Search results for " computational fluid dynamics"

showing 10 items of 23 documents

Transition to turbulence in toroidal pipes

2011

AbstractIncompressible flow in toroidal pipes of circular cross-section was investigated by three-dimensional, time-dependent numerical simulations using a finite volume method. The computational domain included a whole torus and was discretized by up to ${\ensuremath{\sim} }11. 4\ensuremath{\times} 1{0}^{6} $ nodes. Two curvatures $\delta $ (radius of the cross-section/radius of the torus), namely 0.3 and 0.1, were examined; a streamwise forcing term was imposed, and its magnitude was made to vary so that the bulk Reynolds number ranged between ${\ensuremath{\sim} }3500$ and ${\ensuremath{\sim} }14\hspace{0.167em} 700$. The results were processed by different techniques in order to confirm…

PhysicsHopf bifurcationTurbulenceMechanical EngineeringReynolds numberTorusMechanicstransition to turbulence periodic flow quasi-periodic flow computational fluid dynamics curved pipe toroidal pipeCondensed Matter PhysicsSecondary flowVortexVortex ringsymbols.namesakeMechanics of MaterialsIncompressible flowsymbolsSettore ING-IND/19 - Impianti NucleariJournal of Fluid Mechanics
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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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Performance Comparison of Alternative Hollow-Fiber Modules for Hemodialysis by Means of a CFD-Based Model

2022

Commercial hemodialyzers are hollow-fiber cylindrical modules with dimensions and inlet–outlet configurations dictated mostly by practice. However, alternative configurations are possible, and one may ask how they would behave in terms of performance. In principle, it would be possible to depart from the standard counter-flow design, while still keeping high clearance values, thanks to the increase in the shell-side Sherwood number (Sh) due to the cross-flow. To elucidate these aspects, a previously developed computational model was used in which blood and dialysate are treated as flowing through two interpenetrating porous media. Measured Darcy permeabilities and mass transfer coefficients…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSettore ING-IND/25 - Impianti ChimiciProcess Chemistry and TechnologyPorous mediaHollow-fiber membraneUltrafiltrationhemodialysis; hollow-fiber membrane; solute clearance; computational fluid dynamics; porous media; Darcy permeability; ultrafiltration; mass transferFiltration and SeparationComputational fluid dynamicsHemodialysisChemical Engineering (miscellaneous)Mass transferDarcy permeabilitySettore ING-IND/19 - Impianti NucleariSolute clearanceMembranes
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Experimental and Numerical Analysis of a Cross-Flow Turbine

2016

An important component of the management cost of aqueducts is the energy costs. Part of these costs can be recovered by transforming some of the many existing energy dissipations into electric energy by means of economical turbines. This paper describes an experimental study that has been carried out in order to (1) test the performance of an economical cross-flow turbine that maintains high efficiency within a large range of water discharges, and (2) validate a new approximate formula relating main inlet velocity to inlet pressure. It is demonstrated that the proposed formula, on the basis of some simplifying assumptions, exactly links inlet velocity to inlet pressure with any possible geo…

EngineeringInlet velocitybusiness.industry020209 energyMechanical EngineeringNumerical analysisCross-flow turbines Water turbines Turbine experiments Turbine hydraulic design Computational fluid dynamicsMechanical engineering02 engineering and technologyLarge rangeComputational fluid dynamicsTurbineSettore ICAR/01 - IdraulicaElectric energy0202 electrical engineering electronic engineering information engineeringCross-flow turbinebusinessEnergy (signal processing)Water Science and TechnologyCivil and Structural EngineeringMarine engineeringJournal of Hydraulic Engineering
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Numerical and Experimental Investigation of Equivalence Ratio (ER) and Feedstock Particle Size on Birchwood Gasification

2017

This paper discusses the characteristics of Birchwood gasification using the simulated results of a Computational Fluid Dynamics (CFD) model. The CFD model is developed and validated with the experimental results obtained with the fixed bed downdraft gasifier available at the University of Agder (UIA), Norway. In this work, several parameters are examined and given importance, such as producer gas yield, syngas composition, lower heating value (LHV), and cold gas efficiency (CGE) of the syngas. The behavior of the parameters mentioned above is examined by varying the biomass particle size. The diameters of the two biomass particles are 11.5 mm and 9.18 mm. All the parameters investigate wit…

Control and OptimizationBirchwood gasification020209 energycold gas efficiencyEnergy Engineering and Power TechnologyBiomassThermodynamics02 engineering and technologycomputational fluid dynamicsBirchwood gasification; computational fluid dynamics; equivalence ratio; cold gas efficiency; syngaslcsh:Technologyequivalence ratio0202 electrical engineering electronic engineering information engineeringElectrical and Electronic EngineeringEngineering (miscellaneous)Petroleum engineeringRenewable Energy Sustainability and the EnvironmentChemistrylcsh:TProducer gassyngasYield (chemistry)ParticleHeat of combustionParticle sizeMass fractionEnergy (miscellaneous)Syngas
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CFD Predictions of Sufficient Suspension Conditions in Solid-Liquid Agitated Tanks

