Turbomachinery (MEng 3202) Part II

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    Melesse Haile(Asst. Professor)

    Adama UniversityEthiopia

    Turbomachinery (MEng 3202)Part - II

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    Compressors are machines used to increase the pressure of a fluid.

    Note:- This chapter also includes the discussion of Chapter 7 and 8. That is, itincludes the design of rotor blades, guide vanes and spiral casings.

    Classification of work absorbing machines.

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    Classification of Compressors

    Positive displacement compressors increase the pressure of a gas or air byreducing the volume.

    Dynamic compressors increase the air velocity by the rotational motion of impelleror rotor, which is then converted to pressure at the outlet.

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    Classification of Dynamic Compressors1. By the type of flow,

    Radial flow

    Axial flow

    2. By the type of energy conversion, Volute casing Volute casing with guide vanes

    3. By the method of drive, Gear drive

    Belt drive

    Radial flow Axial flow

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    Radial (Centrifugal) Compressors

    Component parts

    1. Impeller2. Inducer3. Diffuser and Diffuser vanes4. Collector or Casing5. Inlet Guide Vane

    Class work

    1. Write the function of each component part.

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    A Typical Compressed air System Components and Network

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    Radial Compressors

    Principle of operation

    When the impeller is rotating at high speed (more than 20000 rpm), air is drawn inthrough the eye of the impeller. The absolute velocity of the inflow air is axial. Themagnitude and direction of relative velocity at inlet depends upon the velocity of theimpeller as well as the magnitude and direction of the entering absolute velocity. Theimpeller vanes at the eye are bent so as to provide shockless entry (inducer). The airthen flows radially through the impeller passages due to centrifugal force. The total

    mechanical energy driving the compressor is transmitted to the fluid stream in theimpeller where it is converted into kinetic energy of air. The diffuser then converts the

    kinetic energy of air into pressure.The air leaving the diffuser iscollected in a spiral passage fromwhich it is discharged from the

    compressor.

    The pressure and velocity variationacross the compressor is as shownin the figure.

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    Radial Compressors

    Shapes of Radial Compressor blades

    Velocity diagrams for a Radial Compressor blades

    inlet outlet

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    Radial Compressors

    Velocity diagrams for a Radial Blades

    at the inletFigure (a) represents the velocity trianglewhen the air enters the impeller in the axialdirection. In this case, C1 = Ca1. Figure (b)represents the velocity triangle at the inlet tothe impeller eye and air enters through theinlet guide vanes. Angle is made by C1 andCa1 and this angle is known as the angle ofprewhirl. The absolute velocity C1 has a whirlcomponent Cw1.

    at the outlet

    In ideal case, as shown in Figure (c), airleaves the impeller tip at an angle of 900.Hence, Cw2 = U2. But in actual case due to slipbetween the impeller and the fluid, Cw1 issomewhat less than U2 as shown in Figure(d).

    inlet

    outlet

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    Radial Compressors

    Slip Factor

    As shown in the figure, due to slip the actual fluid does not follow the blade shape.Slip () is, therefore, defined as,

    For radial vane impellers, a relation for slip is given by Stanitz,

    where, n is the number of vanes.

    Assume, y 0.9 for n value 19 to 21.

    2

    '

    2

    w

    w

    C

    C

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    Radial Compressors

    Energy Transfer (Pt)

    From Eulers equation, the energy transfer per unit mass flow rate is given by,

    considering velocity triangle (a)

    Considering velocity triangle (c), Cw2 = U2 and with slip the theoretical energy transferis given by,

    ct Wm

    P

    inlet outlet

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    Radial Compressors

    Energy Transfer (Pt)

    In a real fluid, some of the power supplied by the impeller is used in overcominglosses that have a breaking effect on the air carried by the vanes. These includewindage, disk friction, and casing friction losses. To take into account these losses, apower input factor () , which is the ratio of the actual to theoretical energy transfer, isintroduced. This factor typically takes values between 1.035 and 1.04. Thus the actual

    work done on the air becomes,

    From Mollier Chart, the stagnation or totaltemperature equivalent of work done on

    the air is given by,

    ( Refer:- Reference-1 page 68 - 75 )

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    Radial Compressors

    Energy Transfer (Pt)

    The compressor isentropic efficiency (c) is defined as,

    T03= T03ss

    Hence,

    And,

    Note:- The tip speed ratio (U2) is about 460 m/s.

    Class work

    1. Write your own observation and conclusion on the derived relation for .

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    Ad U i i M l H il (A P f )

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    Radial Compressors

    Effect of impeller blade shape on performance

    There are three types of blade shapes as shown in the figure.

    a) Backward-curved blades (2

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    Radial Compressors

    Effect of impeller blade shape on performance

    b) Backward-curved blades (2 = 900):-

    From this equation one can observe that, as theenergy or power transfer remains constant.

    c) Forward-curved blades (2 > 900):-

    As the mass flow rate increases energy or power transfer also increases.

