Thermodynamics of internal combustion Engine

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    Thermodynamic Design of Engine

    P M V Subbarao

    Professor

    Mechanical Engineering Department

    Design for Performance..

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    Mean Effective Pressure

    The constant pressure that would have to exist to do the

    same work over Vd as is done by the actual cycle.

    A better measure of engine work than torque

    Depends more on engine design than engine size

    At maximum torque:

    Naturally aspirated: 850 to 1050 kPa

    Turbocharged: 1250 to 1700 kPa These are about 10% lower at maximum power

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    SI Engine Cycle vs Thermodynamic Otto Cycle

    A

    IR

    Intake

    Stroke

    FUEL

    Ignition

    Power

    Stroke

    Fuel/Air

    Mixture

    Compression

    Stroke

    Combustion

    Products

    Exhaust

    Stroke

    TC

    Qin QoutAir

    Compression

    Process

    Const volume

    heat addition

    Process

    Expansion

    Process

    Actual

    Cycle

    OttoCycle BC

    Const volume

    heat rejection

    Process

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    Early CI Engine Cycle and the Thermodynamic Diesel Cycle

    A

    IR

    Intake

    Stroke

    Fuel injected

    at TC

    Power

    Stroke

    Exhaust

    Stroke

    Air

    Compression

    Stroke

    Combustion

    Products

    Air

    Compression

    Process

    Expansion

    Process

    Actual

    Cycle

    DieselCycle BC

    Qout

    C

    onst volume

    heat rejection

    Process

    Qin

    Const pressure

    heat addition

    Process

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    Transient I.C. Engine Processes : Control Mass

    )()()()(

    tWtQdt

    mud

    dt

    mudCMCM

    CM

    fuelair

    irrCM Wdt

    tdV

    tptW

    )(

    )()(

    atmcylCM TtTtUAtQ

    )()()(

    Parameters that require Process Rate model

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    Actual SI Engine cycle

    Ignition

    Total Time Available ~ 10 msec

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    Early CI Engine Cycle

    A

    I

    R

    Combustion

    Products

    Fuel injected

    at TC

    Intake

    Stroke

    Air

    Compression

    Stroke

    Power

    Stroke

    Exhaust

    Stroke

    Actual

    Cycle

    In early CI engines the fuel was injected when the piston reached TC and thuscombustion lasted well into the expansion stroke.

    Fuel injection starts

    Early CI engine

    The combustion process in the early CI engines is best

    approximated by a constant pressure heat addition

    processDiesel Cycle

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    Modern CI Engine Cycle

    Combustion

    Products

    Fuel injected

    at 15o bTC

    Intake

    Stroke

    A

    I

    R

    Air

    Compression

    Stroke

    Power

    Stroke

    Exhaust

    Stroke

    Actual

    Cycle

    In modern engines the fuel is injected before TC (about 15o

    Fuel injection starts

    Modern CI engine

    The combustion process in the modern CI engines is best approximated

    by a combination of constant volume and constant pressureDual Cycle

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    Thermodynamic Design : A tradition of Post Carnot

    Research

    Major portion of motive power generation occurs in any Reciprocating IC

    engine in a control mass (closed system).

    The thermal operation of any IC engine is a transient cyclic process.

    Even at constant load and speed, the value of thermodynamic parameters atany location vary with time.

    Each event may get repeated again and again.

    So, an IC engine operation is a transient process which gets completed in aknown or required Cycle time.

    Higher the speed of the engine, lower will be the Cycle time.

    Modeling of IC engine process can be carried out in many ways.

    Multidimensional, Transient Flow and heat transfer Model.

    Thermodynamic Transient Model USUF.

    Fuel-air Thermodynamic Model.

    Air standard Thermodynamic Model.

