Search results for "IMPIANTI"

showing 10 items of 797 documents

Experimental investigation of the effects of efficiency promoters in a MSF lab-scale unit

2006

Flashing promoters MSF DesalinationSettore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSettore ING-IND/25 - Impianti Chimici
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Flowblockage failures in the EFIT reactor

2011

Flowblockage EFIT reactorSettore ING-IND/19 - Impianti Nucleari
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Modelling Nannochloropsis gaditana Growth in Reactors with Different Geometries, Determination of Kinetic Parameters and Biochemical Analysis in Resp…

2022

Microalgae are unicellular and photosynthetic microorganisms which grow thanks to inorganic salts, CO2 and light, and find applications in several fields thanks to their variety. The industrial application of microalgae has not often been fully exploited because of a lack of information about how microalgae respond to inputs and to different growth environments. In the present work a model able to predict the microalgae growth in reactors with different geometries was developed. We combined a Monod-like model for the specific growth rate with the Lambert-Beer law of homogeneous light distribution in thick photobioreactors. Kinetic parameters related to the cultivation of the microalga Nanno…

Fluid Flow and Transfer Processes<i>Nannochloropsis gaditana</i>; photobioreactor modelling; growth model; lipids; kinetic parametersProcess Chemistry and TechnologySettore ING-IND/25 - Impianti ChimiciGeneral EngineeringGeneral Materials ScienceGrowth model Kinetic parameters Lipids Nannochloropsis gaditana Photobioreactor modellingInstrumentationComputer Science ApplicationsApplied Sciences; Volume 12; Issue 12; Pages: 5776
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A Semi-Theoretical Approach to a Correlation for the Thermal Conductivity of a Beryllium Pebble Bed

2003

In the framework of the European Fusion Technology Programme, Lithium ceramics and Beryllium packed pebble beds are foreseen to be used as Tritium breeders and neutron multipliers, respectively, for the Helium Cooled Pebble Bed breeding blanket of a fusion power reactor operating with a D-T plasma. The present work is focused on the semi-theoretical investigation of the thermal conductivity of single size Beryllium pebble beds, starting from the main hypothesis that this conductivity depends linearly on pebble bed local temperature and total volumetric strain and introducing a method to determine the coefficients of such dependence on the basis of the results obtained by the SUPER-PEHTRA ex…

Fluid Flow and Transfer ProcessesBERYLLIUM PEBBLE BED THERMAL CONDUCTIVITYMaterials scienceMechanical EngineeringNuclear engineeringchemistry.chemical_elementFusion powerBlanketCondensed Matter PhysicsThermal conductivitychemistryThermalNeutronBerylliumPebbleHeliumSettore ING-IND/19 - Impianti Nucleari
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A geometric approach for predicting vertical stationary profiles of weakly inertial advecting-diffusing particles in closed incompressible flows

2004

Abstract Mixing of weakly inertial particles in closed flows is often addressed by considering individual particles as passive advecting-diffusing tracers, subjected to an additional settling velocity resulting from body forces (e.g. gravity). We show that the qualitative and quantitative features of the vertical particle distribution (i.e. the horizontal cross-sectional averages of particle concentration) can be predicted from the structure of the flow resulting from the superposition of the stirring field and the settling velocity. The prediction is based upon the observation that the resulting flow can be divided into two nonoverlapping regions, namely trajectories that are confined with…

Fluid Flow and Transfer ProcessesBody forcePhysicsInertial frame of referenceField (physics)TurbulenceMechanical EngineeringSettore ING-IND/25 - Impianti ChimiciGeneral Physics and AstronomyMechanicsPhysics::Fluid Dynamicsmixing multiphase systemsCFDClassical mechanicsFlow (mathematics)SettlingParticleMixing (physics)inertial particles
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Influence of bundle porosity on shell-side hydrodynamics and mass transfer in regular fiber arrays: A computational study

2023

CFD predictions of the effects of a fiber bundle porosity on shell-side hydrodynamics and mass transfer under conditions of steady laminar flow were obtained. Fluid was assumed to flow around regular hexag-onal or square arrays of cylindrical fibers of different pitch to diameter ratios, yielding bundle porosities ranging from the theoretical minimum up to similar to 1. A large number of axial, transverse and mixed flow combinations were simulated by letting the axial and transverse flow Reynolds numbers and the trans-verse flow attack angle vary. Both fully developed and developing conditions (entrance effects) were con-sidered. The continuity and momentum equations, along with a transport…

