Search results for "fluid"

showing 10 items of 5513 documents

A Thermochromic Liquid Crystals Image Analysis technique to investigate temperature polarization in spacer-filled channels for Membrane Distillation

2013

The analysis of flow fields and temperature distributions is of paramount importance in the development and optimization of new spacer-filled channel geometries for Membrane Distillation modules. The literature reports only few studies on the experimental characterization of such channels and, to the authors’ knowledge, none of them presents local information concerning the temperature distribution on the membrane surface. In the present work, a non-intrusive experimental technique named TLC-IA-TP is presented: it is based on the use of Thermochromic Liquid Crystals (TLCs) and digital Image Analysis (IA) and it is applied here for the first time to the analysis of Temperature Polarization (…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciConvective heat transferbusiness.industryChemistrySettore ING-IND/25 - Impianti ChimiciMechanical engineeringFiltration and Separation02 engineering and technologyMechanicsComputational fluid dynamics021001 nanoscience & nanotechnologyMembrane distillationPolarization (waves)BiochemistryMembrane technologyMembrane020401 chemical engineeringLiquid crystalMembrane distillation Temperature polarization Thermochromic Liquid Crystals Digital Image Analysis Spacer filled channelGeneral Materials Science0204 chemical engineeringPhysical and Theoretical Chemistry0210 nano-technologybusinessCommunication channel
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Digital Image Analysis Technique for mixing pattern measurements in bi-dispersed 2D gas fluidized beds

2011

This work concerns a new experimental technique based on Digital Image Analysis aimed at the measurement of the mixing behaviour of the granular phase in a 2D fluidized bed. In particular, the preliminary results obtained about the mixing pattern of a bi-disperse 2D gas fluidized bed are reported. Two different kind of particles were fluidized having the same density but different size. The technique is based on suitable colour-field decomposition of the fluidized bed, in which particles of different colours are employed. The technique here proposed can effectively measure the concentration field in the whole bed during operation, thus obtaining data that can be reliably used for CFD simula…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciDIAT MIXING FLUIDIZED BED
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A novel 2D model for the assessment of deformation-induced flow redistribution phenomena in electrodialysis units

2022

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciElectromembrane process membrane deformation flow maldistribution fluid-structure interaction Darcy flowElectromembrane processFluid structure interactionflow maldistributionfluid-structure interactionmembrane deformationDarcy flowSettore ICAR/08 - Scienza Delle Costruzioni
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Numerical prediction of flow fields in baffled stirred vessels: A comparison of alternative modelling approaches

1998

Abstract Numerical simulations of the flow field in baffled mixing tanks, based on three alternative methods, are presented and discussed. In the first method, the impeller is not explicitly simulated, and its effects are modelled by imposing suitable, empirically derived, boundary conditions to the external flow. In the second method, the whole vessel volume is divided into two concentric, partially overlapping, regions. In the inner region, containing the impeller, the flow field is simulated in the rotating reference frame of the latter, while in the outer region simulations are conducted in the reference frame of the laboratory. Information is iteratively exchanged between the two regio…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciEngineeringComputer simulationbusiness.industryTurbulenceSettore ING-IND/25 - Impianti ChimiciApplied MathematicsGeneral Chemical EngineeringFlow (psychology)Turbulence modelGeneral ChemistryMechanicsComputational fluid dynamicsRotating reference frameIndustrial and Manufacturing EngineeringExternal flowFree surface flowRushton turbineImpellerStirred tankControl theoryCFDbusinessSettore ING-IND/19 - Impianti NucleariReference frameChemical Engineering Science
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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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CFD analysis of concentration polarization phenomena in spacer-filled channels for Reverse Electro-Dialysis

2012

In this work, carried out within the EU-FP7 funded REAPower project, CFD simulations were carried out in order to study the fluid flow behaviour and mass transport phenomena within spacer-filled channels.