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    Irreversible I.C. Engine Cycle

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    First Law Analysis: Transient Compression of

    Control Mass

    Compression Process

    Fuel/Air

    Mixture Air

    SI Engine CI Engine

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    Ideal Compression Process

    )()()()( tWtQdt

    muddt

    mud CMCMCM

    fuelair

    dt

    tdVptptW ccCM

    )()()(

    atmcylCMTtTtUAtQ

    )()()(

    Parameters that require Process Rate model

    Reversible displacement work:

    Instantaneous Rate of heat transfer:

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    Actual Compression Process : Control mass :

    Variable Property Single Fluid , heat transfer , frictional losses

    )()()()(

    tWtQdt

    mud

    dt

    mudCMCM

    CM

    fuelair

    )()(

    )(

    tWtQdt

    mud

    CMCMCM

    air

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    Isentropic Compression Process

    For a infinitesimal compression process:

    pdVdUTdS

    dVV

    mRTmRdTpdVdTmcVdpdU v

    110

    VdV

    TdTdV

    VTdT

    1

    11

    1

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    kgKkJT

    CT

    CT

    CCcp /100010001000

    3

    3

    2

    210

    Rc

    c

    p

    p

    V

    dVT

    T

    dT)(1

    For infinitesimal compression from initial state.

    Variable Properties of Working fluid

    11 TT dVVdTTTV

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    1V

    11 d

    dVV

    i

    i

    d

    dVV

    12 VrV c

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    Friction Force

    pSf

    Friction force is directly proportional to piston velocity

    1

    sin

    cossin

    60 22

    R

    LNSp

    1sin

    cossin60 22

    R

    LNf

    where is a coefficient of friction that takes into

    account the global frictional losses

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    The extra instantaneous power during Compression

    2

    221

    sin

    cossin

    60

    R

    LNSfP p

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    1V

    12 VrV c

    iV

    ii dVV

    Frictional Adiabatic Compression

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    VdV

    TT

    dT

    comp

    fri

    )(11

    ,

    For Irreversible Adiabatic Compression

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    p

    dp

    Tn

    Tn

    T

    dT

    comp

    irr

    )(

    1)(1

    ,

    For Irreversible Polytropic Compression

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    For another infinitesimal compression fromp+idp:

    idpp

    dp

    dTTn

    dTTn

    dTT

    dTi

    j

    j

    i

    jj

    comp

    i

    j

    j

    i

    1

    1

    1

    11

    ,

    1

    1

    1

    )(

    1)(1

    Evaluation of Polytropic efficiency, hcomp,.

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    Actual Compression Process : Control mass :

    Variable Property Single Fluid , heat transfer , frictional losses

    )()()()(

    tWtQdt

    mud

    dt

    mudCMCM

    CM

    fuelair

    )()(

    )(

    tWtQdt

    mud

    CMCMCM

    air

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    Actual Compression Process : Control mass :

    Variable Property Single Fluid , heat transfer , frictional losses

    )()()( tWtQdt

    Tmcd CMCMCM

    airv

    CI Engine

    Compressions:

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    dt

    tdvp

    dt

    Tcd

    CM

    airv )(

    dt

    dv

    v

    RT

    dt

    dTR 11

    Ideal Gas Model

    dt

    dv

    v

    T

    dt

    dT

    1

    1

    v

    dv

    T

    dT

    1

    1

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    kgKkJT

    CT

    CT

    CCcp

    /100010001000

    3

    3

    2

    210

    )(

    )(

    )( RTc

    Tc

    Tp

    p

    vdvT

    TdT )(1

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    Properties of Gases

    kgKkJ

    T

    C

    T

    C

    T

    CCcp /100010001000

    3

    3

    2

    210

    Gas C

    0C

    1C

    2C

    3

    Air 1.05 -0.365 0.85 -0.39Methane 1.2 3.25 0.75 -0.71

    CO2 0.45 1.67 -1.27 0.39

    Steam 1.79 0.107 0.586 -0.20

    O2 0.88 -0.0001 0.54 -0.33

    N2 1.11 -0.48 0.96 -0.42

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    Variable Properties of Air

    0.5

    0.7

    0.9

    1.1

    1.3

    1.5

    0 200 400 600 800 1000 1200 1400

    Temperature, K

    g

    cp

    cv

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    Properties of Fuels

    kgkJT

    CTC

    TC

    TCCC fp /100010001000 2

    4

    3

    3

    2

    210,

    Fuel C0 C1 C2 C3 C4

    Methane -0.29149 26.327 -10.610 1.5656 0.16573

    Propane -1.4867 74.339 -39.065 8.0543 0.01219

    Isooctane -0.55313 181.62 -97.787 20.402 -0.03095

    Gasoline -24.078 256.63 -201.68 64.750 0.5808

    Diesel -9.1063 246.97 -143.74 32.329 0.0518

    I t i C i V i bl P t M d l

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    Isentropic Compression : Variable Property Model

    s

    T

    11 dvv

    1v

    2

    1

    1

    i

    idvv

    j

    i

    idvv1

    1

    1

    11

    n

    iidvv

    2v

    For a small compression ratio: )(1

    11

    T

    i

    i

    i

    i

    v

    v

    T

    T

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    I t i C i V i bl P t M d l