2012

Abstract Most research efforts on mechanically agitated solid-liquid contactors have been devoted to the assessment of the minimum impeller speed for complete off-bottom suspension, N js . Actually, many industrial vessels are operated at impeller speeds slightly lower than N js (Oldshue, 1983; Rieger et al., 1988). This suggests that the sufficient suspension condition, which is quantitatively specified in this paper by introducing a suitably defined quantity N ss , may represent a valid alternative to that of complete suspension. In the present work time-dependent RANS simulations were carried out with the aim of predicting the achievement of sufficient suspension conditions. The Eulerian…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicistirred tank Computational Fluid Dynamics (CFD) solid-liquid suspension complete suspension Unsuspended Solid Criterion (USC) sufficient suspensionMaterials sciencebusiness.industrySettore ING-IND/25 - Impianti ChimiciApplied MathematicsComputational MechanicsGeneral Physics and AstronomyStatistical and Nonlinear PhysicsComputational fluid dynamicsChemical engineeringMechanics of MaterialsModeling and SimulationSettore ING-IND/06 - FluidodinamicabusinessSuspension (vehicle)Engineering (miscellaneous)Solid liquidInternational Journal of Nonlinear Sciences and Numerical Simulation
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CFD Simulation of Mass Transfer Phenomena in Spacer Filled Channels for Reverse Electrodialysis Applications

2013

Salinity Gradient Power via Reverse Electrodialysis is a topic of primary importance nowadays. It allows getting energy from the “controlled” mixing of solutions at different salt concentration. The performance of this technology depends on many factors such as: components properties (i.e. membranes, spacers, electrodes), stack geometry, operating conditions and feeds features. Concentration polarization phenomena may significantly affect the actual membrane potential, thus reducing the gross power produced. On the other hand, C-polarization phenomena may significantly be reduced by suitably choosing the hydrodynamic regime within the stack. Such a choice may in turn significantly require h…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicilcsh:Computer engineering. Computer hardwareReverse Electrodyalisis; Computational Fluid Dynamics; Mass Transferlcsh:TP155-156lcsh:TK7885-7895Reverse ElectrodyalisiComputational Fluid Dynamiclcsh:Chemical engineeringMass TransferSettore ING-IND/19 - Impianti Nucleari
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CFD simulations of dense solid–liquid suspensions in baffled stirred tanks: Prediction of solid particle distribution

2013

Abstract Industrial tanks devoted to the mixing of solid particles into liquids are often operated at an impeller speed N less than Njs (defined as the lowest speed allowing the suspension of all particles): under such conditions the distribution of solid-particles is very far from being homogeneous and very significant concentration gradients exist. The present work is devoted to assessing the capability of Computational Fluid Dynamics (CFD) in predicting the particle distribution throughout the tank. The CFD model proposed by Tamburini et al. [58] and successfully applied to the prediction of the sediment amount and shape was adopted here to simulate the particle distribution under partia…

EngineeringSettore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSteady statebusiness.industryGeneral Chemical EngineeringSettore ING-IND/25 - Impianti ChimiciMixing (process engineering)Mechanical engineeringGeneral ChemistryMechanicsComputational fluid dynamicsIndustrial and Manufacturing EngineeringRushton turbineImpellerSettore ING-IND/06 - FluidodinamicaEnvironmental ChemistryParticleMulti Fluid Model (MFM) Computational Fluid Dynamics (CFD) turbulence closure solid-liquid suspension partial suspension drag force stirred tank particle distribution Unsuspended Solid Criterion (USC)Suspension (vehicle)businessReynolds-averaged Navier–Stokes equations
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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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Mass transfer in ducts with transpiring walls

2019

Abstract The problem of mass transfer in ducts with transpiring walls is analysed: the concepts of “solvent” and “solute” fluxes are introduced, all possible sign combinations for these fluxes are considered, and relevant examples from membrane processes such as electrodialysis, reverse osmosis and filtration are identified. Besides the dimensionless numbers commonly defined in studying flow and mass transfer problems, new dimensionless quantities appropriate to transpiration problems are introduced, and their limiting values, associated with “drying”, “desalting” and “saturation” conditions, are identified. A simple model predicting the Sherwood number Sh under all possible flux sign combi…

Fluid Flow and Transfer ProcessesSettore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicibusiness.industryMechanical EngineeringSchmidt numberFlow (psychology)02 engineering and technologyMechanicsComputational fluid dynamics021001 nanoscience & nanotechnologyCondensed Matter Physics01 natural sciencesSherwood number010305 fluids & plasmasMass transfer Transpiring wall Sherwood number Computational fluid dynamics Parallel flowMass transfer0103 physical sciencesDiffusion (business)0210 nano-technologybusinessSaturation (chemistry)Settore ING-IND/19 - Impianti NucleariDimensionless quantityMathematicsInternational Journal of Heat and Mass Transfer
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