    Ag

    Um

    g

    UPHence

    A

    mCwhere

    g

    CUUPand

    g

    CUPequationsEulerFrom

    t

    aa

    t

    wt

    22

    2

    2

    22222

    22

    cot,

    ,)cot(

    ,

    ,'

    tconsisg

    UP

    Ag

    Um

    g

    U

    PHence

    A

    mCwhere

    g

    CUUPand

    g

    CUPequationsEulerFrom

    t

    t

    aa

    t

    wt

    tan

    0cot

    cot

    ,

    ,)cot(

    ,

    ,'

    2

    2

    2

    22

    2

    2

    22222

    22

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    Ad U i it M l H il (A t P f )

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    Radial Compressors

    Effect of impeller blade shape on performance

    In the case of backward-curved blades or vanes, the maximum efficiency occurs in theregion of maximum power. If the flow rate increases beyond the design point, thepower starts to decrease. This keeps the motor to operate safely and thischaracteristics is called self-limiting characteristics. Whereas in the case of radialand forward-curved blades or vanes, as the flow rate increases the power also tend toincrease even beyond the design point. This is not only make the operation costly but

    also damage the motor. But, designers may sometimes prefer these two types ofshapes to get some performance advantage as compared to backward-curved blades.

    Compressibility effects

    If the relative velocity of a compressible fluid reachesthe speed of sound in the fluid, separation of flow

    causes excessive pressure losses and cyclic loading onthe impeller due to eddy or shock wave formation. It is,therefore, necessary to control the Mach number at acertain points in the flow to mitigate the problem. TheMach number at the impeller inlet must be less thanunity. This is possible by reducing the relative velocity at

    inlet by introducing a guide vane as shown in the figure.inlet

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    Radial Compressors

    Compressibility effects

    Actually, reducing the relative velocity at inlet causes the tangential velocity of theabsolute velocity to increase. This in turn decreases the work capacity of thecompressor.

    Mach number in the diffuserThe absolute velocity of the fluid becomes a maximum at the tip of the impeller.Assuming a perfect gas, the Mach number at the impeller exit M

    2

    can be written as:

    However, it has been found that as long as the radial velocity component (Cr2) issubsonic, Mach number greater than unity can be used at the impeller tip without loss

    of efficiency.High Mach number at the inlet causes high stagnation pressure. This leads to avariation of static pressure and is transmitted upstream in a radial direction throughthe vaneless space. The end result will be exerting a cyclic type of load on theimpeller. This in turn lead to early fatigue and failure on the impeller.

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    Radial Compressors

    Characteristics of a Radial Compressor

    The performance of compressible flow machines usually be described in terms of thegroups of variables derived in dimensional analysis ( Refer:- Rference-1 on Page 62).These variables are dependent on other variables such as the condition of pressureand temperature at the compressor inlet and physical properties of working fluid. Tostudy the performance of a compressor completely, it is necessary to plotagainst the mass flow parameter for a fixed speed intervals of .

    The figure below shows the theoretical characteristics of a Centrifugal Compressor.

    Consider a valve is placed in the delivery lineof a compressor running at constant speed.Suppose at the beginning the valve is fully

    closed. The pressure ratio then will havesome value as indicated by point A. Thispressure ratio is available from vanes movingthe air about in the impeller. The pressurehead so developed is called shutoff head.

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    Radial Compressors

    Characteristics of a Radial Compressor

    Now, suppose that the valve is opened andair flow begins. The diffuser contributes to thepressure rise. The pressure ratio increasesand the maximum pressure occurs at point B.But the compressor efficiency at thispressure ratio will be below the maximum

    efficiency. Point C indicates the furtherincrease in mass flow, but the pressure isdropped slightly from the maximum possiblevalue. This is the design mass flow ratepressure ratio as efficiency is maximum.

    Further increase in mass flow will decrease the pressure ratio until point D. Thispoint indicates that the pressure rise is zero. At this point all the power absorbed isused to overcome the internal friction and thus the compression efficiency is zero.However, the actual curve is different from this ideal curve shown in the figure dueto chocking, surging and stall.

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    Radial Compressors

    Characteristics of a Radial Compressor

    Choking:- When the velocity of fluid in a passage reaches the speed of sound atany cross-section, then the air ceases to flow and the process is called chocking.Choking may occur at the inlet, at the impeller or at the diffuser.

    Surging:- The phenomenon of a momentary increase in the delivery pressureresulting in unsteady, periodic and reversal flow through the compressor is called

    surging. Surging may lead to failure of the compressor parts.

    Stall:- The phenomenon of a reduction in mass flow rate through the blade passageat higher angle of incidence is known as stall. This phenomenon may lead tosurging.

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    Radial Compressors

    Energy transfer by the impeller to the fluid (air)

    A radial compressor is a dynamic type compressor and it works on the principle offorced vortex flow ( Refer:- Fluid mechanics ). When a certain mass of fluid is rotatedby an external torque, the rise in pressure head of liquid takes place. The rise inpressure head ( Hp ) at any point of the rotating liquid is proportional to the square oftangential velocity ( v) of the liquid at that point.

    g

    r

    g

    vHheadpressureThe p

    22)(

    222

    Thus at the outlet of the impeller where

    radius is more, the rise in pressure is moreand the liquid will be discharged at theoutlet with a high pressure head.

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    Radial Compressors

    Energy transfer by the impeller to the fluid (air)

    In case of radial (centrifugal) compressors, work is done by the impeller on thefluid (air). The expression for work done by the impeller on the air is obtainedby drawing velocity triangle at inlet and outlet of the impeller in a similar way asfor a centrifugal pump.

    Velocity diagram

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    Radial Compressors

    Energy transfer by the impeller to the fluid (air)

    As shown in the velocity diagram, the angle between vand u is called andthe angle between wand u is called . The difference between the absolutevelocity vand the relative velocity w is also illustrated.

    Velocity diagrams

    Inlet

    outlet

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    Radial Compressors

    Ideal Head Equation

    The equation which forms the basis of pump, compressor and blower design isbased on the following assumptions: The fluid leaves the impeller passages tangentially to the vane surfaces or

    there is a complete guidance of the fluid at the outlet and the fluid is

    assumed to be frictionless, non-turbulent, etc.