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    Isentropic Compression : Variable Property Model

    s

    T

    11 dvv

    1v

    2

    1

    1

    i

    idvv

    j

    i

    idvv1

    1

    1

    11

    n

    iidvv

    2v

    For a small compression ratio:

    )(1

    1

    1

    1

    T

    i

    i

    i

    i

    i

    v

    v

    T

    T

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    Explicit Method:

    )(1111

    iT

    ivii rTT

    )(1

    1

    1

    1

    1

    iT

    i

    i

    i

    i

    i

    v

    v

    T

    T

    )(11)(1

    1

    )(1

    11

    iii T

    iv

    T

    ivi

    T

    ivii rrTrTT

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    Pressure Profile During Compression

    Ideal Gas Model:

    V

    mRTp

    )(1111

    iT

    ivii rTT

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    Initial Conditions

    Engine Respirator S stem

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    Engine Respiratory System

    Pexh,cyl

    Exhaust Valve : Operation Schedule

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    Exhaust Valve : Operation Schedule

    Pcyl

    Patm

    I l t V l O ti S h d l

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    Inlet Valve : Operation Schedule

    Pcyl

    Patm

    C li d P Di

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    Cylinder Pressure Diagram

    q

    Aexhaust Aintake

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    Work Required for Compression

    dVV

    mRTdVpW

    TDC

    BDC

    TDC

    BDC

    TDC

    BDCVdVTmRdVpWW ncompressio

    TDC

    IVCV

    dVTmRW ncompressio

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    Global Isentropic Compression Process

    The overall isentropic process between states 1 & 2:

    2

    1

    12 pdvmUU 2

    1

    12 pdvUU

    N

    i

    T

    v

    i

    rTT1

    )(1

    12

    1

    N

    i

    iT

    vrTT 11)(1

    12

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    Basics of Combustion

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    23 Complete combustion at constant volume

    0

    )()()( tWtQdt

    mud CMCMCM

    air

    )(tQdt

    dum

    CM

    CM

    air

    ..)( VCtmdt

    dum fuel

    CM

    air

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    23 Complete combustion at constant volume

    inQUU 23

    ..2

    0

    2

    0

    3

    0

    VCmdTmcQdTmcdTmc fuel

    T

    T

    vin

    T

    T

    v

    T

    T

    v

    ..2

    0

    3

    0

    VCAFdTcmdTmc

    T

    T

    v

    T

    T

    v

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    23 Complete & Finite Duration combustion

    )()(

    )(

    tWtQdt

    mudCMCM

    CM

    air

    dt

    tdVtpVCtm

    dt

    tTdcm combfuel

    CM

    v

    ..)(

    )(,

    dt

    dVpVCm

    dt

    Tdcm combfuel

    CM

    v

    ..)(

    )(,

    dt

    dV

    V

    RTVCm

    dt

    Tdcm combfuel

    CM

    v

    ..)(

    )(,

    Fi it H t R l

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    Finite Heat Release

    A typical heat release curve consists of an initial spark ignition phase,

    followed by a rapid burning phase and ends with burning completion phase

    The curve asymptotically approaches 1 so the end of combustion is defined

    by an arbitrary limit, such as 90% or 99% complete combustion where

    xb = 0.90 or 0.99 corresponding values for efficiency factora are 2.3 and 4.6

    The rate of heat release as a function of crank angle is:

    1

    1

    n

    d

    sb

    d

    inb

    in xna

    Q

    d

    dxQ

    d

    dQ

    bindxQdQ

    .99

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    dt

    dV

    V

    RTVCm

    dt

    Tdcm combfuel

    CM

    v

    ..)(

    )(,

    dt

    dV

    V

    RT

    d

    dQ

    dt

    Tdcm

    CM

    v

    )(

    Ideal gas model: mRTpV

    d

    dQ

    Vd

    dV

    V

    p

    d

    dp 1

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    3 4 Isentropic Expansion

