Search results for " impianti"

showing 10 items of 778 documents

Flow and mass transfer in spacer-filled channels for reverse electrodialysis: a CFD parametrical study

2016

Abstract In reverse electrodialysis (RED) concentration polarization phenomena and pressure drop affect strongly the power output obtainable; therefore the channel geometry has a crucial impact on the system optimization. Both overlapped and woven spacers are commonly commercialised and adopted for RED experiments; the latter exhibit some potential advantages, such as better mixing and lower shadow effect, but they have been poorly investigated in the literature so far. In this work, computational fluid dynamics was used to predict fluid flow and mass transfer in spacer-filled channels for RED applications. A parametric analysis for different spacer geometries was carried out: woven (w) and…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSpacer-filled channelSettore ING-IND/25 - Impianti ChimiciMixing (process engineering)Filtration and Separation02 engineering and technologyCFD; Concentration polarization; Mass transfer; Reverse electrodialysis (RED); Spacer-filled channel; Physical and Theoretical Chemistry; Materials Science (all); Biochemistry; Filtration and SeparationBiochemistryProtein filamentsymbols.namesake020401 chemical engineeringReversed electrodialysisMass transferFluid dynamicsGeneral Materials ScienceMass transfer0204 chemical engineeringPhysical and Theoretical ChemistryConcentration polarizationSettore ING-IND/19 - Impianti NucleariConcentration polarizationPressure dropSettore ING-IND/24 - Principi Di Ingegneria ChimicaChromatographyChemistryReverse electrodialysis (RED)Reynolds numberMechanics021001 nanoscience & nanotechnologysymbolsMaterials Science (all)0210 nano-technologyCFD
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CFD analysis of the fluid flow behavior in a reverse electrodialysis stack

2012

Salinity Gradient Power by Reverse Electrodialysis (SGP-RE) technology allows the production of electricity from the different chemical potentials of two differently concentrated salty solutions flowing in alternate channels suitably separated by selective ion exchange membranes. In SGP-RE, as well as in conventional ElectroDialysis (ED) technology, the process performance dramatically depends on the stack geometry and the internal fluid dynamics conditions: optimizing the system geometry in order to guarantee lower pressure drops (DP) and uniform flow rates distribution within the channels is a topic of primary importance. Although literature studies on Computational Fluid Dynamics (CFD) a…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSpacer-filled channelSettore ING-IND/25 - Impianti ChimiciOcean Engineering02 engineering and technology010501 environmental sciencesComputational fluid dynamics01 natural sciencesStack (abstract data type)Reversed electrodialysisFluid dynamicsOsmotic powerStack designPressure dropSettore ING-IND/19 - Impianti NucleariSimulation0105 earth and related environmental sciencesWater Science and Technologybusiness.industryChemistryModelingProcess (computing)MechanicsElectrodialysis021001 nanoscience & nanotechnologyPollution6. Clean waterCFD; Modeling; Stack design; Pressure drops; Spacer-filled channelSettore ING-IND/06 - FluidodinamicaPotential flowCFD0210 nano-technologybusinessDesalination and Water Treatment
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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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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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Pressure drop in woven-spacer-filled channels for reverse electrodialysis: CFD prediction and experimental validation

2015

Reverse electrodialysis (RED) is a promising technology for electric power generation by the chemical potential difference of two salt solutions within a stack equipped by selective ionexchange membranes (salinity gradient energy). Mechanical energy is required for pumping the feed solutions, which can reduce dramatically the net power output. In this work Computational Fluid Dynamics (CFD) simulations of spacer-filled channels for RED were carried out in parallel with an experimental campaign focused on the collection of data for model validation.

