Search results for "Pension"

showing 10 items of 513 documents

Dense solid–liquid off-bottom suspension dynamics: Simulation and experiment

2009

Dense solid–liquid off-bottom suspension inside a baffled mechanically stirred tank equipped with a standard Rushton turbine is investigated. Dynamic evolution of the suspension from start-up to steady-state conditions has been determined by both visual experiments and computational fluid dynamics (CFDs). A classical Eulerian–Eulerian multifluid model (MFM) along with the “homogeneous” k–ε turbulence model is adopted to simulate suspension dynamics. In these systems the drag inter-phase force affects both solids suspension and distribution. Therefore, different computational approaches are tested in order to compute this term. Simulation results are compared with images obtained from the re…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciEngineeringSettore ING-IND/25 - Impianti ChimiciGeneral Chemical EngineeringMixing (process engineering)Start-upComputational fluid dynamicsPhysics::Fluid Dynamicssymbols.namesakeMixingControl theorySuspensionSuspension (vehicle)Steady stateTurbulencebusiness.industryGeneral ChemistryMechanicsDragEuler equationsRushton turbineSolid–liquidDragsymbolsCFDbusinessChemical Engineering Research and Design
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Modelling Turbulent Inter-Phase Drag in Mechanically Stirred Solid-Liquid Suspensions

2012

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciMaterials scienceTurbulenceDragSettore ING-IND/25 - Impianti ChimiciPhase (matter)Settore ING-IND/06 - FluidodinamicaMixing Solid-liquid Suspension Stirred Tank CFD Drag TurbulenceMechanicsSolid liquidProceeding of THMT-12. Proceedings of the Seventh International Symposium On Turbulence, Heat and Mass Transfer Palermo, Italy, 24-27 September, 2012
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CFD Simulation of Particle Suspension Height in Stirred Vessels

2004

Computational fluid dynamics (CFD) simulation capabilities for stirred solid–liquid dense systems are explored. These systems may give rise to the formation of a thick and well defined clear liquid layer in the upper part of the vessel, whose extension progressively reduces with increasing impeller speed. Experimental measurements of the suspension height (the height of the particle laden layer) were carried out at various agitation speeds for a variety of solid–liquid systems in a fully baffled transparent tank. A clear layer of liquid was actually observed in all runs, with the suspension height almost linearly dependent on agitation speed. CFD simulations of the above described systems w…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciMaterials sciencebusiness.industrySettore ING-IND/25 - Impianti ChimiciGeneral Chemical EngineeringEulerian pathGeneral ChemistryMechanicsDense two-phase mixtureComputational fluid dynamicsParticle dipersionAgitatorEuler equationssymbols.namesakeImpellerParticle suspensionSolids suspensionControl theoryCFD simulationsymbolsParticleStirred vesselsbusinessSuspension (vehicle)Layer (electronics)Chemical Engineering Research and Design
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ASSESSMENT OF THE MINIMUM POWER REQUIREMENTS FOR COMPLETE SUSPENSION IN TOP-COVERED UNBAFFLED STIRRED TANKS

2012

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSettore ING-IND/25 - Impianti ChimiciComplete suspension power number unbaffled stirred tanks solid liquid suspension mixing
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Suspension phenomena in solid-liquid agitated systems

2011

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSettore ING-IND/25 - Impianti Chimicisolid liquid suspension stirred tanks mixing computational fluid dynamics
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CFD MODELLING OF PARTICLE SUSPENSION IN STIRRED TANKS

2011

Mixing of solid particles into liquids in mechanically agitated vessels is a topic of primary importance for several industrial applications. A great deal of research efforts has been devoted so far to the assessment of the minimum impeller speed (Njs) able to guarantee that all particles are suspended. Conversely, only little attention has been paid to the evaluation of the amount of solid particles that are suspended at impeller speeds N lower than Njs, despite the fact that in a number of industrial applications agitation speeds smaller than Njs are actually adopted [1,2]. The present work deals with dense solid-liquid partial suspensions in baffled stirred tanks and particularly focuses…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciStirred tankMulti Fluid ModelSettore ING-IND/25 - Impianti ChimiciMultiphase FlowSolid liquid suspensionComputational Fluid Dynamic
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Suspension phenomena in solidliquid agitated systems