    AIR

    )(tw

    dt

    duCM

    CM

    air

    Isentropic Expansion : Variable Property Model

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    Isentropic Expansion : Variable Property Model

    s

    T

    1

    1

    3

    n

    i

    idvv

    4v

    j

    i ij

    dvv1

    2

    1

    3

    i

    idvv

    13

    dvv

    3v

    For a small compression ratio:

    )(1

    1

    1

    1

    T

    i

    i

    i

    i

    i

    v

    v

    T

    T

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    Explicit Method:

    )(1111

    iT

    ivii rTT

    )(1

    1

    1

    1

    1

    iT

    i

    i

    i

    i

    i

    v

    v

    T

    T

    )(11)(1

    1

    )(1

    11

    iii T

    iv

    T

    ivi

    T

    ivii rrTrTT

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    Pressure Profile During Expansion

    Ideal Gas Model:

    V

    mRTp

    )(1111

    iT

    ivii rTT

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    Work Delivered during Expansion

    dV

    VmRTdVpW

    BDC

    TDC

    BDC

    TDC

    BDC

    TDCVdVTmRdVpWW ansion

    exp

    TDC

    IVCV

    dVTmRW ansion

    exp

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    Global Isentropic Expansion Process

    The overall isentropic process between states 3 & 4:

    4

    3

    12 pdvmUU 4

    3

    12 pdvUU

    N

    i

    T

    v

    i

    rTT1

    )(1

    43

    1

    N

    i

    iT

    vrTT 11)(1

    43

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    Constant Volume Heat Removal

    1

    1

    4

    4

    T

    P

    T

    P

    AIR

    Qout

    BC

    )()()(

    tWtQdt

    mudCMCM

    CM

    air

    0

    )(tQdt

    dum

    CM

    CM

    air

    TUAdt

    dum

    CM

    air

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    41 Complete Cooling at constant volume

    outQUU 41

    out

    T

    T

    vout

    T

    T

    v

    T

    T

    v QdTmcQdTmcdTmc 1

    0

    1

    0

    4

    0

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    41 Complete & Finite Duration Cooling

    )()(

    )(

    tWtQdt

    mudCMCM

    CM

    air

    dt

    tdVtptTtUA

    dt

    tTdcm

    CM

    v

    )(

    dt

    dVpTTUA

    dt

    Tdcm amb

    CM

    v

    )(

    dt

    dV

    V

    RTTTUA

    dt

    Tdcm amb

    CM

    v

    )(

    Surface Area for Cooling

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    Surface Area for Cooling

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    Engine Heat Losses

    For many engines, the heat losses can be subdivided:

    ambientoilcoolantloss QQQQ

    General range of various heat losses are:

    Type of loss Range Remarks

    Cooling 10 30 %

    5 15%

    Diesel engines on

    higher side

    Oil At low load higherlosses

    Ambient 2 10%

    Engine Cooling System

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    Measurement of Engine Heat Transfer

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    Measurement of Engine Heat Transfer

    S I Engine Temperatures

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    S I Engine Temperatures

    Three of the hottest points are

    around the spark plug,

    the exhaust valve and port, and

    the face of the piston.

    Highest gas temperatures during

    combustion occur around the spark

    plug. This creates a critical heat transfer

    problem area.

    The exhaust valve and port operate hot

    because they are located in pseudo-

    steady flow of hot exhaust gases. The piston face is difficult to cool

    because its is separated form the water

    jacket or finned surface.

    Computed Temperature of A Piston

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    Computed Temperature of A Piston

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    Heat Transfer in Combustion Chambers

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    cg

    coolantgas

    hk

    x

    h

    TT

    A

    Qq

    11

    Gas to Surface Heat Transfer

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    Heat transfer to walls is cyclic.

    Gas temperature Tg in the combustion chamber varies greatly over and

    engine cycle.

    Coolant temperature is fairly constant.

    Heat transfer from gas to walls occurs due to convection & radiation.

    Convection Heat transfer:

    Radiation heat transfer between cylinder gas and combustion chamber

    walls is

    wallgasgcconvconv TThA

    Qq

    w

    w

    g

    g

    wallgas

    wallgasgrrad

    rad

    F

    TTTTh

    A

    Qq

    111

    21

    44

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    The Cyclic Integral

    dVpWcycle

    dVpWcycle

    kNWP cycleengine

    60

    k=1:for two-strokecycle

    k=2:for four-stroke

    cycle