Search results for "Anti nuclear"

showing 10 items of 415 documents

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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Integrated modelling of membrane deformation, fluid dynamics and mass transfer in electromembrane processes

In recent years, water and energy supply issues have drawn the attention of the scientific community to electromembrane processes. Electrodialysis (ED) and Reverse Electrodialysis (RED) are two of the most attractive electromembrane technologies for water desalination and electric energy production from salinity gradients, respectively. In order to gain an important place in the industrial market, technological challenges on various aspects are involved in the optimization of these processes. In this context, profiled membranes exhibit interesting performance. However, the mechanical behavior of the membranes and its interaction with fluid dynamics has been poorly investigated so far. In me…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicielectrodialysifluid-structure interactionmembrane deflectionCFDreverse electrodialysiSettore ING-IND/19 - Impianti NucleariIon exchange membrane
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Comparison of different hollow fibre haemodialysis module configurations by a CFD multiscale approach

2021

Objectives The study aims to predict 3-D flow and solute concentrations fields both for blood and dialysate and overall performance parameters (such as dialysate pressure drop and clearance) for different hollow-fibre haemodialysis modules. Methods A multiscale approach was used. At small (unit cell)-scale, dialysate flow and mass transfer around straight cylindrical fibres arranged in regular lattices were simulated. At module-scale, hydraulic permeabilities and mass transfer coefficients derived from small-scale simulations were used to define two different porous media representative of blood and dialysate, sharing the same volume and exchanging solute. Simulations involved different mod…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicihollow fibre membrane haemodialysis Computational Fluid Dynamics porous media mass transferSettore ING-IND/19 - Impianti Nucleari
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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 prediction of solid particle distribution in baffled stirred vessels under partial to complete suspension conditions

2013

Solid-liquid mixing within tanks agitated by stirrers can be easily encountered in many industrial processes. It is common to find an industrial tank operating at an impeller speed N lower than the minimum agitation speed for the suspension of solid particles: under such conditions the distribution of solid-particles is very far from being homogeneous and very significant concentration gradients exist. The present work evaluates the capability of a Computational Fluid Dynamics (CFD) model to reliably predict the particle distribution throughout the tank under either partial or complete suspension conditions. A flat bottomed baffled tank stirred by a Rushton turbine was investigated. Both tr…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicilcsh:Computer engineering. Computer hardwareSettore ING-IND/25 - Impianti Chimicilcsh:TP155-156lcsh:TK7885-7895lcsh:Chemical engineeringMixing Solid liquid suspensions CFDSettore ING-IND/19 - Impianti NucleariComputational Fluid Dynamics Baffled Stirred Vessel Solid Liquid Suspension
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Experimental Analysis via Thermochromic Liquid Crystals of the Temperature Local Distribution in Membrane Distillation Modules

2013

A reliable and optimized design of channels for Membrane Distillation (MD) requires knowledge of local temperature distributions within the module. This information is essential to measure the temperature polarization, choice the module configuration (net spacer features, channel size, etc) providing the best process performance. Notwithstanding such crucial aspects, only few studies have been devoted to the experimental characterization of MD channels and none of them includes data on the local temperature distribution. In the present work, an experimental technique based on the use of Thermochromic Liquid Crystals (TLCs) and digital image processing, previously proposed by the authors (Pi…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicilcsh:Computer engineering. Computer hardwarelcsh:TP155-156lcsh:TK7885-7895lcsh:Chemical engineeringThermochromic Liquid Crystals Heat Transfer Enhancement Membrane DistillationSettore ING-IND/19 - Impianti Nucleari
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A process model of electrodialysis including membrane deformation effects

2020

Electrodialysis (ED) is an electro-driven process that makes use of ion exchange membranes (IEMs) under an applied electric field. The main application of ED is the desalination for drinking water production. A transmembrane pressure (TMP) distribution may arise in ED stacks due to an uneven pressure distribution in the two fluid channels, thus causing membrane/channel deformation and flow redistribution. This can occur in large-scale non-parallel configurations, e.g. crossflow arrangements. Detrimental effects of membrane deformation have widely been studied with reference to several membrane processes. However, this aspect has been neglected in ED applications. In this work, a novel proce…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicimembrane deformationElectrodialysiSettore ICAR/08 - Scienza Delle CostruzioniSettore ING-IND/19 - Impianti Nuclearimulti-scale model
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