Search results for "fluid"

showing 10 items of 5513 documents

Ion Exchange Membrane deformation and its relevance in Reverse ElectroDialysis

2017

Reverse electrodialysis (RED) is an innovative electro-membrane technology for electric energy generation from two salt solutions with different concentration. This different concentration is the driving force to a selective movement of ions from the concentrate channel to the dilute one oriented by Ion Exchange Membranes (IEMs). Typically, RED stack are made by piling alternatively cation exchange membranes and anion exchange membranes with the aid of spacers or profiles built on the membrane surface. Two electrodic compartments are placed at the two ends of the stack, where the ion flux generated is converted into an electric current able to circulate through an external load connected to…

Settore ING-IND/24 - Principi Di Ingegneria ChimicaSettore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSettore ING-IND/25 - Impianti ChimiciSettore ING-IND/06 - FluidodinamicaReverse electrodialysis Ion exchange membrane deformationSettore ICAR/08 - Scienza Delle Costruzioni
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Coupling CFD simulation with a simplified process model for reverse electrodialysis units

2017

Salinity gradient between two solutions is a renewable source of energy. Among the technologies able to exploit the salinity gradient, reverse electrodialysis (RED) is an electrochemical process for electrical power generation through direct conversion. Ion exchange membranes, piled alternately and separated by net spacers or membrane profiles, are the key elements of a RED stack. A multiplex phenomenology occurs in RED units; Ohmic and non-Ohmic (due to concentration changes) voltage losses and pressure drop are the main issues, and the membrane/channel configuration is crucial for the stack performance. In this framework, mathematical modelling can be a powerful tool for predictive purpos…

Settore ING-IND/24 - Principi Di Ingegneria ChimicaSettore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSettore ING-IND/25 - Impianti ChimiciSettore ING-IND/06 - FluidodinamicaSalinity gradient energy Reverse electrodialysis CFD Process modelSettore ING-IND/19 - Impianti Nucleari
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CFD simulation of gas-liquid hydrodynamics in a rectangular air–lift loop reactor

2006

Computational Fluid Dynamics is an increasingly important tool for carrying out realistic simulations of process apparatuses. As a difference from single phase systems, for multi phase systems the development of CFD models is still at its early stages. Moreover, gas-liquid systems are characterised by an additional complexity level, related to the fact that, as a difference with solid-liquid systems, bubble sizes are not known in advance, being rather the result of formation and breakage-coalescence dynamics, and therefore of complex phenomena related to flow dynamics and interfacial effects. In the present work CFD simulations of gas-liquid air-lift reactors are reported. All bubbles are a…

Settore ING-IND/25 - Impianti ChimiciComputational fluid dynamics
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USE OF SUPERCRITICAL CO2 AS DISSOLVED GAS FOR THE ATOMIZATION OF ETHANOL

2011

Supercritical dissolved gas atomization (SDGA) is an atomization process in which carbon dioxide at temperatures and pressures above its critical point is used as atomizing gas. In this work SDGA has been experimentally studied when ethanol is used as the liquid to be atomized. The spray characteristics in terms of droplets size and distribution have been investigated using a droplet size analyzer based on a laser diffraction method. Very narrow droplet size distributions were produced down to 2.5 μm. The main parameter that influences the droplets size is the gas to liquid mass ratio. From the point of view of the atomization mechanism, mean droplet diameter is mainly influenced by the two…

Settore ING-IND/25 - Impianti Chimicisupercritical fluids atomization dissolved gas
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Turbulent heat transfer in spacer-filled channels: Experimental and computational study and selection of turbulence models

2019

Abstract Heat transfer in spacer-filled channels of the kind used in Membrane Distillation was studied in the Reynolds number range 100–2000, encompassing both steady laminar and early-turbulent flow conditions. Experimental data, including distributions of the local heat transfer coefficient h, were obtained by Liquid Crystal Thermography and Digital Image Processing. Alternative turbulence models, both of first order (k-e, RNG k-e, k-ω, BSL k-ω, SST k-ω) and of second order (LRR RS, SSG RS, ω RS, BSL RS), were tested for their ability to predict measured distributions and mean values of h. The best agreement with the experimental results was provided by first-order ω-based models able to …

