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1、Heat Transfer ModelingHeadlamp modeled withDiscrete OrdinatesRadiation ModelOutlineIntroductionConjugate Heat TransferNatural ConvectionRadiationPeriodic Heat TransferIntroductionEnergy transport equation:Energy source due to chemical reaction is included for reacting flows.Energy source due to spec
2、ies diffusion included for multiple species flows.Always included in coupled solver; can be disabled in segregated solver.Energy source due to viscous heating:Describes thermal energy created by viscous shear in the flow.Important when shear stress in fluid is large (e.g., lubrication) and/or in hig
3、h-velocity, compressible flows.Often negligiblenot included by default for segregated solver; always included for coupled solver.In solid regions, simple conduction equation solved.Convective term can also be included for moving solids.Conjugate Heat TransferAbility to compute conduction of heat thr
4、ough solids, coupled with convective heat transfer in fluid.Coupled Boundary Condition:available to wall zone that separates two cell zones.GridTemperature contoursVelocity vectorsExample: Cooling flow over fuel rodsNatural Convection - IntroductionNatural convection occurswhen heat is added to flui
5、dand fluid density varieswith temperature.Flow is induced by force ofgravity acting on densityvariation.When gravity term isincluded, pressure gradientand body force term in themomentum equation are re-written as:whereThis format avoids potential roundoff error when gravitational body force term is
6、included.Natural Convection the Boussinesq ModelBoussinesq model assumes the fluid density is uniform Except for the body force term in the momentum equation along the direction of gravity, we have:Valid when density variations are small (i.e., small variations in T).It provides faster convergence f
7、or many natural-convection flows than by using fluid density as function of temperature.Constant density assumptions reduces non-linearity.Suitable when density variations are small.Cannot be used together with species transport or reacting flows.Natural convection problems inside closed domains:For
8、 steady-state solver, Boussinesq model must be used.The constant density, o, properly specifies the mass of the domain.For unsteady solver, Boussinesq model or ideal-gas law can be used. Initial conditions define mass in the domain.User Inputs for Natural Convection1. Set gravitational acceleration.
9、Define Operating Conditions.2. Define density model.If using Boussinesq model:Select Boussinesq as the Density method and assign constant value, o.Define Materials.Set Thermal Expansion Coefficient, .Set Operating Temperature, To.If using temperature dependent model, (e.g., ideal gas or polynomial):
10、Specify Operating Density or,Allow Fluent to calculate o from a cell average (default, every iteration).RadiationRadiation effects should be accounted for when is of equal or greater magnitude than that of convective and conductive heat transfer rates.To account for radiation, radiative intensity tr
11、ansport equations (RTEs) are solved.Local absorption by fluid and at boundaries links RTEs with energy equation.Radiation intensity, I(r,s), is directionally and spatially dependent.Intensity, I(r,s), along any direction can be modified by:Local absorptionOut-scattering (scattering away from the dir
12、ection)Local emissionIn-scattering (scattering into the direction)Five radiation models are provided:Discrete Ordinates Model (DOM)Discrete Transfer Radiation Model (DTRM)P-1 Radiation ModelRosseland ModelSurface-to-Surface (S2S)Discrete Ordinates ModelThe radiative transfer equation is solved for a
13、 discrete number of finite solid angles, si:Advantages:Conservative method leads to heat balance for coarse discretization.Accuracy can be increased by using a finer discretization.Most comprehensive radiation model:Accounts for scattering, semi-transparent media, specular surfaces, and wavelength-d
14、ependent transmission using banded-gray option.Limitations: Solving a problem with a large number of ordinates is CPU-intensive.absorptionemissionscatteringDiscrete Transfer Radiation Model (DTRM)Main assumption: radiation leaving surface element in a specific range of solid angles can be approximat
15、ed by a single ray.Uses ray-tracing technique to integrate radiant intensity along each ray:Advantages:Relatively simple model.Can increase accuracy by increasing number of rays.Applies to wide range of optical thicknesses.Limitations:Assumes all surfaces are diffuse. Effect of scattering not includ
16、ed.Solving a problem with a large number of rays is CPU-intensive.P-1 ModelMain assumption: Directional dependence in RTE is integrated out, resulting in a diffusion equation for incident radiation. Advantages:Radiative transfer equation easy to solve with little CPU demand. Includes effect of scatt
17、ering. Effects of particles, droplets, and soot can be included.Works reasonably well for combustion applications where optical thickness is large.Limitations:Assumes all surfaces are diffuse. May result in loss of accuracy, depending on complexity of geometry, if optical thickness is small.Tends to
18、 overpredict radiative fluxes from localized heat sources or sinks.Surface-to-Surface Radiation ModelThe S2S radiation model can be used for modeling enclosure radiative transfer without participating media.e.g., spacecraft heat rejection system, solar collector systems, radiative space heaters, and
19、 automotive underhood coolingView-factor based modelNon-participating media is assumed.Limitations: The S2S model assumes that all surfaces are diffuse. The implementation assumes gray radiation. Storage and memory requirements increase very rapidly as the number of surface faces increases.Memory re
20、quirements can be reduced by using clusters of surface faces.Clustering does not work with sliding meshes or hanging nodes. Not to be used with periodic or symmetry boundary conditions. Cannot be used for models with multiple enclosures geometry.Choosing a Radiation ModelFor certain problems, one ra
21、diation model may be more appropriate in general.Define Models Radiation.Computational effort: P-1 gives reasonable accuracy with less effort.Accuracy: DTRM and DOM more accurate.Optical thickness: DTRM/DOM for optically thin media (optical thickness 1); P-1 better for optically thick media.Scatteri
22、ng: P-1 and DOM account for scattering.Particulate effects: P-1 and DOM account for radiation exchange between gas and particulates.Localized heat sources: DTRM/DOM with sufficiently large number of rays/ ordinates is more appropriate. Periodic Heat Transfer (1)Also known as streamwise-periodic or f
23、ully-developed flow.Used when flow and heat transfer patterns are repeated, e.g.,Compact heat exchangersFlow across tube banksGeometry and boundary conditions repeat in the streamwise direction.Outflow at one periodic boundary is inflow at the otherinflowoutflowPeriodic Heat Transfer (2)Temperature (and pressure) vary in the streamwise direction.Scaled temperature (and periodic pressure) is same at periodic boundaries. For fixed wall temperature problems, scaled temperature defined as: Tb = suitably defined bulk temperatureCan also model flows with s
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