    The impeller passages are completely filled with actively flowing fluid at all

    times. The velocities of the fluid at similar points on all the flow lines are the same.

    The ideal total head developed by the impeller based on these assumptions iscalled Eulerhead and designated by HE and is given by,

    Note:-The deviation of actual conditions from these assumptions will be

    considered later.

    .

    .

    .,

    2

    1

    21

    velocityabsoluteinchangetoduediffusertheinheadpressuretheisH

    velocityrelativeinchangetodueimpellertheinheadpressuretheisH

    forcelcentrifugatodueimpellertheinheadpressuretheisHWhere

    HHHH

    d

    i

    i

    diiE

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    Radial Compressors

    The Pressure Head in the impeller due to centrifugal force (Hi1)

    Consider a closed container filled with fluid (air), as shown in the figure, isrotated at constant speed about its axis. The motion is transmitted to the fluidby its viscosity until the angular velocity of the fluid is the same as that of thecontainer.

    Rotating container filled with fluid

    To determine the pressure distribution

    within the fluid, consider a very small fluidelement having a width b, thickness dRandcircumferential length Rd rotating with anangular velocity . The centrifugal forceacting on the particle is,

    The pressure increment due to this forcebetween R and R+dR is,

    dRdRbdFHence

    dRRdbdmWhereRdmdF

    22

    2

    ,

    ,

    dRR

    Rdb

    dRdRb

    dA

    dFdp 2

    22

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    Radial Compressors

    The Pressure Head in the impeller due to centrifugal force (Hi1)

    Rotating container filled with fluid

    Integrating between the radii R1 and R2gives the total pressure,

    g

    uuHHH

    HHg

    ppbut

    g

    uu

    g

    ppHence

    uRandRR

    pp

    ipp

    pp

    2

    ,2

    ,

    ,2

    2

    1

    2

    2112

    1212

    2

    1

    2

    212

    2222

    1

    2

    22

    12

    y ( f )

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    Radial Compressors

    The Pressure Head in the impeller due to change in relative velocity (Hi2)

    Consider the passage through the impeller at radius rhaving a cross-section daas shown in the figure. Let the small element of area da moves a smalldistance dsin time dt. Hence,

    g

    ww

    g

    pH

    ww

    dwwdpp

    outletandinletbetweenequationthegIntegratin

    dww

    wdt

    dsbutdw

    dt

    dsdp

    dabyalldividingand

    dt

    dwdsdadpdadF

    i2

    2

    ),2()1(

    ,

    2

    2

    2

    1

    2

    2

    2

    2

    2

    2

    1

    2

    1

    y ( f )

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    Radial Compressors

    The Pressure Head in the diffuser due to change in absolute velocity (Hd)

    Inside the diffuser, the dynamic pressure or velocity head is converted intostatic pressure head. The velocity in the discharge pipeline is almost the sameas the velocity in the suction pipe.Consider a fluid element of area da moving through the diffuser vanes adistance ds in time dt as shown in the figure.

    g

    vv

    g

    p

    H

    vv

    dvvdpp

    outletandinletdiffuserbetweenequationthegIntegratin

    dvv

    vdt

    dsbutdw

    dt

    dsdp

    dabyalldividingand

    dt

    dv

    dsdadpdadF

    d 2

    2

    ),1()2(

    ,

    2

    1

    2

    2

    2

    2

    2

    1

    2

    1

    2

    1

    y ( f )

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    Radial Compressors

    The Ideal Total Head (HE)

    g

    vuH

    inletradialhavingimpellerforand

    g

    vuvuH

    vvandvvbut

    g

    vuvuH

    equationabovetheinequationstheseInserting

    vuvuw

    vuvuw

    impellertheofoutletandinletatdiagramvelocitytheFrom

    g

    vvwwuu

    g

    vv

    g

    ww

    g

    uuHHHH

    uE

    uuE

    uu

    E

    diiE

    22

    0

    1

    1122

    222111

    111222

    222

    2

    2

    2

    2

    2

    2

    11121

    21

    21

    2

    1

    2

    2

    2

    2

    2

    1

    2

    1

    2

    2

    2

    1

    2

    2

    2

    2

    2

    1

    2

    1

    2

    2

    21

    ),90(

    coscos,

    coscos

    ,

    cos2

    cos2

    ,

    2

    222

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    Radial Compressors

    The Ideal Power (P) and Torque (T)

    NminvRvRQ

    vRvRQ

    vuvuQ

    PT

    HPinvuvuQ

    kWinvuvuQ

    Wing

    vuvugQ

    gHmP

    uu

    uu

    uu

    uu

    uu

    uu

    E

    )(

    )(

    )(

    746)(

    1000

    )(

    )(

    1122

    1122

    1122

    1122

    1122

    1122

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    Radial Compressors

    Degree of Reaction ( )Degree of reaction is the ratio of the static pressure head rise in the impeller (H

    i1

    ) tothe total head rise (HE).

