Fourier Conduction

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    Fouriers Law

    and the

    Heat Equation

    Chapter Two

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    Fouriers Law

    A rate equationthat allows determination of the conduction heat flux

    from knowledge of the temperature distriutionin a medium

    Fouriers Law

    !ts most general "#ector$ form for multidimensional conduction is%

    q k T =

    !mplications%

    & Heat transfer is in the direction of decreasing temperature

    "asis for minus sign$'

    & (irection of heat transfer is perpendicular to lines of constant

    temperature "isotherms$'

    & Heat flux #ector ma) e resol#ed into orthogonal components'

    & Fouriers Law ser#es to define the thermal conducti#it)of the

    medium

    *k q T

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    Heat Flux Components

    "+',-$T T Tq k i k j k k r r z

    =

    rq q zq

    C)lindrical Coordinates% ( ). .T r z

    sin

    T T Tq k i k j k k

    r r r

    =

    "+'+,$

    rq q q

    /pherical Coordinates% ( ). .T r

    Cartesian Coordinates% ( ). .T x y z

    T T T

    q k i k j k k x y z

    = xq yq zq

    "+'0$

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    Heat Flux Components "cont'$

    !n angular coordinates . the temperature gradient is still

    ased on temperature change o#er a length scale and hence has

    units of C*m and not C*deg'

    ( )or .

    Heat ratefor one1dimensional. radial conductionin a c)linder or sphere%

    & C)linder

    +r r r r q A q rLq = =

    or.

    +r r r r q A q rq = =

    & /phere

    +2r r r r q A q r q = =

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    Heat Equation

    The Heat Equation A differential equation whose solution pro#ides the temperature distriution in a

    stationar) medium'

    3ased on appl)ing conser#ation of energ) to a differential control #olume

    through which energ) transfer is exclusi#el) ) conduction'

    Cartesian Coordinates%

    4et transferof thermalenerg) into the

    control #olume "inflow1outflow$

    p

    T T T T k k k q c

    x x y y z z t

    + + + =

    "+',0$

    Thermal energ)

    generationChange in thermal

    energ) storage

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    Heat Equation "5adial /)stems$

    +

    , ,

    p

    T T T T

    kr k k q cr r r z z t r

    + + + =

    "+'+6$

    /pherical Coordinates%

    C)lindr

    ical Coordinates%

    +

    + + + +

    , , ,sin

    sin sin p

    T T T T kr k k q c

    r r tr r r

    + + + =

    "+'00$

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    Heat Equation "/pecial Case$

    7ne1(imensional Conductionin a 8lanar 9ediumwith Constant 8roperties

    and4o :eneration

    +

    +

    ,T T

    tx

    =

    thermal diffu osi#it f the med) iump

    k

    c

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    3oundar) Conditions

    3oundar) and !nitial Conditions For transient conduction. heat equation is first order in time. requiring

    specification of an initial temperature distriution% ( ) ( )6

    . .6t

    T x t T x= =

    /ince heat equation is second order in space. twooundar) conditions

    must e specified' /ome common cases%

    Constant /urface Temperature%

    ( )6. sT t T=

    Constant Heat Flux%

    6;x s

    T

    k qx =

    =

    Applied Flux Insulated Surface

    6; 6x

    T

    x =

    =

    Con#ection

    ( )6; 6.xT

    k h T T t x

    =

    =

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    8roperties

    Thermoph)sical 8roperties

    Thermal Conducti#it)% A measure of a materials ailit) to transfer thermal

    energ) ) conduction'

    Thermal (iffusi#it)% A measure of a materials ailit) to respond to changes

    in its thermal en#ironment'

    8ropert) Tales%

    /olids% Tales A', & A'0

    :ases% Tale A'2

    Liquids% Tales A'< & A'=

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    Conduction Anal)sis

    9ethodolog) of a Conduction Anal)sis

    /ol#e appropriate form of heat equation to otain the temperature

    distriution'

    >nowing the temperature distriution. appl) Fouriers Law to otain the

    heat flux at an) time. location and direction of interest'

    Applications%

    Chapter 0% 7ne1(imensional. /tead)1/tate Conduction

    Chapter 2% Two1(imensional. /tead)1/tate Conduction

    Chapter

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    8rolem % Thermal 5esponse of 8lane ?all

    8rolem +'2@ Thermal response of a plane wall to con#ection heat transfer'

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    8rolem% Thermal 5esponse "Cont'$

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    in con# s6E q A dt

    =

    d$ The total energ) transferred to the wall ma) e expressed as

    ( )( )in s 6E hA T T L.t dt

    =

    (i#iding oth sides ) AsL. the energ) transferred per unit #olume is

    ( ) 0in6

    E hT T L.t dt *m

    B L

    =

    8rolem% Thermal 5esponse "Cont'$

    8 l 4 if : i d

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    8rolem% 4on1niform :eneration due

    to 5adiation Asorption

    8rolem +'+- /urface heat fluxes. heat generation and total rate of radiation

    asorption in an irradiated semi1transparent material with a

    prescried temperature distriution'

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    8rolem% 4on1niform :eneration "Cont'$

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    8rolem% 4on1niform :eneration "Cont'$