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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Autores:: Laín Beatove, Santiago
Sommerfeld, Martin

Tipo de recurso:: Article of journal

Fecha de publicación:: 2014

Institución:: Universidad Autónoma de Occidente

Repositorio:: RED: Repositorio Educativo Digital UAO

Idioma:: eng

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dc.title.eng.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 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.fl_str_mv	Laín Beatove, Santiago Sommerfeld, Martin
dc.contributor.author.none.fl_str_mv	Laín Beatove, Santiago Sommerfeld, Martin
dc.subject.armarc.spa.fl_str_mv	Control neumático
topic	Control neumático Pneumatic control Pneumatic conveying Numerical calculation (CFD) Euler/Lagrange approach Horizontal pipe/bend/vertical pipe
dc.subject.armarc.eng.fl_str_mv	Pneumatic control
dc.subject.proposal.eng.fl_str_mv	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.issued.none.fl_str_mv	2014-11
dc.date.accessioned.none.fl_str_mv	2020-03-25T18:04:22Z
dc.date.available.none.fl_str_mv	2020-03-25T18:04:22Z
dc.type.spa.fl_str_mv	Artículo de revista
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dc.identifier.issn.none.fl_str_mv	0008-4034
dc.identifier.uri.none.fl_str_mv	http://hdl.handle.net/10614/12166
dc.identifier.doi.spa.fl_str_mv	https://doi.org/10.1002/cjce.22105
dc.identifier.eissn.none.fl_str_mv	ISSN:1939-019X
dc.identifier.instname.spa.fl_str_mv	Universidad Autónoma de Occidente
dc.identifier.reponame.spa.fl_str_mv	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.iso.eng.fl_str_mv	eng
language	eng
dc.relation.eng.fl_str_mv	The Canadian Journal Of Chemical Engineering. Volumen 93, número 1, (enero 2015); páginas 1-17
dc.relation.citationendpage.none.fl_str_mv	17
dc.relation.citationissue.none.fl_str_mv	1
dc.relation.citationstartpage.none.fl_str_mv	1 93
dc.relation.cites.eng.fl_str_mv	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
dc.relation.ispartofjournal.eng.fl_str_mv	The Canadian Journal of Chemical Engineering
dc.relation.references.none.fl_str_mv	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.spa.fl_str_mv	Derechos Reservados - Canadian Society for Chemical Engineering, 2015
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dc.format.extent.spa.fl_str_mv	17 páginas
dc.publisher.eng.fl_str_mv	Wiley
institution	Universidad Autónoma de Occidente
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spelling	Laín Beatove, Santiagovirtual::2559-1Sommerfeld, Martin4225b01693727b10986bcc383715fa702020-03-25T18:04:22Z2020-03-25T18:04:22Z2014-110008-4034http://hdl.handle.net/10614/12166https://doi.org/10.1002/cjce.22105ISSN:1939-019XUniversidad Autónoma de OccidenteRepositorio Educativo DigitalThe 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 flowapplication/pdf17 páginasengWileyThe 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)http://purl.org/coar/access_right/c_abf2Parameters influencing dilute‐phase pneumatic conveying through pipe systems: a computational study by the Euler/Lagrange approachArtículo de revistahttp://purl.org/coar/resource_type/c_6501http://purl.org/coar/resource_type/c_2df8fbb1Textinfo:eu-repo/semantics/articlehttp://purl.org/redcol/resource_type/ARTREFinfo:eu-repo/semantics/publishedVersionhttp://purl.org/coar/version/c_970fb48d4fbd8a85Control neumáticoPneumatic controlPneumatic conveyingNumerical calculation (CFD)Euler/Lagrange approachHorizontal pipe/bend/vertical pipePublication082b0926-3385-4188-9c6a-bbbed7484a95virtual::2559-1082b0926-3385-4188-9c6a-bbbed7484a95virtual::2559-1https://scholar.google.com/citations?user=g-iBdUkAAAAJ&hl=esvirtual::2559-10000-0002-0269-2608virtual::2559-1https://scienti.minciencias.gov.co/cvlac/visualizador/generarCurriculoCv.do?cod_rh=0000262129virtual::2559-1CC-LICENSElicense_rdflicense_rdfapplication/rdf+xml; charset=utf-8805https://red.uao.edu.co/bitstreams/858f003a-66b9-4f50-8be7-57ad7ea9a434/download4460e5956bc1d1639be9ae6146a50347MD52LICENSElicense.txtlicense.txttext/plain; charset=utf-81665https://red.uao.edu.co/bitstreams/ed20a739-d086-4ad7-9d88-da91687e844e/download20b5ba22b1117f71589c7318baa2c560MD5310614/12166oai:red.uao.edu.co:10614/121662024-03-06 16:42:02.976https://creativecommons.org/licenses/by-nc-nd/4.0/Derechos Reservados - Canadian Society for Chemical Engineering, 2015metadata.onlyhttps://red.uao.edu.coRepositorio Digital Universidad Autonoma de Occidenterepositorio@uao.edu.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

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

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