Search results for "Anti nuclear"

showing 10 items of 415 documents

Flowblockage failures in the EFIT reactor

2011

Flowblockage EFIT reactorSettore ING-IND/19 - Impianti Nucleari
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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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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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Investigation of the Cooling of Hot Walls by Liquid Water Sprays

1999

An experimental study was conducted for the heat transfer from hot walls to liquid water sprays. Four full cone, swirl spray nozzles were used at different upstream pressures, giving mass fluxes impinging on the wall, G, from 8 to 80 kg m(-2) s(-1), mean droplet velocities, U, from 13 to 28 m s(-1) and mean droplet diameters, D, from 0.4 to 2.2 mm. A target consisting of two slabs of beryllium-copper alloy, each 4 x 5 cm in size and 1.1 mm thick, was electrically heated to about 300 degrees C and then rapidly and symmetrically cooled by water sprays issuing from two identical nozzles. The midplane temperature was measured by a fast response, thin-foil thermocouple and the experimental data …

Fluid Flow and Transfer ProcessesMass fluxSettore ING-IND/24 - Principi Di Ingegneria ChimicaMaterials scienceYield (engineering)Mechanical EngineeringNozzleThermodynamicsMechanicsHeat transfer coefficientCondensed Matter PhysicsHeat TransferCritical Heat FluxHeat fluxThermocoupleHeat transferLeidenfrost temperatureBoilingCooling curveWater spraySettore ING-IND/19 - Impianti Nucleari
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Local Effects of Longitudinal Heat Conduction in Plate Heat Exchangers

2007

Abstract In a plate heat exchanger, heat transfer from the hot to the cold fluid is a multi-dimensional conjugate problem, in which longitudinal heat conduction (LHC) along the dividing walls often plays some role and can not be neglected. Large-scale , or end-to-end, LHC is always detrimental to the exchanger’s effectiveness. On the contrary, if significant non-uniformities exist in the distribution of either convective heat transfer coefficient, small-scale , or local, LHC may actually enhance the exchanger’s performance by improving the thermal coupling between high heat transfer spots located on the opposite sides of the dividing wall.

Fluid Flow and Transfer ProcessesMaterials scienceConvective heat transferMechanical Engineeringlongitudinal heat conductionPlate heat exchangerThermodynamicsconjugate heat transferHeat transfer coefficientMechanicsHeat sinkCondensed Matter Physicsplate heat exchangerHeat transferHeat spreaderMicro heat exchangerPlate fin heat exchangerSettore ING-IND/19 - Impianti Nucleari
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The Nukiyama Curve in Water Spray Cooling: its Derivation from Temperature-Time Histories and its Dependence on the Quantities that Characterize Drop…

2007

Abstract Heat transfer from hot aluminium walls to cold water sprays was investigated. The method used was the transient two-side symmetric cooling of a planar aluminium target, previously heated to temperatures of up to 750 K, by twin sprays issuing from full-cone swirl spray nozzles of various gauge. The target’s mid-plane temperature was recorded during the cooling transient by thin-foil K thermocouples and a high-frequency data acquisition system. In order to determine the wall temperature Tw, the wall heat flux q w ″ and the q w ″ - T w heat transfer (Nukiyama) curve, two different approaches were used: the first was based on the solution of an inverse heat conduction problem, the seco…

Fluid Flow and Transfer ProcessesMaterials sciencespray coolingCritical heat fluxMechanical EngineeringDrop (liquid)Thermodynamicsinverse conduction problemHeat transfer coefficientCondensed Matter Physicsinduction heatingDrop impactPhysics::Fluid DynamicsHeat fluxThermocoupleHeat transferMass flow rateSettore ING-IND/19 - Impianti Nucleari
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