(5) transient conduction - lumped cap mtd - s1 2013-2014 (1)

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    Dr. K.C. Leong, 2006

    Lecture 2:Radiation & Conservation of Energy Requirement

    (5) Trans ient Conduc t ion : Lumped

    Capacitance Methodby

    Assoc Prof Leong Kai ChoongSchool of Mechanical and Aerospace Engineering

    MA3003/MP3003/AE3003 Heat TransferSemester 1, AY 2013-2014

    Read Chapter 4: Section 4-1 of the

    textbook before these lecture

    slides

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    2

    At the end of these lectures, you should be able to

    assess when the spatial variation of temperature of a

    solid is negligible and temperature varies nearly

    uniformly with time, making the lumped capacitance

    analysis applicable,

    calculate the time taken by a solid to reach some

    temperature Tor the temperature reached by a solid

    at some time t,

    calculate the amount of heat transferred (in J) during

    the transient conduction process, and perform general lumped capacitance calculations.

    Learning Objectives

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    3

    Transient Conduction

    Solid body suddenly subjected to change in thermal

    conditions at the boundary temperature varies with

    space and time until steady-state.

    Unsteady, time-dependent ortransient heat

    conduction occurs in the interim period.

    We can solve general heat conduction equation for

    T(x,y,z,t) in solid subject to initial and boundary

    conditions.

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    4

    t

    Tce

    z

    Tk

    zy

    Tk

    yx

    Tk

    xpgen

    For example, solve

    or solve

    with 6 boundary conditions and 1 initial condition

    T(x,y,z,t)

    1

    2

    2

    t

    T

    x

    T

    with two boundary conditions and one initialcondition T(x,t)

    semi-infinite solid

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    5

    Analytical solutions may be obtained for simple

    geometries and conditions.

    Such complicated solutions may be obtained

    from advanced heat transfer texts such as

    Carslaw, H.S. and J.C. Jaeger, Conduction ofHeat in Solids, 2nd ed., Oxford UniversityPress, London, 1959.

    Ozisik, M.N., Heat Conduction, 2nd ed., Wiley,New York, 1993.

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    6

    Lumped Capacitance Method

    Sudden change in thermal environment e.g.quenching of hot metal forging in cooler liquid

    (Figure 1)

    Temperature of solid spatially uniform during

    transient process i.e. no temperature gradients in

    solid

    Approximated if resistance to solid conduction is

    small compared to resistance to convectionbetween solid and fluid.

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    7

    Fig. 1 Cooling of a hot metal forging

    Source: Incropera et al. (2007)

    convQ

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    8

    Temperature of forging cannot be obtained by solving heat

    conduction equation. Take overall energy balance on solid

    (3)exp

    (2)ln

    Write

    0

    tVc

    hA

    TT

    TT

    hA

    Vct

    dtd

    hA

    Vc

    TT

    s

    ii

    i

    s

    t

    si

    convQ

    dt

    dTVcTThA

    EE

    s

    stout

    (1)

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    9

    Fig. 2 Transient temperature response of lumped

    capacitance solids for different time constants

    Source: Incropera et al. (2007)

    1/e

    t

    Vc

    hAs

    i

    exp

    s

    i

    hA

    Vc

    texp

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    10

    Electrical analogy can be used if we define a

    thermal time constant

    )4(1

    tt

    st

    CRVchA

    Analogous to voltage decay,Ewhen charged

    capacitor,Cdischarges through a resistor,R in a

    RCcircuit (See figure on next slide)

    (3)Recall

    tVc

    hA

    TT

    TT s

    ii

    exp

    %8.361

    At

    e

    t

    i

    t

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    11

    Equivalent thermal circuit for a lumpedcapacitance solid

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    12

    0

    RC

    E

    dt

    dE

    ForRC electric circuit,

    Solution with initial conditionE(0) =E0isRCteEE /

    0

    For transient conduction (lumped capacitancemodel), total energy transferQin J occurring up

    to some time tcan be calculated by

    ti

    tt

    sconv

    tVc

    dthAdtQQ

    /exp1

    00

    ttCRt

    ie/

    analogous to

    s

    t hA

    Vc

    N.B.

    f f

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    13

    QE

    EQ

    EEEE

    st

    st

    stoutgin

    or00

    Alternatively, use conservation of energy over finite

    time interval, t= t- 0 = t

    tistti

    iist

    tVcEQ

    tVc

    VcTTVcE

    /exp1Hence,

    /exp1

    For quenching,Q

    is positive (Eout

    )

    For heating, Q is negative. (Ein

    )

    tt

    ie /

    Whi h h l b l b

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    14

    Which thermal system below can bemodelled as a lumped capacitance system?

    Source: engel, Y.A. and Ghajar, A.J., Heat and Mass Transfer:

    Fundamentals and Ap pl ications, 4th Ed. (SI Units), McGraw-Hill, 2011.

