http://hdl.handle.net/10614/12166
https://doi.org/10.1002/cjce.22105
dc.language.none.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv The Canadian Journal Of Chemical Engineering. Volumen 93, número 1, (enero 2015); páginas 1-17
17
1
1
93
Lain Beatove, S., Sommerfeld, M. (2015). Parameters influencing dilute-phase pneumatic conveying through pipe systems: A computational study by the Euler/Lagrange approach. The Canadian Journal Of Chemical Engineering. 93(1), 1-17. https://doi.org/10.1002/cjce.22105
The Canadian Journal of Chemical Engineering
N. Huber, M. Sommerfeld, Powder Technology 1994, 79, 191
W. Siegel, Pneumatische Förderung: Grundlagen, Auslegung, Anlagenbau, Betrieb. Vogel Verlag, Würzburg 1991
S. Laín, R. Aliod, Study of the Eulerian dispersed phase equations in non-uniform turbulent two-phase flows: Discussion and comparison with experiments. Int. J. Heat Fluid Flow 2000, 21, 374
S. Dasgupta, R. Jackson, S. Sundaresan, Powder Technology 1998, 96, 6
M.Hidayat, A. Rasmuson, Powder Technology 2005, 153, 1
H. Bilirgen, E.K. Levy, Powder Technology 2001, 119, 134
Z.F. Tian, K. Inthavong, J.Y. Tu, G.H. Yeoh, Int. J. Heat and Mass Transfer 2008, 51, 1238.
A.S. Berrouk, D. Laurence, Int. J. Heat and Fluid Flow 2008, 29, 1010
M. Sommerfeld, S. Lain, Multiphase Science and Technology 2009, 21, 123
G. Kohnen, M. Rüger, M. Sommerfeld, Numerical Methods in Multiphase Flows 1994, (Eds. C.T. Crowe et al.), ASME Fluids Engineering Division Summer Meeting, Lake Tahoe, U.S.A. 1994, FED-Vol. 185, 191
S. Lain, M. Sommerfeld, CD-ROM Proceedings 7th International Conference on Multiphase Flow, ICMF2010, Tampa, FL USA, May 30. – June 4. 2010
S. Lain, M. Sommerfeld, 9th International ERCOFTAC Symposium ETMM9, Thessaloniki, Greece, 6. – 8. June 2012
S. Lain, M. Sommerfeld, 12th Int. Conf. on Multiphase Flow in Industrial Plants. Paper No. 141, Ischia (Napoli), Italy September 21-23, 2011
M. Sommerfeld, B. van Wachem, R. Oliemans, Best Practice Guidelines for Computational Fluid Dynamics of Dispersed Multiphase Flows. ERCOFTAC, Brussels, ISBN 978-91-633-3564-8, 2008
M. Sommerfeld, G. Kohnen, M. Rüger, Proc. 9th Symp. on Turbulent Shear Flows, Kyoto, Japan, paper 15-1, 1993
Ho, C.A. and Sommerfeld, M. (2002) Modelling of micro-particle agglomeration in turbulent flow. Chemical Engineering Science, 57, 3073-3084
C.A. Ho, M. Sommerfeld, Chemie Ingenieur Technik 2005, 77, 282
M. Sommerfeld, S. Lain, Ninth International Conference on CFD in the Minerals and Process Industries, CSIRO, Melbourne, Australia, 10-12 December 2012
M. Sommerfeld, Part. and Part. Systems Characterization 1990, 7, 209
S. Lain, M. Sommerfeld, Int. Journal of Heat and Fluid Flow, 2003, 24, 616
dc.rights.none.fl_str_mv Derechos Reservados - Canadian Society for Chemical Engineering, 2015
https://creativecommons.org/licenses/by-nc-nd/4.0/
info:eu-repo/semantics/openAccess
Atribución-NoComercial-SinDerivadas 4.0 Internacional (CC BY-NC-ND 4.0)
rights_invalid_str_mv Derechos Reservados - Canadian Society for Chemical Engineering, 2015
https://creativecommons.org/licenses/by-nc-nd/4.0/
Atribución-NoComercial-SinDerivadas 4.0 Internacional (CC BY-NC-ND 4.0)
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv application/pdf
17 páginas
dc.publisher.none.fl_str_mv Wiley
publisher.none.fl_str_mv Wiley
dc.source.none.fl_str_mv reponame:RED: Repositorio Educativo Digital UAO
instname:Universidad Autónoma de Occidente
instacron:Universidad Autónoma de Occidente
instname_str Universidad Autónoma de Occidente
instacron_str Universidad Autónoma de Occidente
institution Universidad Autónoma de Occidente
reponame_str RED: Repositorio Educativo Digital UAO
collection RED: Repositorio Educativo Digital UAO
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spelling Parameters influencing dilute‐phase pneumatic conveying through pipe systems: a computational study by the Euler/Lagrange approachLaín Beatove, SantiagoSommerfeld, MartinControl neumáticoPneumatic controlPneumatic conveyingNumerical calculation (CFD)Euler/Lagrange approachHorizontal pipe/bend/vertical pipeThe present contribution summarizes research related to the numerical computation of pneumatic conveying systems applying the Euler/Lagrange approach. For that purpose, a rigorous modelling of the particulate phase was aspired, including the relevant fluid dynamic forces, particle‐wall collisions with wall roughness and inter‐particle