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciWoven spacer Pressure drop Reverse Electrodialysis; CFDWoven spacer Pressure drop Reverse ElectrodialysiCFDSettore ING-IND/19 - Impianti Nucleari
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CFD prediction of scalar transport in thin channels for reverse electrodialysis

2014

Reverse ElectroDialysis (RED) is a very promising technology allowing the electrochemical potential difference of a salinity gradient to be directly converted into electric energy. The fluid dynamics optimization of the thin channels used in RED is still an open problem. The present preliminary work focuses on the Computational Fluid Dynamics (CFD) simulation of the flow and concentration fields in these channels. In particular three different configurations were investigated: a channel unprovided with a spacer (empty channel) and two channels filled with spacers, one made of overlapped filaments the other of woven filaments. The transport of two passive scalars, representative of the ions …

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicibusiness.industryChemistrySettore ING-IND/25 - Impianti ChimiciScalar (mathematics)Ocean EngineeringMechanicsCFD Salinity Gradient Power renewable energy Reverse Electro Dialysis water electric energy spacer woven polarization concentration concentration boundary layer.Computational fluid dynamicsElectrodialysisPollutionReversed electrodialysisFluid dynamicsOsmotic powerElectronic engineeringSettore ING-IND/06 - FluidodinamicaPeriodic boundary conditionsbusinessWater Science and TechnologyConcentration polarization
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CFD simulations of early- to fully-turbulent conditions in unbaffled and baffled vessels stirred by a Rushton turbine

2021

Abstract Laboratory scale unbaffled tanks provided with a top cover and a baffled tank both stirred by a Rushton turbine were simulated by carrying out RANS simulations. Three different turbulence models were adopted (k- ω SST, k- e and the SSG Reynolds stress model) to predict the flow field and the relevant performance parameters (power and pumping numbers) of the tank operated from early to fully turbulent conditions. CFD results were compared with literature experimental data and DNS simulation results to validate and properly compare the models. In the range of Reynolds numbers investigated, results showed that, for the unbaffled tank, the SSG model based on Reynolds stresses is a bett…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicibusiness.industryTurbulenceGeneral Chemical EngineeringSettore ING-IND/25 - Impianti ChimiciReynolds number02 engineering and technologyGeneral ChemistryReynolds stressMechanicsComputational fluid dynamicsLaboratory scale021001 nanoscience & nanotechnologyFlow fieldRushton turbinesymbols.namesake020401 chemical engineeringCFD SSG Stirred tank Turbulence model Unbaffled vesselsymbols0204 chemical engineering0210 nano-technologybusinessReynolds-averaged Navier–Stokes equationsSettore ING-IND/19 - Impianti NucleariMathematics
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Numerical simulation of electroconvection phenomena in electrodialysis

In water desalination by electrodialysis, the current density i cannot exceed specific constraints, notably the diffusion limit. Working at higher i (overlimiting current regime) would make higher desalination rates possible. The main phenomenon allowing overlimiting current densities is the electrokinetic instability that arises when a sufficiently intense electric potential gradient is imposed, and leads to electroconvective mixing in the near-wall layer. In this study, these phenomena were investigated by CFD. The governing equations were the Nernst-Planck transport equations for anions and cations, the Poisson equation for the electrical potential and the Navier-Stokes and continuity eq…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicielectroconvectionelectrodialysioverlimitingelectrokinetic instabilitySettore ING-IND/19 - Impianti Nucleari
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CFD study on the influence of water transpiration on flow and mass transfer in channels with bipolar membranes

2018

The future energetic supply based on the massive use of renewable sources poses issues linked to fluctuations of power produced and consumed, thus requiring the use of energy storage systems.

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimicielectrodialysiBipolar membranemass transportCFDreverse electrodialysiSettore ING-IND/19 - Impianti Nucleari
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Mechanical-fluid dynamics coupled model for profiled Ion Exchange Membranes design

2018

In this work, we developed an advanced model useful for the design of profiled IEMs, based on the coupled simulation of local mechanical deformations and of fluid dynamics and associated mass transport phenomena within deformed channels

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimicielectrodialysideflectionCFDSettore ICAR/08 - Scienza Delle Costruzionireverse electrodialysiSettore ING-IND/19 - Impianti NucleariIon exchange membrane
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