University of Limerick Institutional Repository

Application of the Lagrangian meshfree approach to modelling of batch crystallisation: Part I-modelling of stirred tank hydrodynamics

DSpace Repository

Show simple item record

dc.contributor.author Nikolić, Dragan D
dc.contributor.author Frawley, Patrick J.
dc.date.accessioned 2017-04-03T10:34:57Z
dc.date.issued 2016
dc.identifier.uri http://hdl.handle.net/10344/5657
dc.description peer-reviewed en_US
dc.description.abstract Crystallization phenomena in stirred reactors are influenced by local hydrodynamic conditions and these must be taken into account for successful process scale-up and optimization. This article is the first of two presenting the application of the Smoothed Particle Hydrodynamics (SPH) method to modelling of batch crystallisation in stirred tanks. The benefits of the Lagrangian meshfree methods were discussed and the SPH method was proposed as an efficient method for the rapid prediction of the global mean flow in stirred reactors. Various aspects of the simulation results were discussed such as quality of the fluid prediction, computational requirements and availability of the crystal size distribution without reconstruction. It has been shown that the computational requirements and accuracy of the fluid flow prediction can be controlled through the particle size and that the particles with a radius of 1.50-1.75 mm in the reactor of 2.65 I provide a good balance between the quality of the prediction and the computational requirements.The developed Smoothed Particle Hydrodynamics model was applied to a numerical solution of coupled computational fluid dynamics and discretised population balance equations to model a batch crystallization process. Due to the specific formulation of the SPH equations the resulting ODE system is solved using the weighted contributions rather than numerically by solving a linear system of equations. Therefore, a large number of additional transport equations resulting from the discretisation of the population balance leads to only a minor increase in computational requirements (around 60% for 200 equations). The non-idealities in the reactor result in non-uniform mixing and contribute to the dispersion of the CSD. The effect of the hydrodynamics on the local temperature/supersaturation and the resulting crystal size distribution was captured and compared to the ideal mixing case.The developed SPH method served as a basis for the Part II of the series where a methodology for solution of population balance equations using high-resolution finite volume schemes or method of characteristics computed in parallel and independently from the Navier-Stokes equations is presented. (C) 2015 Elsevier Ltd. All rights reserved. en_US
dc.language.iso eng en_US
dc.publisher Elsevier en_US
dc.relation.ispartofseries Chemical Engineering Science;145, pp. 317-328
dc.relation.uri http://dx.doi.org/10.1016/j.ces.2015.08.052
dc.rights This is the author’s version of a work that was accepted for publication in Chemical Engineering Science. Changes resulting from the publishing process, such as peer review, editing, corrections, structural formatting, and other quality control mechanisms may not be reflected in this document. Changes may have been made to this work since it was submitted for publication. A definitive version was subsequently published in Chemical Engineering Science, 145, pp. 317-328, http://dx.doi.org/10.1016/j.ces.2015.08.052 en_US
dc.subject CFD en_US
dc.subject crystallisation en_US
dc.subject population balance en_US
dc.subject CUDA en_US
dc.subject smoothed particle hydrodynamics en_US
dc.title Application of the Lagrangian meshfree approach to modelling of batch crystallisation: Part I-modelling of stirred tank hydrodynamics en_US
dc.type info:eu-repo/semantics/article en_US
dc.type.supercollection all_ul_research en_US
dc.type.supercollection ul_published_reviewed en_US
dc.date.updated 2017-04-03T10:22:53Z
dc.description.version ACCEPTED
dc.identifier.doi 10.1016/j.ces.2015.08.052
dc.contributor.sponsor SFI en_US
dc.date.embargoEndDate 2017-09-24
dc.embargo.terms 2017-09-28 en_US
dc.rights.accessrights info:eu-repo/semantics/openAccess en_US
dc.internal.rssid 1638871
dc.internal.copyrightchecked Yes
dc.identifier.journaltitle Chemical Engineering Science
dc.description.status peer-reviewed


Files in this item

This item appears in the following Collection(s)

Show simple item record

Search ULIR


Browse

My Account

Statistics