    2

    2

    2

    1

    2

    2

    2

    2

    2

    1

    2

    2

    2

    2

    2

    2

    12

    21

    11

    0

    22

    2

    1

    2

    2

    1

    ,

    ,

    ;90

    ,

    21

    ,

    1

    u

    uur

    r

    rr

    r

    u

    Ed

    E

    d

    E

    dE

    E

    i

    vvvand

    vvvvv

    trianglevelocityoutletFromvv

    vv

    vv

    inletradialFor

    vuvv

    HandHforngSubstituti

    H

    H

    H

    HH

    H

    H

    22

    2

    2

    2

    22

    2

    2

    22

    2

    2

    22

    2

    2

    tan1

    2

    1

    2

    tan1

    tan

    ,

    2

    1

    21,

    u

    v

    u

    vu

    vuv

    trianglevelocityoutlettheFrom

    u

    v

    vu

    vHence

    r

    r

    ru

    u

    u

    u

    Question:- What do you observe fromthis relation ?

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    Radial Compressors

    Degree of Reaction ( )

    From this relation one can observe that,a) For 2 = 90

    0, the degree of reaction = , as 2 = . This means that thepressure generated by the impeller and diffuser will be the same.

    b) For 2 having values between 00 and 900 , the degree of reaction is more than

    half. This means is that the pressure generated by the impeller is more than inthe diffuser.

    c) When the degree of reaction is one.

    22

    2

    tan1

    2

    1

    u

    vr

    2

    1

    .)(,1,

    0

    ,tan

    tan,

    tan1tan

    2

    222

    2

    2

    2

    22

    222

    22

    2

    22

    2

    zeroisHheadtotalidealtheforThus

    v

    uvu

    g

    uH

    ofvaluethengSubstituti

    vu

    g

    u

    g

    vuHThen

    u

    vor

    u

    v

    E

    r

    rE

    ruE

    rr

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    Radial Compressors

    Degree of Reaction ( )

    d) When = 0, there is no static pressure change in the impeller. The energy transferis entirely due to the change of absolute velocity in the diffuser. In other words,the impeller has equi-pressure blades or impulse blades. Machines having suchan impeller is known as an impulse machines. The blades of impulse impellersare forward curved and the blades of reaction impellers are backward curved asshown in the figure. In order to generate more pressure in the impeller, the angle

    2 should be nearly zero. For the same discharge reaction machines have largeroutlet impeller diameter or high rotational speed than impulse machines.

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    Radial Compressors

    Actual Head or Power developed by the impeller

    It has been discussed that the ideal head or power developed by the impeller isderived based on the listed assumptions. Some of these assumptions were if thefluid is frictionless, non-turbulent, etc. In this section the factors which causes thesedeviations will be discussed.

    Factors which causes deviation of actual machines from the ideal

    a) Circulatory flow:- If a closed container is filled with fluid and rotated about anaxis, the fluid tends to rotate in opposite direction relative to the container due toits inertia. It is apparent that the fluid in contact with the side A of the container isat a higher pressure than at B, as the container is exerting a pressure on the fluidon that side while it is being accelerated as shown in the figure.

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    Radial Compressors

    Actual Head or Power developed by the impeller

    Factors which causes deviation of the actual machines from the idealThis implies that the velocity at B is higher than A according to Bernoullisequation. The amount of this circulatory flow depends on the shape of thecontainer. It will be less if is long and narrow. In a rotating impeller two flows takeplace simultaneously; namely, the flow of fluid through the passage and thecirculatory flow as shown in the figure. The resultant effect for a given flow is to

    cause the fluid to leave the wheel at an angle less than the vane angle and toincrease the guide blade angle. This effect is illustrated in the velocity diagramwhere the dotted lines represent the ideal velocity diagrams.

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    Radial Compressors

    Actual Head or Power developed by the impeller

    Factors which causes deviation of the actual machines from the idealb) Effect of Finite Number of Blades:-Taking finite number of blades of impeller,

    the Ideal or Euler Head (HE) is changed as follows due to changes in velocitydiagram.

    Where, is the correction factor for finite number of blades. It is sometimes known as

    blade efficiency blade.

    Eu

    E

    Euu

    E

    Hg

    vuH

    inletradialhavingimpellerforand

    Hg

    vuvuH

    '

    22'

    0

    1

    '

    11

    '

    22'

    ),90(

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    Radial Compressors

    Actual Head or Power developed by the impeller

    Factors which causes deviation of the actual machines from the idealc) Shock loss:-The usual assumption made in designing such a machine is that

    the fluid enters the impeller vanes radially so that 1 = 900. As the fluid

    approaches the vane inlet, it comes in contact with the rotating impeller. Thistends to cause a mismatch between the blade angles and the inlet flowdirections specially at high flow rates. This causes the inlet vane angle to be

    larger as shown in the figure. The net effect is to reduce the head and hence thepower to be transferred to the fluid due to the presence of vu1.

    g

    vuH

    inletradialhavingimpellerforand

    g

    vuvuH

    uE

    uuE

    22

    01

    1122

    ),90(

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    Radial Compressors

    Actual Head or Power developed by the impeller

    Factors which causes deviation of the actual machines from the ideald) Fluid and Disc or Surface Friction:-This is due to the friction that exists within

    the fluid and between the fluid and the surfaces of the impeller and the diffuser.

    e) Turbulence:-The type of flow existing in a pump or a compressor or a blower isturbulent as the determined from the Reynold number. The effect of turbulence is

    also to reduce the machine performance.

    f) Leakage:- This is due to the loss of fluid during operation. The effect of thisleakage loss is to reduce the discharge capacity.

