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dc.contributor.authorBuffo, Antonio
dc.contributor.authorMarchisio, Daniele L.
dc.date.accessioned2021-09-21T07:53:20Z
dc.date.available2021-09-21T07:53:20Z
dc.date.issued2014
dc.identifier.citationBuffo, A., & Marchisio, D. L. (2014). Modeling and simulation of turbulent polydisperse gas-liquid systems via the generalized population balance equation. Reviews in Chemical Engineering, 30(1). doi:10.1515/revce-2013-0015
dc.identifier.issn2191-0235
dc.identifier.issn0167-8299
dc.identifier.doi10.1515/revce-2013-0015
dc.identifier.urihttp://hdl.handle.net/10754/671364
dc.description.abstractThis article reviews the most critical issues in the simulation of turbulent polydisperse gas-liquid systems. Here the discussion is limited to bubbly flows, where the gas appears in the form of separate individual bubbles. First, the governing equations are presented with particular focus on the generalized population balance equation (GPBE). Then, the mesoscale models defining the evolution of the gas-liquid system (e.g., interface forces, mass transfer, coalescence, and breakup) are introduced and critically discussed. Particular attention is devoted to the choice of the drag model to properly simulate dense gasliquid systems in the presence of microscale turbulence. Finally, the different solution methods, namely, Lagrangian and Eulerian, are presented and discussed. The link between mixture, two- and multi-fluid models, and the GPBE is also analyzed. Eventually, the different methodologies to account for polydispersity, with focus on Lagrangian or direct simulation Monte Carlo methods and Eulerian quadrature-based moment methods, are also presented. A number of practical examples are discussed and the review is concluded by presenting the advantages and disadvantages of the different methods and the corresponding computational costs. © 2014 Walter de Gruyter GmbH, Berlin/Boston.
dc.description.sponsorshipThis work is the result of the research carried out at DISAT, Politecnico di Torino on gas-liquid systems over the past decade. This research was financially supported by ENI (Italy) and BASF (Germany). The important contributions of Miriam Petitti (DISAT), Marco Vanni (DISAT), Fabrizio Podenzani (ENI), Peter Renze (BASF), Rodney O. Fox (Iowa State University), Matteo Icardi (KAUST), and Djamel Lakehal and Chidu Narayanan (ASCOMP) are gratefully acknowledged.
dc.publisherWalter de Gruyter GmbH
dc.relation.urlhttps://www.degruyter.com/document/doi/10.1515/revce-2013-0015/html
dc.rightsArchived with thanks to REVIEWS IN CHEMICAL ENGINEERING
dc.subjectbubble breakup
dc.subjectbubble coalescence
dc.subjectbubble column
dc.subjectcomputational fluid dynamics
dc.subjectCQMOM
dc.subjectDQMOM
dc.subjectdrag force
dc.subjectgas-liquid flow
dc.subjectpopulation balance model
dc.subjectQBMM
dc.subjectQMOM
dc.subjectstirred tank
dc.titleModeling and simulation of turbulent polydisperse gas-liquid systems via the generalized population balance equation
dc.typeArticle
dc.identifier.journalREVIEWS IN CHEMICAL ENGINEERING
dc.identifier.wosutWOS:000330850100003
dc.eprint.versionPost-print
dc.contributor.institutionIstituto di Ingegneria Chimica, Dipartimento di Scienza Applicata e Tecnologia, Politecnico di Torino, Corso Duca degli Abruzzi 24, 10129 Torino, Italy
dc.identifier.volume30
dc.identifier.issue1
dc.identifier.pages73-126
dc.identifier.eid2-s2.0-84900658201
kaust.acknowledged.supportUnitBAS


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