L20 AE0637 Combustors Part1 2013

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    AE0637AdvancedAircraftPropulsion

    (Part1)

    RandyChue(Assoc.Prof.)

    .

    Phone:67906399

    . .

    1

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    TheCombustor

    Thescramjetcombustorhastwobasicfunctions:

    .

    2. Tocombustthemixture

    Keydesignissues:

    Mixinglengthandcombustionlengthgrowwithincreasing

    flowMach

    number

    or

    velocity

    Thecombustorisahighheatingandhighdragregionandmus eass or asposs e

    Fuelinjection,vaporization,mixing

    2

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    CombustionStoichiometry

    Wehaveseenduringourlecturesonengineperformance

    . . .

    energyreleasedfromcombustionoccurswhenthefuelis

    mixedwith

    just

    enough

    air

    so

    that

    all

    of

    the

    hydrogen

    atoms

    formwatervaporH2O,andallofthecarbonatomsform

    carbondioxideCO2

    Thiscondition

    of

    complete

    combustion

    is

    called

    stoichiometric

    reaction,andforageneralhydrocarbonfuel(CxHy),theideal

    Fromp.8,EnginePerformanceMeasures(Part1)

    22222 N421

    OH2

    CON21

    O4

    HC

    xxxyx

    Oxidizer Nitrogen

    3

    Representativeair Assumedinert

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    CombustionStoichiometry(Contd)

    Thestoichiometricfuel/airratio(massbased)wasderivedto

    airfuel/kgkg,

    4103

    336

    yx

    yxfst

    FromEnginePerformance

    Measures

    slides,

    p.

    9

    Involumetricormolarbase,thestoichiometricfuel/airratio

    productsN2179O

    4HC 22

    yxyx

    moles

    21

    791

    4

    y

    xmole1

    airfuel/molsmols,

    4100

    84

    791

    1

    yxyx

    fst

    4

    214

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    CombustionStoichiometry(Contd)

    Anotherparameteroftenusedtodescribecombustion

    , ,

    definedastheactualfuel/airdividedbythestoichiometry

    fuel/airratio:

    stf

    f

    mixturetricstoichiome,1mixturelean-fuel,1

    Thechemical

    reaction

    for

    a

    eneraloff

    stoichiometric mixture

    mixturerich-fuel,1

    offuelandaircanthenbeexpressedsimplyas:

    79

    5

    pro uc s

    21422

    xyx

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    TheCompleteCombustionAssumption

    Notethatthecompletecombustionassumption doesnotim l that inactual ractice astoichiometricmixtureoffuelandairwillonlyyieldH2OandCO2ascombustionproducts

    Inreality,

    even

    when

    we

    have

    astoichiometric

    fuel

    air

    m xture,wemay ave:

    Somedissociationofthecombustionproducts(H2OandCO2)

    Incom lete combustion insufficient time to burn the reactants

    withinthe

    combustion

    when

    the

    flow

    speed

    is

    high

    Somelevelofnitrogenoxidation(N2isnotinert)

    eac ua gases eav ng ecom us ormay nc u e:

    Unreactedreactants(fuel&air)

    Dissociated

    roducts

    Incompletelyoxidizedfuelmolecules

    Oxidizednitrogen:nitricoxide(NO),nitrousoxide(N2O),andnitrogen

    6

    2 . x

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    OffStoichiometricCombustion

    Foroffstoichiometricfuel/airmixtures,asaroughgeneral

    ,

    ratios:

    22.0

    Foroffstoichiometricmixtures,therewillbeincomplete

    combustion,sothattheproductsspecieslistcanbefarmore

    thanthose

    of

    H2O

    and

    CO2.

