1-steady state heat conduction

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    Steady state heat

    conduction

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    Heat Transfer

    A background in ODE

    Important analogies between heat,

    mass, and momentum transfer

    Heat transfer is the science that seeksto predict energy transfer that may

    take place between material bodies asa result of a temperature difference.

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    The science of heat transfer seeks

    to predict the rateat which the heatexchange will take place under

    certain specified conditions.

    Thus, heat transfer rate is the

    desired objective

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    Difference between Heat Transferand Thermodynamics

    Thermodynamics deals with the systems inequilibrium.

    Heat transfer predicts how fast change of asystem from one state to another will takeplace.

    Heat transfer supplements First and SecondLaws of Thermodynamics with additionalexperimental rules.

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    Consider the cooling of a hot steelbar placed in a jar full of water __

    Thermodynamics may be used to predictthe final equilibrium temperature of the

    steel bar water combination.

    Thermodynamics will not tell us how longit takes to reach this equilibriumcondition, or what the temperature ofthe bar will e after a certain length oftime before equilibrium is achieved.

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    The three modes of heat transfer are:

    Conduction,

    convection,

    and radiation.

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    x

    T

    A

    q

    x

    TkAq

    Conduction heat transfer:When a temperature gradient exists in a

    body, there is an energy transfer from the

    high-temperature region to the low-temperature region.

    The heat transfer rate per unit area isproportional to the normal temperature

    gradient,Here, q is the heat transfer rate

    and

    is temperature gradient in the

    direction of heat flow.

    k is a positive constant, called

    thermal con duct iv i tyof the

    material, W/m/OC

    x

    T

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    Three-dimensional analysis:

    Heat conduction in and out of a unit volume in all threedirections: Energy balance

    Total heat conducted in to the system+ the heatgenerated within the system= the total heatconducted out of the system+ the change ininternal energy of the system

    E

    qqqqqqq dzzdyydxxgenzyx

    x

    T

    kdydzqx

    dydzdx

    x

    Tk

    xx

    Tkq dxx

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    Cartesian Coordinates:

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    y

    Tkdxdzqy

    dxdzdyy

    Tk

    yy

    Tkq dyy

    z

    Tkdxdyqz

    dxdydz

    z

    Tk

    zz

    Tkq dzz

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    dxdydzqqgen

    T

    Cdxdydzd

    dE

    T

    Cqz

    Tk

    zy

    Tk

    yx

    Tk

    x

    Substituting the above all in the energy balance equation

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    T

    kq

    zT

    yT

    xT 1

    2

    2

    2

    2

    2

    2

    C

    k

    For constant thermal conductivity,

    Here,

    is thermal diffusivity.

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    Special Cases:

    Steady state one-dimensional heat flow (no heat generation)

    02

    2

    x

    T (1.4)

    Two-dimensional steady state conduction without heat

    sources(1.7)

    02

    2

    2

    2

    y

    T

    x

    T

    Steady state one-dimensional heat flow with heat sources

    (1.6)

    02

    2

    k

    q

    x

    T

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    Steady state one-dimensional heat flow incylindrical coordinates

    01

    2

    2

    dr

    dT

    rr

    T (1.5)

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    Thermal conductivity

    The Mechanism of Thermal Conduc t iv i ty in aGas

    We identify the kinetic energy of a molecule with

    its temperature. Thus, in a high-temperatureregion, the molecules have higher velocities than

    in some lower temperature region. The

    molecules are in continuous random motion,

    colliding with one another and exchanging

    energy and momentum.

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    The molecules have this randommotion whether or not a temperaturegradient exists in a gas. If a moleculemoves from a high-temperature region

    to a low-temperature region, ittransports the kinetic energy to thelower temperature part of the system

    and gives up this energy thrucollisions with lower-energy molecules.

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    In general, thermal conductivity is

    strongly temperature-dependent.

    The numerical value of thermal

    conductivity indicates how fast heat will

    flow in a given material.

    The faster the molecules move, the

    faster they will transport energy.

    Therefore, the thermal conductivity of a

    gas depends on temperature.

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    Thermal conductivity, k, of a gas varies as

    Tk

    where T is absolute temperature. For most

    gases at moderate pressures, k is a function

    of temperature alone.

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    Thermal energy may be conducted in

    so l ids by two modes:Lattice vibrations, and

    Transport by free electrons.

    In good electric conductors, a large number

    of free electrons move about in the lattice of

    material. These electrons also carry thermalenergy from a high-temperature region to a

    low-temperature region. These electrons are

    thus referred to as electron gas.

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    Energy may also be transported as

    vibrational energy in the latticestructure of a material. But this

    component is usually smaller than

    electron transport.

    Thus, good electrical conductors arealmost always good heat conductors.

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    Thermal conduct iv i ty at 0OC

    Copper (pure) 385 W/m OC

    Diamond 2300

    Sawdust 0.059

    Glass wool 0.038

    Window glass 0.78

    Ice 2.22

    Hg 8.21Water 0.556

    Air 0.024

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    Steady state one-dimensional heat flow (no heat generation)

    02

    2

    x

    T

    Integrating once

    dT/dx = C1 >>>>> eqn. 1

    Integrating again

    T = C1 * x + C2 >>>>>>> eqn. 2

    Applying Boundry condtions x=0 , T=T1 and x=L , T=T2

    C2 = T1 and C1 = (T2-T1)/L

    Q = - KA dT/dx = K A ( T1-T2)/L

    or Q = ( T1-T2)/ ( L/ KA)

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    1-Dimensional Heat Conduction

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    20

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    A flat wall is exposed to the environment

    temperature of 27C. The wall is covered with twolayers of insulation of 2.5 mm thickness each

    whose thermal conductivities are 1.4 and 1.7 W/m-

    K respectively. The wall loses heat to the

    environment by convection. Compute the value ofthe convection heat transfer coefficient which must

    be maintained on the outer surface of the insulation

    to ensure that the outer surface temperature does

    not exceed 41C. The innermost surface is

    maintained at a temp of 70C.

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