    The actual head is called the manometric head (Hm) is, therefore, given by:

    .

    sin

    22 radialisvelocityf lowinletifHg

    vu

    HH

    gcaandimpellertheinLossesheadEulerH

    Lu

    LE

    m

    Video-5Video-6Video-7

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    http://video/YouTube-%20Centrifugal%20Compressor%20Principles(Video-5).mp4http://video/YouTube-%20Centrifugal%20Pump%20Principles(Video-6).mp4http://video/YouTube-%203D%20Pumps%20Technical%20Animation(Video-7).mp4http://video/YouTube-%203D%20Pumps%20Technical%20Animation(Video-7).mp4http://video/YouTube-%203D%20Pumps%20Technical%20Animation(Video-7).mp4http://video/YouTube-%203D%20Pumps%20Technical%20Animation(Video-7).mp4http://video/YouTube-%20Centrifugal%20Pump%20Principles(Video-6).mp4http://video/YouTube-%20Centrifugal%20Pump%20Principles(Video-6).mp4http://video/YouTube-%20Centrifugal%20Pump%20Principles(Video-6).mp4http://video/YouTube-%20Centrifugal%20Compressor%20Principles(Video-5).mp4http://video/YouTube-%20Centrifugal%20Compressor%20Principles(Video-5).mp4http://video/YouTube-%20Centrifugal%20Compressor%20Principles(Video-5).mp4
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    Radial Compressors

    EfficienciesThe actual head developed by a compressor is less than the ideal or Euler Head (HE)due to various losses. In designing such machines it is usually difficult to predictthese losses. Engineers or Designers prefer to use empirical relations and/orefficiencies to consider the effects of these losses in the performance of themachine.a) Circulatory flow coefficient ( ):- the ideal or Euler Head (HE) is derived by

    considering an impeller with infinite number of vanes so as to avoid circulatoryflow. The effect of circulatory flow is to reduce v2 as shown in the velocity diagram.

    2

    '

    2

    u

    u

    v

    v

    As v2 reduces, vu2 also reduces and hencethe head will reduce.

    Hence, the circulatory flow coefficient () isgiven by,

    g

    vuH

    inletradialhavingimpellerforand

    g

    vuvuH

    uE

    uuE

    22

    0

    1

    1122

    ),90(

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    Efficiencies

    b) Overall Head Coefficient ( ):- the head developed by a turbomachine due toforced vortex flow has been derived as,

    But, due to the shape of the vanes and the casing the ratio can not be unity.Hence, in actual case the ratio 1 is replaced by .

    From this equation, D2 can also be determined.

    c) Hydraulic efficiency ( H):- the actual head or manometric head (Hm) developedby the machine is less than the ideal or Euler Head (HE) due to mainly friction andturbulence losses. To consider this effect, a hydraulic efficiency (H) is related as,

    )()( 11221122 uu

    m

    uu

    m

    t

    out

    E

    mH

    vuvu

    gH

    vuvum

    gHm

    P

    P

    H

    H

    .,122

    2

    2

    2 headoffShuttheisHWheregH

    uor

    g

    uH

    gHu

    2

    2

    N

    H

    N

    HgHD

    NDgHugHu

    5.84

    260

    602

    2

    2

    22

    2

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    Efficiencies

    d) Volumetric efficiency ( V):- the volumetric efficiency is a measure of the amountof leakage. It is given by,

    e) Mechanical efficiency ( m):- It is the ratio of the power at the impeller (Pt) to the

    power of the the shaft (Ps).

    f) Overall efficiency ( o):- It is the ratio of the fluid power (Pout) to the power of theprime mover (Pin).

    .,

    .arg,

    leakagetheisQand

    ratef lowedischtheisQWhereQQ

    Q

    L

    L

    V

    TPandT

    vuvum

    vuvumPWhereP

    P

    suu

    uut

    s

    tm

    ,)(

    )(,

    1122

    1122

    mVH

    in

    m

    mout

    in

    outo

    PgHQ

    gHmPWhereP

    P

    ,

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    Reading Assignment

    Refernce-1 ( Turbomachinery design and theory)Page 187 273

    Class work

    1. 10 kg/s of air is to be compressed in centrifugal compressor of the single sided impeller

    type. The ambient air conditions are 1 bar and 200

    C. The compressor runs at 20000 rpm,has isentropic efficiency of 80 % and compresses air from 1 bar static pressure to 4.5 bartotal pressure. The air enters the impeller eye with a velocity of 150 m/s with no prewhirl.Assuming that the ratio of whirl speed is 0.95, determine:

    a) rise in total temperature during compression,b) the impeller tip speed and tip diameter,c) power required to drive to drive the compressor,

    d) the external diameter of the eye, for which the internal diameter is 15 cm.

    Worksheet 6-1

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    Preliminary Design of a Centrifugal (Radial) Pump

    Example:-Design a water transport system given in Assignment 5-1.

    Design procedure:Step-1:- Determine the specific speed of the pump (Ns).

    rpm

    H

    QNNs

    14.13

    35

    017.01450

    4

    3

    4

    3

    %65o

    Estimate the pump efficiency (o)from the curve for a specific speedof 13.14 rpm and discharge of 1020LPM (Liter Per Minute).

    Adama University

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    http://worksheets%2C%20labs%2C%20and%20assignments%20%28tubomachinery%29/Assignment%205-1%20(MEng%203202).dochttp://worksheets%2C%20labs%2C%20and%20assignments%20%28tubomachinery%29/Assignment%205-1%20(MEng%203202).dochttp://worksheets%2C%20labs%2C%20and%20assignments%20%28tubomachinery%29/Assignment%205-1%20(MEng%203202).dochttp://worksheets%2C%20labs%2C%20and%20assignments%20%28tubomachinery%29/Assignment%205-1%20(MEng%203202).dochttp://worksheets%2C%20labs%2C%20and%20assignments%20%28tubomachinery%29/Assignment%205-1%20(MEng%203202).dochttp://worksheets%2C%20labs%2C%20and%20assignments%20%28tubomachinery%29/Assignment%205-1%20(MEng%203202).doc
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    Preliminary Design of a Centrifugal (Radial) Pump

    Step-2:-

    Determine the Maximum Shaft Power (Psmax).This can be determined from the performance curve.