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimici020209 energyLiquid crystal thermographyMembrane distillation02 engineering and technologyHeat transfer coefficientMembrane distillation01 natural sciences010305 fluids & plasmassymbols.namesakeComputational fluid dynamic0103 physical sciencesDigital image processingHeat transfer0202 electrical engineering electronic engineering information engineeringRange (statistics)Overlapped spacerSettore ING-IND/19 - Impianti NucleariRANS turbulence modelPhysicsTurbulenceGeneral EngineeringReynolds numberLaminar flowMechanicsCondensed Matter PhysicsHeat transfersymbols
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ON THE BUBBLING DYNAMICS OF BINARY MIXTURES OF PARTICLES IN 2D GAS-SOLID FLUIDIZED BEDS

2011

The bubbling behaviour of fluidized beds has been thoroughly investigated in the last decades by means of several techniques, e.g. X-ray, Inductance, Resistance and Impedance based techniques, PIV. In recent years, Digital Image Analysis Techniques have shown their potential for accurate and cost effectively measurements. Most of the work related to bubble behaviour analysis deals with monodispersed particles, while almost all industrial equipment operates with mixtures of particles. Although considerable work has been done in the past with focus on the analysis of the mixing-segregation behaviour and predictions of fluid dynamics regime transitions, a lack of knowledge exists in the analys…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciBINARY MIXTURESBUBBLES FLUIDIZATION MIXTUREBubbling fluidized bedbubbling dynamics
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CFD PREDICTION OF SCALAR TRANPORT 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. Fluid dynamics optimization of the thin channels to be devoted for the RED process 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 and two different spacer (made of either overlapped filaments or woven filaments) filled channels. Two passive scalars were transported along with the water in orde…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciCFD Salinity Gradient Power renewable energy Reverse Electro Dialysis water electric energy spacer woven polarization concentration concentration boundary layerSettore ING-IND/25 - Impianti ChimiciSettore ING-IND/06 - Fluidodinamica
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Membrane Distillation efficiency increase by enhanced heat transfer

2009

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciComputational Fluid Dynamics Membrane Distillation spacer geometry design optimisationsimulation temperature polarization
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Experimental and computational investigation of hollow-fiber membrane modules for biomedical applications

2022

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciComputational fluid dynamicMass transfer.Porous mediaHemodialysiHollow fiber membrane
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Fluid-structure interaction and flow redistribution in membrane-bounded channels

2019

The hydrodynamics of electrodialysis and reverse electrodialysis is commonly studied by neglecting membrane deformation caused by transmembrane pressure (TMP). However, large frictional pressure drops and differences in fluid velocity or physical properties in adjacent channels may lead to significant TMP values. In previous works, we conducted one-way coupled structural-CFD simulations at the scale of one periodic unit of a profiled membrane/channel assembly and computed its deformation and frictional characteristics as functions of TMP. In this work, a novel fluid&ndash

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciControl and OptimizationMaterials scienceFluid structure interactionEnergy Engineering and Power Technologycomputational fluid dynamics02 engineering and technologyComputational fluid dynamicsComputational fluid dynamicslcsh:TechnologyNumerical modelElectromembrane process020401 chemical engineeringComputational fluid dynamicHydraulic permeabilityReversed electrodialysisFluid–structure interactionMembrane deformationSDG 7 - Affordable and Clean Energy0204 chemical engineeringElectrical and Electronic EngineeringElectromembrane proceEngineering (miscellaneous)Profiled membraneSettore ING-IND/19 - Impianti NucleariIon exchange membraneDarcy's lawSuperficial velocitylcsh:TRenewable Energy Sustainability and the Environmentbusiness.industryFlow maldistributionMechanicsElectrodialysisDarcy flow021001 nanoscience & nanotechnologyelectromembrane processFlow velocity0210 nano-technologyPorous mediumbusinessSettore ICAR/08 - Scienza Delle CostruzioniEnergy (miscellaneous)
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