collisions. For the validation of the computations, experiments of Huber and Sommerfeld were selected for the conveying through a 80 mm stainless steel pipe with 5 m horizontal pipe, bend and 5 m vertical pipe. The majority of the computations were done for the same pipe system; however, in this instance, consisting of 150 mm stainless steel pipes. In these cases the average conveying velocity was 27 m/s and the particle mass loading was 0.3 (mass flow rate of particles/mass flow rate of air). For this configuration the influence of wall roughness, inter‐particle collisions, particle size, and mass loading on the resulting particle concentration distribution, the secondary flow as well as the pressure drop in the different pipe elements was analyzed. Moreover, a segregation parameter was defined which describes the location of the maximum particle concentration throughout the pipe system. The secondary flow intensity (SFI) was used to characterize the influence of the particle phase on the developing structure of the secondary flowWiley2020-03-25T18:04:22Z2020-03-25T18:04:22Z2014-11Artículo de revistahttp://purl.org/coar/resource_type/c_6501Textinfo:eu-repo/semantics/articlehttp://purl.org/redcol/resource_type/ARTREFinfo:eu-repo/semantics/publishedVersionapplication/pdf17 páginas0008-4034http://hdl.handle.net/10614/12166https://doi.org/10.1002/cjce.22105ISSN:1939-019XUniversidad Autónoma de OccidenteRepositorio Educativo DigitalengThe Canadian Journal Of Chemical Engineering. Volumen 93, número 1, (enero 2015); páginas 1-17171193Lain Beatove, S., Sommerfeld, M. (2015). Parameters influencing dilute-phase pneumatic conveying through pipe systems: A computational study by the Euler/Lagrange approach. The Canadian Journal Of Chemical Engineering. 93(1), 1-17. https://doi.org/10.1002/cjce.22105The Canadian Journal of Chemical EngineeringN. Huber, M. Sommerfeld, Powder Technology 1994, 79, 191W. Siegel, Pneumatische Förderung: Grundlagen, Auslegung, Anlagenbau, Betrieb. Vogel Verlag, Würzburg 1991S. Laín, R. Aliod, Study of the Eulerian dispersed phase equations in non-uniform turbulent two-phase flows: Discussion and comparison with experiments. Int. J. Heat Fluid Flow 2000, 21, 374S. Dasgupta, R. Jackson, S. Sundaresan, Powder Technology 1998, 96, 6M.Hidayat, A. Rasmuson, Powder Technology 2005, 153, 1H. Bilirgen, E.K. Levy, Powder Technology 2001, 119, 134Z.F. Tian, K. Inthavong, J.Y. Tu, G.H. Yeoh, Int. J. Heat and Mass Transfer 2008, 51, 1238.A.S. Berrouk, D. Laurence, Int. J. Heat and Fluid Flow 2008, 29, 1010M. Sommerfeld, S. Lain, Multiphase Science and Technology 2009, 21, 123G. Kohnen, M. Rüger, M. Sommerfeld, Numerical Methods in Multiphase Flows 1994, (Eds. C.T. Crowe et al.), ASME Fluids Engineering Division Summer Meeting, Lake Tahoe, U.S.A. 1994, FED-Vol. 185, 191S. Lain, M. Sommerfeld, CD-ROM Proceedings 7th International Conference on Multiphase Flow, ICMF2010, Tampa, FL USA, May 30. – June 4. 2010S. Lain, M. Sommerfeld, 9th International ERCOFTAC Symposium ETMM9, Thessaloniki, Greece, 6. – 8. June 2012S. Lain, M. Sommerfeld, 12th Int. Conf. on Multiphase Flow in Industrial Plants. Paper No. 141, Ischia (Napoli), Italy September 21-23, 2011M. Sommerfeld, B. van Wachem, R. Oliemans, Best Practice Guidelines for Computational Fluid Dynamics of Dispersed Multiphase Flows. ERCOFTAC, Brussels, ISBN 978-91-633-3564-8, 2008M. Sommerfeld, G. Kohnen, M. Rüger, Proc. 9th Symp. on Turbulent Shear Flows, Kyoto, Japan, paper 15-1, 1993Ho, C.A. and Sommerfeld, M. (2002) Modelling of micro-particle agglomeration in turbulent flow. Chemical Engineering Science, 57, 3073-3084C.A. Ho, M. Sommerfeld, Chemie Ingenieur Technik 2005, 77, 282M. Sommerfeld, S. Lain, Ninth International Conference on CFD in the Minerals and Process Industries, CSIRO, Melbourne, Australia, 10-12 December 2012M. Sommerfeld, Part. and Part. Systems Characterization 1990, 7, 209S. Lain, M. Sommerfeld, Int. Journal of Heat and Fluid Flow, 2003, 24, 616Derechos Reservados - Canadian Society for Chemical Engineering, 2015https://creativecommons.org/licenses/by-nc-nd/4.0/info:eu-repo/semantics/openAccessAtribución-NoComercial-SinDerivadas 4.0 Internacional (CC BY-NC-ND 4.0)reponame:RED: Repositorio Educativo Digital UAOinstname:Universidad Autónoma de Occidenteinstacron:Universidad Autónoma de Occidente2024-03-06T21:42:02Z
score 15,812429

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