    The

    generalized

    chemical

    reaction

    canberepresentedby:

    OHCOCON

    21

    79O

    4

    HC 2OHCO2CO22 22

    nnny

    xyx

    whereetc.includesalltheotherpossiblegasspeciesthat

    etc.ONNOOO 2ON2NOO2O 222 nnnn

    7

    mayexistsfromthecombinationsofO,H,C,andNatoms

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    OffStoichiometricCombustion(Contd)

    Thiscanalsoberepresentedby:NS

    where:

    i

    iiyx nx1

    22 N21

    O4

    HC

    NSisthetotalnumberofspeciesthatmayappearontheproductsideofthechemicalequation

    Aiis

    the

    chemical

    formula

    of

    the

    ith

    species

    niisthemolenumberfortheithspecies

    Thefullproductspecieslistandtheirmolenumberswillbe.

    ,

    mayassumethatthechemicalreactionswouldreachequilibrium(althoughnotnecessarilycompletereaction)

    8

    Achemicalequilibriumanalysiswouldcalculatesuchareaction

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    FuelAirMixing

    Chemicalreactionsbetweenthefuelandtheairtakeplaceat

    Fuelandairmoleculesmustcomeincontactwitheachother

    (molecularcollisions)

    Theyaremixedtonearstoichiometric proportionsforcombustionto

    takeplace

    Mixingcan

    be

    considered

    to

    occur

    at

    two

    levels

    Macromixin stirrin event. Fuel and air are forcibl stirred so

    thattheyarepresentamongeachother

    Micromixing molecular

    diffusion.

    The

    molecules

    of

    the

    fuel

    and

    the

    a rare use an eycome n ocon ac w eac o er

    9

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    FuelAirMixinginParallelStreams

    Considerthemixingoftwoparallelflowingstreams(airand

    m

    thickness

    Streamvelocities:u1(air)andu2 (fuel)(neglectboundarylayer)

    = =

    10

    Fuel

    (YA)2=0,

    (YF)2=

    1

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    FuelAirMixinginParallelStreams(Contd)

    Forsimplicity,weassume:

    Static ressureofbothstreamsaree ualandconstant

    Densityofbothstreamsareequalandconstant

    Only

    the

    velocities

    are

    different

    a oun ary ayersonsp erp a ean onou erwa sareneg ec e

    Ifthetwovelocitiesaredifferent,ashearlayerisgeneratedatthe interface between the two streams. Lateral trans orts at

    theinterface

    include

    Momentumistransportedlaterallyfromthefastertotheslower

    Vorticity

    Thermaland

    mechanical

    energy

    Mass(molecules)transport

    Itislikeaboundarylayer,butitisnotatthewallboundary.

    11

    ,

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    ZeroshearMixingLayer

    Onelimitingcaseiswhenthetwostreamshavethesame

    Thereisnoshear,butthereismoleculardiffusion

    gradientandisgivenbyFicksLaw:

    yCDj AFAA

    (kmolA/m3)

    Molardiffusivefluxofair2

    Concentrationgradient

    ,

    Moleculardiffusivity

    betweenfuelandair

    12Subscripts

    &

    symbols:

    Afor

    air,

    Ffor

    fuel

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    ZeroshearMixingLayer(Contd)

    Moleculardiffusionisverysimilartoviscousdiffusion

    FA

    TheSchmidtnumberistheratioofviscositycoefficientto

    DFA

    .

    0.1CS

    Forthezerosheardiffusionproblem,themixinglayer

    FA

    FA

    m

    xD

    8

    whereucistheaverageormeanconvectivevelocitydefined

    as:

    c

    13velocityconvectivemean,2

    21

    uc

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    ZeroshearMixingLayer(Contd)

    ThetotaldistanceLmrequiredforthemixinglayerboundaryto

    m

    b1+ b2)

    2b=

    c

    mFA

    u

    LDb 82

    FA

    cm

    DbuL

    16

    2

    L

    Thisisjustanapproximation,andtheactualmixinglengthmay

    betwice

    as

    lon

    TheresultsindicatethattheLmrequireddecreaseswithb2. If

    brepresentsthefuelinjectorheight,bshouldbeminimizedto

    14reduce

    the

    mixing

    length

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    ZeroshearMixingLayer(Contd)