2011

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSuspensionphenomena
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CFD simulations of dense solid–liquid suspensions in baffled stirred tanks: Prediction of the minimum impeller speed for complete suspension

2012

Abstract In the literature on mechanically agitated solid–liquid systems, several methods are described to estimate the minimum impeller speed Njs at which all particles are suspended, but few studies have been devoted so far to their critical comparative assessment [67] . In the present paper, several alternative Njs prediction methods are applied to CFD results obtained for selected test cases covering a broad range of suspension conditions and impeller speeds. Results are compared with one another and with classic empirical correlations [88] . The aim of the work is to assess the adequacy of different methods for predicting Njs and, more generally, to contribute to a viable CFD-based str…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciWork (thermodynamics)Engineeringbusiness.industrySettore ING-IND/25 - Impianti ChimiciGeneral Chemical EngineeringMixing (process engineering)Mechanical engineeringGeneral ChemistryMechanicsStirred tank Multi-fluid model Computational fluid dynamics Solid–liquid two-phase flow Complete suspension speed Sufficient suspension speed Unsuspended solids criterionComputational fluid dynamicsIndustrial and Manufacturing EngineeringControl volumeImpellerEnvironmental ChemistrySuspension (vehicle)Reynolds-averaged Navier–Stokes equationsbusinessContactorChemical Engineering Journal
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Dense Solid-Liquid Suspensions in Top-Covered Unbaffled Stirred Vessels

2011

In the present work solids suspension is investigated in an unbaffled tank stirred by a Rushton turbine and provided with a top-cover in order to avoid the formation of the well known central vortex. The data obtained are compared with those pertaining baffled stirred tanks via comparison with the well known Zwietering’s correlation. The dependence of Njs on particle concentration is found to be similar to that well established for baffled vessels, while, as a difference from the latter, Njs is found to decrease when liquid viscosity increases. Results also show that Njs is substantially independent of particle size, a feature that may advice the adoption of unbaffled tanks when large heavy…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicilcsh:Computer engineering. Computer hardwareSettore ING-IND/25 - Impianti ChimiciMixing; SCRM; Suspension; Solid-Liquid; Unbaffledlcsh:TP155-156lcsh:TK7885-7895UnbaffledSCRMMixingSuspensionComputingMethodologies_DOCUMENTANDTEXTPROCESSINGlcsh:Chemical engineeringSolid-LiquidComputingMilieux_MISCELLANEOUSComputingMethodologies_COMPUTERGRAPHICS
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CFD Simulation of Solid Liquid Suspensions in Baffled Stirred Vessels Below Complete Suspension Speed

2011

Suspension of solid particles into liquids within stirred vessels is a complex phenomenon encountered in several industrial applications. Most researchers have focused their attention on the assessment of the minimum impeller speed (Njs) able to guarantee the suspension of all particles. Actually, in a number of industrial cases an impeller speed N lower than Njs is chosen as typical operating condition (Oldshue, 1983) as the resulting energy savings well counterbalance the loss of active interfacial area. Therefore, the assessment of the amount of unsuspended particles at any given impeller speed represents the key to quantify the economical advantage/disadvantage of adopting an impeller s…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicilcsh:Computer engineering. Computer hardwareSettore ING-IND/25 - Impianti Chimicilcsh:TP155-156Suspension Curveslcsh:TK7885-7895Mixing; Suspension; Solid-Liquid; CFD; PGT; MFM; Suspension CurvesMFMPGTMixingSuspensionComputingMethodologies_DOCUMENTANDTEXTPROCESSINGSolid-Liquidlcsh:Chemical engineeringCFDComputingMilieux_MISCELLANEOUSComputingMethodologies_COMPUTERGRAPHICSChemical Engineering Transactions
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