Heat Transfet Basics

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  • 7/29/2019 Heat Transfet Basics

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    ME601 1/18/06Slide 1

    Heat Transfer Heat transfer modes:

    conduction - heat transfer through a solid

    convection - heat transfer from a surface to a fluid

    radiation - heat transfer from surface-to-surface via electromagneticwaves

    In this class, you will concentrate on solving heat transfer problemsnumerically rather than analytically

    However, proper use of numerical software requires that you understandheat transfer theory sufficiently to:

    understand the important aspects of your problem (what can andcannot be neglected)

    develop appropriate sanity checks for your solution

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    ME601 1/18/06Slide 2

    Conduction

    Conduction is governed by Fouriers law:

    x

    Tq k A

    x

    heat transfer in x-direction

    thermal conductivity

    temperature gradient

    x

    T

    xq

    area x-direction

    one sanity check is that the temperature distribution makes sense relative to Fouriers law

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    ME601 1/18/06Slide 3

    Conduction Resistances

    TH TC

    L

    The analysis of conduction withinsimple geometries can be conciselysummarized in the form of thermal

    resistances

    For example, the analysis of 1-D,

    steady state conduction through aplane wall leads to:

    A

    TH

    TCq

    H Ck A

    q T T

    L

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    ME601 1/18/06Slide 4

    Resistance Concept

    H Ck A

    q T TL

    heat transfer temperature difference

    1 21

    e

    I V VR

    Ohms LawHeat Transfer

    current voltage difference

    electrical resistance(thermal resistance)-1

    1

    H C

    pw

    q T TR

    length you have to conduct

    conductivity area available for conductionpw

    LR

    k A

    whereRpw is the thermal resistance associated with conduction through a plane wall:

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    ME601 1/18/06Slide 5

    Conduction through Other Shapes

    ln

    2

    out

    in

    cyl

    r

    rR

    L k

    1H C

    cyl

    q T T

    R

    where

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    ME601 1/18/06Slide 6

    Conduction through Other Shapes

    1 1 1

    4sph

    in out

    Rk r r

    1H C

    sph

    q T TR

    where

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    7/15ME601 1/18/06Slide 7

    Convection Resistance

    surface temperature = Ts

    fluid temperature = Tf

    convq

    Newtons law of cooling:

    conv s s f q h A T T

    heat transfer temperature difference

    (thermal resistance)-1

    1

    conv s f

    conv

    q T TR

    1conv

    s

    Rh A

    whereRconv is the thermal resistance associated with convection:

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    Radiation Resistance

    surface emissivity, esurface temperature = Ts

    surrounding surfaces at temperature = Tsur

    radq

    heat transfertemperature difference

    (thermal resistance)-1

    1

    rad s f rad

    q T TR

    32 21 1

    4rad

    ss s sur s sur

    RA TA T T T T e e

    whereRrad is the thermal resistance associated with radiation:

    4 4rad s s sur q A T T e

    2 2rad s s sur s sur s sur q A T T T T T T e

    -82 4W5.67x10 m K

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    Why Should I Care?

    Understanding you can quickly discern what is controlling the heat

    transfer in your problem by estimating thermal resistances

    Analytical Verification you can sometimes simplify your numericalproblem to a point where it can be exactly verified against these

    analytical, resistance solutions

    Sanity Check you can always see if your numerical solution makessense by calculating thermal resistances

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    10/15ME601 1/18/06Slide 10

    Heater in a Bathroom Floor

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    11/15ME601 1/18/06Slide 11

    Resistance Network Model

    air at Tair,1 = 15C

    air at Tair,2 = 5C

    plywood

    studs

    airdrywall

    strip heater

    lineoleum

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    Th

    Tair,2= 5C

    hq

    Rp=

    0.002 K/W

    Rs =0.15 K/W

    Rair=

    0.46 K/W

    Rd=0.014 K/W

    Rconv =

    0.011 K/W

    RL =

    0.016 K/W

    Tair,1= 15C

    Rconv =

    0.011 K/W

    TL

    1q2q

    Resistance Values

    What can you learn from this?

    most of the heat will go to the bathroom

    most of the heat will go through the studs

    the characteristics of the drywall, plywood and basement convection do not matter

    the characteristics of the studs, linoleum, and bathroom convection do matter

    you can estimate the heater temperature and heater power required

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    Bracket

    k = 14 W/m-K

    thickness = 1 cm

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    FE Analysis

    predicted heat flow is 1.84 W

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    ME601 1/18/06Slide 15

    Resistance Analysis Sanity Check

    2

    19cm m K 100 cm K 136

    14 W 1 cm m Wbracket

    LR

    k A

    200 C 20 C W1.33W

    136 K

    H C

    bracket

    T Tq

    R

    length you have to conduct

    conductivity area available for conductionpw

    LR

    k A