    Determine shaft diameter (Ds) using stress theory.

    Q(m3/sec) Hp(m) Ps(HP) o(%) Hsys(m)

    0 46.2 4.2 0 26

    0.005 42.9 7 40.07 26.77

    0.01 39.6 9.4 55.21 29.09

    0.015 36.3 11.4 62.87 32.96

    0.02 33 12.9 67.21 38.38

    0.025 29.6 14 69.73 45.34

    0.03 26.3 14.6 71.05 53.85

    0.035 23 14.8 71.44 63.91

    0.04 19.7 14.6 70.97 75.52

    MPastress

    shearepermissibltheisandN

    PTWhere

    TD s

    ss

    s

    ss

    30

    ,30

    ,16 m ax

    3

    Adama University

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    Preliminary Design of a Centrifugal (Radial) Pump

    Step-3:-

    Determine the Hub diameter (DH) and the diameter of suction flange (Dsu).a) Hub diameter (DH) can be assumed 1 cm larger than the shaft diameter.

    b) Suction flange diameter (Dsu).

    Step-4:- Determine Impeller dimensions.

    a) Impeller eye diameter (Do).

    cmDD sH 1

    smvelocitysuctionisVWhereVQD susu

    su /3,4

    2

    1

    4H

    su

    o DV

    QDD

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    Preliminary Design of a Centrifugal (Radial) Pumpb) Impeller inlet passage width (b1).

    c) Inlet vane angle (1).

    d) Impeller outside diameter (D2).

    e) Impeller outlet passage width (b2).

    Note:- Other variables and dimensions can be determined from the

    velocity diagrams.

    1

    1

    1

    11

    1

    111

    1

    sin85.0,

    /25.0,

    D

    tZD

    orfactorncontractiotheisand

    smVvelocityflowisVWhere

    VD

    Qb sur

    r

    or DDand

    NDuWhere

    u

    V

    diagramsvelocitythefrominletradialaFor

    11

    1

    1

    11 ,

    60,tan

    ,

    05.1,5.84

    2 tcoefficienheadtheisWhereN

    HD

    00

    2

    222

    2 4030 toassumedbemayandVD

    Qb

    r

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    Preliminary Design of a Centrifugal (Radial) Pump

    Step-5:-

    Design vanes of the impeller.a) The radius of arc (), defining the shape between any two rings having radius ra

    and rb is given by,

    b) The number of vanes (Z) is given by,

    c) The thickness of vanes ( t ) can be determined from stress analysis. In actualdesign a uniform thickness of 3 mm is adopted.

    anglevanetheisWhererr

    rr

    aabb

    ab

    ,

    )coscos(2

    22

    221121

    12

    12 ,2

    )(sin5.6

    andWhere

    DD

    DDZ

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    Preliminary Design of a Centrifugal (Radial) Pump

    d) Plot or generate the curves of vanes.

    Procedure:- Divide the distance between the impeller internal radius r1 and r2 into a

    number of equal parts (say 4 or 5) as shown in the figure. For each division determine the values of r, ra, rb, and as shown in the

    table.

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    Preliminary Design of a Centrifugal (Radial) Pump

    Draw all concentric circles with O as center and radius r1,rx,rY,rZ and r2.

    Draw a radial line OJ = r1 from the center of rotation O to the point J. With J as center and angle OJK = 1 and radius 1, get point K . With K as center and radius 1, draw the arc JL . Draw a line through points L and K of length 2 = LM. With M as center and radius 2, draw the arc LN. Draw a line through points N and M of length 3 = NP. With P as center and radius 3, draw the arc NQ. Draw a line through points Q and P of length 4 = QR. With R as center and radius 4, draw the arc QS.

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    Preliminary Design of a Centrifugal (Radial) Pump

    Step-6:- Compute data for determining the passage width.

    Similarly, the following data can be obtained and the side view of theimpeller is drawn as shown.

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    Preliminary Design of a Centrifugal (Radial) Pump

    Both the front and side views are as shown below.

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    Preliminary Design of a Centrifugal (Radial) Pump

    Step-7:- Design the volute.

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    Preliminary Design of a Centrifugal (Radial) Pump

    The following relations are used in designing the volute.

    718.2log

    ,

    ,

    .6030sec

    60,

    tan,2

    tan2

    ,

    2

    ,

    ,360

    .

    .

    :

    2

    tan

    2

    00

    0

    23

    23

    3

    22

    0

    2

    2

    arithmnaturalofbasebasetheise

    radianinmeasuredangletheis

    vaneimpellertheofanglevaneguidetheisWhereeRR

    bygivenisRforrelationThe

    orlinesradialthewithofangleanhavingtrapezoidbetoassumedisvolutetheofshapetionalcrossbasicThe

    and

    RandRradiusanybetweencedistheisxWherexbb

    bygivenisbwidthaverageThe

    bb

    asassumedisbvolutetheofwidthbaseThe

    tonguethefrommeasuredangletheisWhereR

    dRb

    Q

    vR

    neglectedbetoassumedarelossesandslipofeffectThe

    f lowspiralnearlyhavetoassumedvolutetheinwaterThe

    sAssumption

    t

    R

    R

    ut

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    Preliminary Design of a Centrifugal (Radial) Pump

    The output of the mathematical relations for the volute is as shown in thetable.

