Lecture of Heat Transfer

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Lecture Objectives: • Review - Heat transfer – Convection – Conduction – Radiation Analysis of a practical problem

description

Review of Heat transfer mechanisms:Convection Conduction Radiation&Analysis of a practical problem

Transcript of Lecture of Heat Transfer

  • Lecture Objectives:Review - Heat transferConvection Conduction Radiation

    Analysis of a practical problem

  • Example Problem radiant barrier in attic

  • Example Problem heat transfer in window construction

  • Convection

  • Convection coefficient h [W/m2K]ConductionConvection Natural convectionForced convectionL characteristic lengthh natural convectionk air conductionL- characteristic lengthorNusselt number:areaSpecific heat fluxHeat flux

  • Which surface in this classroom has the largest forced convectionA. Window B. CeilingC. WallsD. Floor

    Which surface has the largest natural convection

  • How to calculate h ?

    What are the parametrs that affect h ?

    What is the boundary layer ?

  • Laminar and Turbulent Flowforced convection

  • Forced convection governing equations1) Continuity

    2) Momentumu, v velocities n air viscosityNon-dimensionless momentum equation

    Using

    L = characteristic length and U0 = arbitrary reference velocityReLReynolds number

  • Forced convection governing equationsEnergy equation for boundary layerNon-dimensionless energy equationsT temperature, a thermal diffusivity a=k/rcp, k-conductivity, r - density, cp specific cap. Wall temperatureAir temperature outside of boundary layerInertial forceViscous forceMomentum diffusivity Thermal diffusivityReynolds number Prandtl number

  • Simplified Equation for Forced convection

    For laminar flow: For turbulent flow:For air: Pr 0.7, n = viscosity is constant, k = conductivity is constant General equationSimplified equation:Or:

  • Natural convection

  • GOVERNING EQUATIONSNatural convection Continuity

    Momentum which includes gravitational force

    Energyu, v velocities , n air viscosity , g gravitation, b1/T - volumetric thermal expansion T temperature, air temperature out of boundary layer, a temperature conductivity

  • Characteristic Number for Natural ConvectionNon-dimensionless governing equations

    Using

    L = characteristic length and U0 = arbitrary reference velocity Tw- wall temperatureThe momentum equation becomeMultiplying by Re2 number Re=UL/n Gr

  • Grashof number Characteristic Number for Natural Convection The Grashof number has a similar significance for natural convection as the Reynolds number has for forced convection, i.e. it represents a ratio of buoyancy to viscous forces.Buoyancy forcesViscous forces General equation

  • Even more simpleNatural convection simplified equationsFor laminar flow: For turbulent flow:For air: Pr 0.7, n = constant, k= constant, b= constant, g=constant Simplified equation:Or:T - air temperature outside of boundary layer, Ts - surface temperature

  • Forced and/or natural convectionIn general,Nu = f(Re, Pr, Gr)natural and forced convectionforced convectionnatural convection

  • Combined forced and natural conventionChurchill and Usagi approach :This equation favors a dominant term (h1 or h2), and exponent coefficient n determines the value for hcombined when both terms have the same order of value

  • Example of general forced and natural convectionEquation for convection at cooled ceiling surfacesn

  • What kind of flow is the most common for indoor surfacesA. Laminar B. TurbulentC. TransitionalD. Laminar, transitional, and turbulent

    What about outdoor surfaces?

  • Conduction

  • Conductive heat transferSteady-state

    Unsteady-state

    Boundary conditions

    Dirichlet Tsurface = Tknown

    Neumann

    LTairk - conductivity of materialTS1TS2h

  • Boundary conditionsBiot number

    conventionconduction

  • Importance of analytical solution

  • What will be the daily temperature distribution profile on internal surface for styrofoam wall? A.

    B.External temperature profileTtime

  • What will be the daily temperature distribution profile on internal surface for tin glass? A.

    B.External temperature profileTtime

  • Conduction equation describes accumulation

  • Important numbersInertial forceViscous forceReynolds number Momentum diffusivity Thermal diffusivityPrandtl number Buoyancy forcesViscous forces ConductionConvection Nusselt number thermal internal resistance surface film resistance Grashof number Biot number Reference book: Fundamentals of Heat and Mass Transfer, Incropera & DeWitt

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