    Onepossiblewaytoreducetheinjectorheightbisby

    , rapidmixingthatisrequiredinramjetsandscramjetengines

    15

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    LaminarShear/MixingLayer(Contd)

    Forlaminarshearmixinglayer,itdoesntdomuchbetterthan

    .

    approximately=1(i.e.,DFA=)

    Alllateral

    transport

    is

    by

    molecular

    diffusion

    (both

    viscosity

    and

    mass

    diffusivityareduetomoleculardiffusion)

    Thelaminarshearlayerthicknessisbasicallythesameasthe

    m x ng ayert c ness

    Theincreaseingrowthrateformisverysmall

    Inordertosignificantlyincreasethelateraltransportinthe

    s ear ayer, snecessary o ncrease eve oc y erenceusothattheshear/mixinglayerisnolongerlaminar

    17

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    TurbulentShear/MixingLayer

    Whenthe

    velocity

    difference

    uis

    sufficiently

    high,

    the

    laminarfloweventuallyundergoestransitiontoturbulentflow

    Whenthisoccurs,thestructureoftheshearlayerisdrastically

    changed Theshearlayerbecomesunstableandunsteady

    Largevorticesareperiodicallyformedbetweenthetwostreams

    e u ynam cp enomenon s escr e y e e v n

    Helmoholtz instability(flowinstabilityinshearlayers)

    18

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    TurbulentShear/MixingLayer(Contd)

    Thesequence

    of

    events

    that

    occurs

    following

    the

    formation

    of

    largevorticesis:

    Dashedcurves:mixant

    boundariesfor

    moleculardiffusion

    Fullymicromixedregion

    Shearstress

    causes

    the

    periodic

    formation

    of

    large

    vortices

    ,frombothstreams,andstretchesthemixantinterface

    Further

    stretching

    of

    the

    mixant

    interface

    increases

    the

    interfacialareaandenhancesmoleculardiffusion

    Moleculardiffusionoccursatthestretchedmixantinterface

    19

    an even ua yresu s n u ym crom xe s a e

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    TurbulentShear/MixingLayer(Contd)

    Turbulentshearcanincreasemixingdrastically

    However,italsoresultsinlosses

    Justasinwallboundarylayers,freeshearlayersleadto

    viscousdissipationofmechanicalenergytothermalenergy

    Entropyincreases

    Totalpressureloss

    Decreaseincycleefficiency

    20

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    TurbulentShearLayerMixing

    Wehaveseenthatturbulentshearlayermixingismuchmore

    TheratioofmixinglengthtothefuelinjectorheightLm/bis

    ordersof

    ma nitude

    smaller

    than

    those

    of

    zero

    shear

    and

    laminarshearlayers

    2b=

    m

    mixingshear-noorlaminar,)1000O(~b

    Lm

    21mixingshearturbulent,)100O()50O(~ b

    Lm

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    TurbulentShearLayerMixing(Contd)

    However,turbulentshearlayermixingisstillinadequatein

    , 2,optimalcombustioncannotbemetbyshearlayermixing

    Therefore,shear

    layer

    mixing,

    particularly

    turbulent

    shear

    mixing,isofgreatacademicinterestbutitisimpracticalinreal

    combustordesigns

    22

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    FurtherRemarksaboutShearLayerMixing

    Wehaveonlyconsideredtheeffectsofvelocitydifferent

    Thedifferenceindensitybetweenthetwostreams

    Temperaturedifference

    The

    Mach

    numbers

    (compressibility

    effects)

    Heatrelease(whenincombustion)

    Asawhole,thesefactorsarenotstrongenoughtochangethe

    Needsomethingstrongertoenhancemixing

    23

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    References

    Textbook:

    HypersonicAirbreathingPropulsion,W.H.Heiser&D.T.

    Pratt.

    Sections6.1.1,

    6.2.1,

    6.2.2,

    6.2.5.

    24