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    Preliminary Design of a Centrifugal (Radial) Pump

    Using the values in the table, the volute can be drawn as shown in the figure.

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    Preliminary Design of a Centrifugal (Radial) Pump

    This is generally a preliminary design, but the results of a complete design issimilar to the design shown in the figures.

    Video-7

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    Two important areas of application of thermodynamics are powergeneration and refrigeration.

    The devices or systems used to produce a net power output are oftencalled heat engines, and the thermodynamic cycles they operate on arecalled power cycles.

    Main application areas

    ofThermodynamics

    Power cycles Refrigeration cycles

    Vapor powercycles

    Gaspower cycles

    Steam power plants

    Nuclear power plants

    Gasoline (Otto cycle) engines Diesel (Diesel cycle) engines

    Gas turbines (Brayton cycle)

    Refrigerators Heat pumps

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    What is a Steam Turbine ?

    A Steam Turbine is a turbomachine which converts steam or vapor

    (thermal) energy into mechanical energy. The so obtained mechanicalenergy is used to drive a generator.

    Steam power plants use steam or vapor as a working medium. Suchpower plants are: coal plants, nuclear plants, or natural gas plants,depending on the type of fuel used to supply heat to the water or steam.

    The thermodynamic cycle on which such power plants operate is called

    the vapor power cycle (Rankine cycle). In the vapor power cycle theworking fluid continuously vaporized and condensed. Vapor(steam) orwater is the most common working fluid used in vapor power cyclebecause of its many desirable characteristics, such as low cost,availability, and high enthalpy of vaporization.

    (Refer:- Engineering Thermodynamics).

    Steam turbineThermal(Steam)energy

    Mechanicalenergy

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    Principle of operation of a simple vapor power cycle (Rankine Cycle)

    A simple ideal vapor power cycle (Rankine cycle) consists of four

    processes.

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    Principle of operation of a Reheat-Regenerative vapor power cycle

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    Steam Turbine

    Basic configuration of a Steam Power Plant

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    Steam Turbine

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    Steam Turbine

    Basic configuration of a Steam Power Plant

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    Steam Turbine

    In a steam turbine, high-pressure steam from the boiler expands in a set

    of stationary blades (nozzles). The high-velocity steam from stationaryblades (nozzles) strikes the set of moving blades (buckets) as shown inthe figure.

    The kinetic energy of the steam or vapor isutilized to produce work on the turbine rotor.

    Low-pressure steam then leaves the turbineand enters into the condenser.

    There are two types of steam-turbine stagedesigns: the impulse stage, and the reaction stage.

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    Steam Turbine

    Principles of Impulse stage-turbines

    In the case of Impulse stage-turbine: pressure change (drop) occurs across thenozzles.

    pressure drop does not occur across themoving blades (buckets).

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    Steam Turbine

    Velocity diagram

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    Steam Turbine

    Velocity diagram

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    Steam Turbine

    Maximum Efficiency

    For supplementary notes, referRefernce-1 ( Turbomachinery design and theory)

    Page 279 324

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    Main application areas of Gas Power Cycles are in the design andoperation of IC Engines and Gas Turbines.

    Gas Turbines

    IC EnginesIn gas power cycles, the working fluid remains a gas throughout the entire cycle.Spark-ignition engines, compression-ignition engines, and conventional gas turbinesare familiar examples of devices that operate on a gas power cycle. In all theseengines, energy is provided by burning a fuel within the system boundaries. That is,

    they are internal combustion (IC) engines.

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    Principle of operation of a simple gas power cycle (Brayton Cycle)

    Brayton cycle

    The Brayton cycle, an ideal cycle for gas turbines, was first proposed byGeorge Brayton in 1870. This cycle can operate as an open cycle or as aclosed cycle.

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    The closed Brayton cycle composed of four internally reversible processes:

    isentropic compression (1-2), constant-pressure heat addition (2-3), isentropicexpansion (3-4), and constant-pressure heat rejection (4-1). Such a cycle isused in the combined Vapor-Power Cycle to generate electrical energy.

    Principle of operation of a simple gas power cycle (Brayton Cycle)

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    Ideal Jet-Propulsion cycleThe ideal Jet-Propulsion cycle is a modified Brayton open cycle, used in thedesign of jet propulsion systems. Gas-turbine engines are widely used to

    power aircraft because they are light and compact and have high power-to-weight ratio. Aircraft gas turbines operate on an open cycle called a jet-propulsion cycle. The ideal jet-propulsion cycle differs from the ideal Braytoncycle in that the gases are expanded to a pressure such that the powerproduced by the turbine is just sufficient to drive the compressor and the

    auxiliary equipment, such as a small generator and hydraulic pumps. That isthe net work output of a jet-propulsion cycle is zero. The gases that exit theturbine at a relatively high pressure are subsequently accelerated in a nozzleto provide the thrust to propel the aircraft.

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    What is a Wind Turbine ?

    A Wind Turbine is a turbomachine which converts wind (fluid) energy intomechanical energy. The so obtained mechanical energy is used to drive apump or a generator.

    Wind energy is a renewable, pollution free and cheap energy source likethose of water and solar energies.Wind is air in motion, caused by uneven heating of the earth by the sun.

    This creates difference in densities and leads to a mass movement of airfrom one location to the other.