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciFluid DynamicSalinity gradient powerconcentration polarizationmodelingspacer filled channelReapower ProjectCFDSettore ING-IND/19 - Impianti Nucleari
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Analysis of the bubbling behaviour of 2-D gas solid fluidized beds part II: Comparison between experiments and numerical simulations via Digital Imag…

2009

In the field of gas–solid fluidization, bubbles, and all features regarding them, have a very great importance, as they significantly affect the process performance. Numerous experimental studies on bubbles, and their formation, evolution, and properties, have been performed in the past. These investigations appear particularly difficult, due to the nature of these systems, since the gas phase is distributed in both the bubble and the emulsion phase. Several experimental approaches have been developed to tackle this study. Among these, the Digital Image Analysis Technique purposely developed in Part I of the present work, based on the use of a video camera for monitoring the phenomenon coup…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciFluidization Computational fluid dynamics Digital Image Analysis TechniqueSettore ING-IND/25 - Impianti Chimici
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CFD PREDICTION OF BUBBLES BEHAVIOUR IN 2-DIMENSIONAL GAS-SOLID FLUIDIZED BEDS

2008

In recent years the use of Computational Fluid Dynamics (CFD) is significantly increasing to simulate multi-phase flows. It is invariably emphasized that a necessary step towards the development of reliable fully predictive CFD models is an extensive experimental validation of the simulation results. This work in particular focuses on the CFD simulation of a lab-scale 2D fluidized bed and the relevant experiments, in order to validate the prediction capability of the used codes and models. It must be emphasized that both experimental and computational quantitative data have been obtained by means of an original Digital Image Analysis Technique, that allows coherent comparison of computation…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciFluidization Frequency analysis CFD.Settore ING-IND/25 - Impianti Chimici
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On some issues in the computational modelling of spacer-filled channels for membrane distillation

2017

Abstract This study addresses issues which arise in the computational and experimental modelling of flow and heat/mass transfer in membrane distillation and other processes adopting spacer-filled channels (either planar or spiral wound), but have not been sufficiently clarified in the literature so far. Most of the argumentations presented are based on original computational results obtained by the authors by finite volume simulations; some literature results are also considered. The questions addressed regard the choice of scales for the reduction of data and the definition of dimensionless numbers ( Re , f , Nu , Sh ); the definition of average heat or mass transfer coefficients; the comb…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciGeneral Chemical EngineeringSettore ING-IND/25 - Impianti ChimiciThermodynamicsMembrane distillation02 engineering and technologyMembrane distillationComputational fluid dynamics; Heat transfer; Mass transfer; Membrane distillation; Spacer filled channel; Chemistry (all); Chemical Engineering (all); Materials Science (all); Water Science and Technology; Mechanical Engineeringsymbols.namesakeThermal conductivity020401 chemical engineeringComputational fluid dynamicMass transferHeat transferGeneral Materials ScienceMass transferChemical Engineering (all)0204 chemical engineeringSettore ING-IND/19 - Impianti NucleariWater Science and TechnologyFinite volume methodChemistryMechanical EngineeringChemistry (all)Reynolds numberGeneral ChemistrySpacer filled channel021001 nanoscience & nanotechnologyThermal conductionHeat transfersymbolsMaterials Science (all)0210 nano-technologyDimensionless quantityDesalination
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CFD prediction of flow, heat and mass transfer in woven spacer-filled channels for membrane processes

2021

Abstract Flow and heat or mass transfer in channels provided with woven spacers made up of mutually orthogonal filaments were studied by Computational Fluid Dynamics. The problem addressed was the combined effect of the parameters that characterize the process: pitch to height ratio P/H (2, 3 and 4), flow attack angle θ (0, 7, 15, 20, 30, 40 and 45°) and Reynolds number Re (from ~1 to ~4000). The Prandtl number was 4.33, representative of water at ~40°C, while the Schmidt number was 600, representative of NaCl solutions. Simulations were performed by the finite volume code Ansys CFX™ 18.1 using very fine grids of ~6 to ~14 million volumes. For Re > ~400, the SST turbulence model was used to…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciMaterials science020209 energyPrandtl number02 engineering and technologyComputational fluid dynamicsSherwood numbersymbols.namesakeTemperature polarizationMass transfer0202 electrical engineering electronic engineering information engineeringPressure dropConcentration polarizationWoven spacerSettore ING-IND/19 - Impianti NucleariFluid Flow and Transfer ProcessesTurbulenceMechanical EngineeringSchmidt numberReynolds numberMechanics021001 nanoscience & nanotechnologyCondensed Matter PhysicsNusselt numberSST turbulence modelHeat transfersymbols0210 nano-technology
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