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    15

    Validity of Lumped Capacitance Method

    Assume steady-state conditions of Fig. 3 to developthe conditions under which the lumped capacitance

    method may be used.

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    16

    Fig. 3 Effect of Biot number on steady-state temperature

    distribution in a plane wall with surface convection

    Source: Incropera et al. (2007)

    convQ

    condQ TThATTL

    kAsss 2,2,1,

    Bi

    /1

    /

    2,

    2,1,

    khL

    R

    R

    hA

    kAL

    TT

    TT

    conv

    cond

    s

    ss

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    17

    Dimensionless numberBiot(pronounced as Bee-oh)

    numbercan be interpreted as

    conv

    cond

    R

    R

    hA

    kAL

    k

    hL

    /1/

    Bi

    Note that kis the thermal conductivity of the solid, not thefluid as in Nusselt number,

    Nu hL/kto be introduced in convection.Bi

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    18

    Fig. 4 The Biot number can be viewed as the ratio of

    convection (not convection resistance) at the

    surface to conduction (not conduction resistance)

    within the body

    T

    L

    Ak

    ThA

    k

    hL

    or

    R

    R

    hA

    kAL

    k

    hL

    conv

    cond

    Bi

    /1

    /Bi

    Illustration from engel and Ghajar (2011)

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    19

    Born 21 April 1774, Paris

    Died 3 February 1862, Paris

    Nationality

    French

    physicist, astronomer, and

    mathematician.

    Fields

    Professor of Mathematics at

    Beauvais (1797) and

    Professor of Physics at

    Collge de France, Paris

    (1800)

    Doctoral student William Ritchie

    Known for Biot-Savart law

    Influences Louis Pasteur

    Jean-Baptiste Biot

    Fig 5 Transient temperature distributions for different Biot

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    Fig. 5 Transient temperature distributions for different Biot

    numbers in a plane wall cooled by convection

    Source: Incropera et al. (2007)

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    21

    For arbitrarily-shaped bodies, characteristic

    length is defined as

    s

    cA

    VL

    ?lengthaxialof

    cylindersizefiniteandsideofcubeaforisWhat

    spherefor3/

    cylinderlongfor2/

    wallplanefor2/

    L

    LL

    rL

    rL

    LL

    c

    c

    c

    c

    Show that

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    22

    )5(FoBiexp

    TTTT

    ii

    c

    kydiffusivitthermal

    LtmberFourier nu

    L

    t

    k

    hL

    Vc

    thA

    c

    c

    cs

    ,and

    timeessdimensionlisFo,where

    FoBi

    2

    2

    Dimensionless temperature solution of Equation

    (3) can be re-written as

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    23

    Example 1: Transient Response of a Thermocouple

    Thermocouple used to measure temperature of a gas

    stream flowing in a duct

    Approximate junction as a sphere (D= 1 mm).

    Actual thermocouples come in standard wire sizes denoted

    as American Wire Gage (a.w.g.), e.g.

    a.w.g. 18 denotes 1.024 mm diameter wire

    a.w.g. 24 denotes 0.5106 mm diameter wire

    a.w.g. 30 denotes 0.1270 mm diameter wire

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    24

    Thermocouple in this example is Type Kmade of

    chromel and alumel wires

    c= 0.4 kJ/kgK, k= 30 W/ mK, = 8600 kg/m3

    Convection coefficient, h = 280 W/m2K

    chromelalumel

    Gas

    stream

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    25

    Find:

    (a) time required for thermocouple to reach 98% of

    the applied temperature difference, i.e.

    TTTtTi

    100

    2)(

    (b) time constant or response time of thermocouple

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    26

    Solution:

    Must check Bito see whether we can use lumped

    capacitance approach.

    m1067.1

    3100.5

    34

    3

    4

    4-

    3-

    2

    3

    r

    r

    r

    A

    VL

    s

    c

    1.01056.130 1067.1280Bi3-

    -4

    k

    hL c

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    27

    s03.8

    2

    100ln

    280

    104.01067.18600

    lnln

    34

    ici

    sh

    cLhAVct

    (a) Time required to reach 98% of applied

    temperature difference is given by

    (b) Time constant is

    s05.2

    280

    104.01067.18600 34

    h

    cL

    hA

    Vcc

    s

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    28

    Magnitude of time constant indicates how sensitive

    the thermocouple is to a change in temperature.

    A smaller bead diameter implies a more sensitive

    thermocouple.

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    29

    Example 2: Annealing of Steel Balls

    Carbon steel balls ( = 7833 kg/m3, k= 54 W/mK,c =

    465 J/kgK, and = 1.474 x 10-6 m2/s) 8 mm indiameter are annealed by heating them first to 900C in

    a furnace and then allowing them to cool slowly to

    100C in ambient air at 35C.

    a) If the average heat transfer coefficient is 75 W/m2K,determine how long the annealing process will take.

    b) If 2500 balls are to be annealed per hour, determine

    the total rate of heat transfer from the balls to the

    ambient air.