Fluid Flow and Transfer ProcessesComputational Fluid Dynamics Hollow fiber membrane Entrance effects Darcy permeability Mass transfer coefficient HemodialysisSettore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciMass transfer coefficientHemodialysisSettore ING-IND/25 - Impianti ChimiciMechanical EngineeringEntrance effectsComputational Fluid DynamicsCondensed Matter PhysicsDarcy permeabilitySettore ING-IND/19 - Impianti NucleariHollow fiber membraneInternational Journal of Heat and Mass Transfer
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Low-Prandtl Number Natural Convection in Volumetrically Heated Rectangular Enclosures - III. Shallow Cavity, AR=0.25

2001

Abstract Natural convection in a volumetrically heated rectangular enclosure filled with a low-Prandtl number (Pr=0.0321) fluid was studied by direct numerical two-dimensional simulation. The enclosure had isothermal side walls and adiabatic top/bottom walls. The aspect ratio was 4 and the Grashof number Gr, based on conductive maximum temperature and cavity width, ranged from 3.79 × 104 to 1.26 × 109. According to the value of Gr, different flow regimes were obtained: steady-state, periodic, and chaotic. The first instability of the steady-state solution occurred at Gr≈3×105; the resulting time-periodic flow field consisted of a central rising plume and of convection rolls, periodically ge…

Fluid Flow and Transfer ProcessesConvectionNatural convectionMaterials scienceNatural ConvectionEnclosureMechanical EngineeringPrandtl numberEnclosureGrashof numberThermodynamicsInternal Heat GenerationMechanicsCondensed Matter PhysicsNusselt numberPlumePhysics::Fluid Dynamicssymbols.namesakeCombined forced and natural convectionsymbolsCFDSettore ING-IND/19 - Impianti Nucleari
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MHD free convection in a liquid-metal filled cubic enclosure. II. Internal heating

2002

The buoyancy-driven magnetohydrodynamic flow in a liquid-metal filled cubic enclosure was investigated by three-dimensional numerical simulation. The enclosure was differentially heated at two opposite vertical walls, all other walls being adiabatic, and a uniform magnetic field was applied orthogonal to the temperature gradient and to the gravity vector. The Rayleigh number was 105 and the Prandtl number was 0.0321 (characteristic of Pb–17Li at 573 K). The Hartmann number was made to vary between 102 and 103 and the electrical conductance of the walls between 0 and ∞. The continuity, momentum and enthalpy transport equations, in conjunction with a Poisson equation for the electric potentia…

Fluid Flow and Transfer ProcessesConvectionPhysicsNatural convectionEnclosureMechanical EngineeringPrandtl numberEnclosureFree ConvectionInternal Heat GenerationThermodynamicsRayleigh numberMechanicsMagnetohydrodynamicCondensed Matter PhysicsHartmann numberPhysics::Fluid Dynamicssymbols.namesakesymbolsMagnetohydrodynamic driveMagnetohydrodynamicsCFDSettore ING-IND/19 - Impianti NucleariInternational Journal of Heat and Mass Transfer
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Investigation of Flow and Heat Transfer in Corrugated-Undulated Plate Heat Exchangers

2000

An experimental and numerical investigation of heat transfer and fluid flow was conducted for corrugated-undulated plate heat exchanger configurations under transitional and weakly turbulent conditions. For a given geometry of the corrugated plates the geometrical characteristics of the undulated plates, the angle formed by the latter with the main flow direction, and the Reynolds number were made to vary. Distributions of the local heat transfer coefficient were obtained by using liquid-crystal thermography, and surface-averaged values were computed; friction coefficients were measured by wall pressure tappings. Overall heat transfer and pressure drop correlations were derived. Three-dimen…

Fluid Flow and Transfer ProcessesDynamic scraped surface heat exchangerMaterials scienceHeat transfer enhancementPlate heat exchangerThermodynamicsTurbulence modelHeat transfer coefficientMechanicsCondensed Matter PhysicsHeat TransferChurchill–Bernstein equationNusselt numberPhysics::Fluid DynamicsFluid flowbody-fitted gridHeat transferMicro heat exchangerPlate heat exchangerCFDSettore ING-IND/19 - Impianti Nucleari
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MHD free convection in a liquid-metal filled cubic enclosure. I. Differential heating

2002

Fluid Flow and Transfer ProcessesEnclosureMechanical EngineeringFree ConvectionMagnetohydrodynamicCFDCondensed Matter PhysicsSettore ING-IND/19 - Impianti NucleariInternational Journal of Heat and Mass Transfer
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