    Assumptions:

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    min2.7s163ln

    0013.0

    validisanalysisecapacitanclumped

    1.00018.0Bi

    TT

    TT

    hA

    Vct

    A

    VL

    k

    hL

    i

    s

    s

    c

    c

    kW543

    J/h1,952,500

    J/ball781balls/h2500

    ballperJ781

    QnQ

    TTmcEQ

    ball

    ifst

    Assumptions:

    (1) Constant properties (2) Constant and uniform ha)

    b)

    Source: engel and Ghajar (2011)

    Example 3: Freezing of Biological Tissue

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    31

    Example 3: Freezing of Biological Tissue

    A 1-cm cube of biological tissue is to be frozen in a

    freezer at 80C. The properties of the tissue has thesame properties as liquid water at 25C. The convective

    heat transfer coefficient is 10 W/m2K, and the tissue is

    initially at 25C.

    Determine the time it takes to freeze the tissuecompletely.

    The freezing temperature is taken as 0C. The properties

    of liquid water at 25C may be taken as: Thermal

    conductivity of 0.6 W/mK, density of 997 kg/m3

    , andspecific heat of 4.18 kJ/kgK.

    Schematic:

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    validisModeleCapacitancLumped

    1.0028.06

    Bi

    k

    hak

    hLc

    ANALYSIS:

    min3.15s189ln

    i

    shA

    Vct

    66 2

    3 a

    a

    a

    A

    VL

    s

    c

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    General Lumped Capacitance Analysis

    Transient conduction commonly initiated by

    convection heat transfer - simple lumped

    capacitance analysis.

    In general, thermal conditions in solid may besimultaneously influenced by convection, radiation,

    surface heat fluxand internal heat generation as

    shown in Fig. 6.

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    Fig. 6 Control surface for general lumped

    capacitance analysis

    sq

    radq

    convq

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    Applying conservation of energy at any instant t:

    )7(),(44, dtdTVcATTTThEAq rcssurghss

    Eq. (7) - non- linear, first-order, non-

    homogeneous ODE with no exact solution.

    )6(),(,dt

    dTVcAqqEAq rcsradconvghss

    Simplified cases:

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    36

    Simplified cases:

    Case 1: Radiation exchange only

    dtdT

    VcTTA surrs

    44

    ,

    T

    T

    t

    rs

    i surTT

    dTdt

    Vc

    A44

    0

    ,

    (8)

    Time required to reach temperature T

    isur

    isur

    sur

    sur

    rs TT

    TT

    TT

    TT

    TA

    Vct

    sur

    lnln4 3,

    sur

    i

    sur T

    T

    T

    T 11

    tantan2(9)

    Cannot obtain Tin terms oftexplicitly.

    For T = 0 i e radiation to deep space

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    37

    ForTsur

    0 i.e. radiation to deep space,

    (10)11

    3 33,

    iTTA

    Vct

    rs

    Case 2: Convection, surface heat flux and heat

    generation without radiation where h is assumedto be independent of time.

    Exact solution to the linear, first-order non-

    homogeneous differential equation of the form

    TT

    VcEAqbVchAawhere

    badt

    d

    ghsscs

    and

    ,/

    0

    ,,

    tiontransformagintroducinbyityinhomogeneEliminate

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    38

    )exp()/(

    )/(

    ,forngSubstituti

    ).exp(

    ),(to0fromgintegratinandvariablesSeparating

    0

    ngSubstituti

    tiontransformagintroducinbyityinhomogeneEliminate

    '

    '

    '

    ''

    ''

    '

    atabTT

    abTT

    at

    tot

    adt

    d

    a

    b

    i

    i

    i

    Hence

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    39

    Hence,

    )11(exp1/

    exp at

    TT

    abat

    TT

    TT

    ii

    When b = 0, Eq. (11) reduces to Eq. (3) introduced

    previously and yields T = Tiat t= 0.

    )3(exp

    tVc

    hA

    TT

    TT s

    i

    ./becomesEq.(11),As abTTt See Example 5.2 of Incropera et al. (2007)

    Some Review Questions

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    1. For which solid is the lumped capacitance analysis more

    likely to be applicable: an actual apple or a golden apple of

    the same size? Why?

    2. For what kind of bodies made of the same material is the

    lumped capacitance analysis more likely to be applicable:

    slender ones or well-rounded ones of the same volume?

    3. What is the significance of the thermal time constant?

    4. To what electrical circuit is the lumped capacitance systemanalogous?

    5. Why is it necessary to employ the concept ofcharacteristic

    length in lumped capacitance analysis?

    6. What are the physical significances of the Biot and Fouriernumbers?

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