    Wind Turbines may be classified as Vertical-Axis, Horizontal-Axis, Fast-Running, Slow-Running, etc.

    Wind turbineWind

    energy

    Mechanical

    energy

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    Component parts of a Horizontal-Axis, Fast-Running Wind Turbine

    A

    Detail A

    Class work

    1. Write the principle of operation.

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    Principle of operationThe figure shown below is the cross-section of the rotor blade called anaerofoil. It is similar to the aerofoil of an aircraft.

    When air is moving over the surface of

    an aerofoil, a pressure difference iscreated ( Refer:-Bernoullis Principle ).This pressure difference creates aresultant force F. If this force isdecomposed into perpendicular andparallel to flow direction, results Lift L

    and Drag D.

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    Determination of maximum power available from the wind

    .,

    .,2

    1

    0

    2

    0

    velocityflowairisVand

    airofmassismwheremVKE

    As it is already defined, wind is

    air in motion. Since air hasmass and a certain velocity,then it has got a kinetic energygiven by:

    Question:-Is it possible to getsuch power in a real machine ?

    I II IVIII

    p

    p

    2

    02

    1

    ,)(

    Vmt

    KEP

    bygivenisPPowerWind

    wind

    wind

    3

    0

    0

    2

    1,

    .

    ,

    ,

    AVPHence

    airofdensityis

    rotortheofareasweptisAWhere

    AVmbut

    awind

    a

    a

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    Determination of maximum power available from the wind

    The maximum mechanical

    power has a direct relationshipwith Cpmax. Cpmax is known asthe Betzs coefficient and isobtained from the followingassumptions: flow is compressible,

    flow is non-viscous, flow is entirely axial.

    Hence,

    I II IVIII

    p

    p

    )2.11..(........................................)'(,

    111...........)()(

    :'

    1010

    AppFlso

    ).(uVAuuVmF

    MotionofLawSecondsNewtonrom

    th

    ath

    )3.11(............................22

    :)()('

    22

    00

    g

    u

    g

    p

    g

    V

    g

    p

    IIandIbetweenEquationsBernoulliApplynig

    aa

    )4.11(..............................22

    '

    :)()('

    2

    10

    2

    gu

    gp

    gu

    gp

    IVandIIIbetweenEquationsBernoulliApplynig

    aa

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    Determination of maximum power available from the wind

    I II IVIII

    p

    p

    )5.11(................................)(2

    1'

    :)4.11()3.11(

    2

    1

    2

    0 uVpp

    andEquationsFrom

    a

    )6.11(................................)(2

    1

    :)2.11(int)5.11(

    2

    1

    2

    0 uVAF

    oEquationsngSubstituti

    ath

    )7.11........(........................................)(2

    1

    )()(2

    1

    :)1.11()6.11(

    10

    10

    2

    1

    2

    0

    uVu

    uVAuuVA

    andEquationsEquating

    aa

    Which shows that the airvelocity u at the rotor isequal to the mean of theupstream and downstream

    velocities V0 and u1.

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    Determination of maximum power available from the wind

    I II IVIII

    p

    p

    Axial Induction Factor a

    The axial induction factor ais a measure of the decreasein axial air velocity through theturbine .

    The power extracted by therotor is the difference betweenthe power of the wind up-

    steam and down-stream of therotor. Hence, Pmech is given by,

    )8.11...(..................................................0

    )1( Vau

    )9.11(..................................................)21(

    )(2

    1)1(

    :)7.11()8.11(

    01

    100

    Vau

    uVVa

    andEquationsEquating

    )10.11(................))1(4(2

    1

    :,

    )(2

    1

    23

    0

    1

    2

    1

    2

    0

    aaVAP

    givesuanduforngSubstituti

    uVuAP

    amech

    amech

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    Determination of maximum power available from the wind

    I II IVIII

    p

    p

    Maximum power is obtainedwhen Cp attains its maximumvalue. Hence, Cpmax can beobtained by differentiating theabove equation,

    2

    3

    0

    23

    0

    )1(4

    2

    1

    ))1(4(2

    1

    aa

    AV

    aaVA

    P

    PC

    a

    a

    wind

    mech

    p

    3

    1

    0)1(4(2

    aaada

    d

    da

    dCp

    3

    ))3

    12(1(

    )21(

    ),9.11(sin

    max

    0

    0

    01

    1

    V

    V

    Vau

    equqtionguobtainedbecanpower

    imumthetoingcorresponduofvalueThe

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    Determination of maximum power available from the wind

    I II IVIII

    p

    p

    The maximum mechanical

    power is given by,

    Power Density (PD)The ratio of mechanical power

    (Pmech) to swept area (A) ofthe rotor.

    Assignment:- Plot the curves

    of PDversus V0.

    27

    16

    )3

    11)(

    3

    1(4

    )1(4

    2

    2

    ma x

    aaCp

    )2

    1(

    27

    16 30ma x AVP amach

    )2

    1(

    27

    16 30V

    A

    PP a

    mechD

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    Fluid Couplings and Torque Converters are power transmitting systems. Power istransmitted between the driving and driven shaft usually by mechanical means like

    gear drive. In such drives the shock loads and vibration are transmitted from one sideto the other which is not desirable. Also in gear drives there is a speed fluctuation. Incertain cases where the driven machine has a large inertia, the driving prime moverlike electric motor will not be able to provide a large starting torque. Instead of themechanical connection if fluids can be used for such drives, high inertia can be met.Also shock loads and vibration will not be transmitted. Smooth speed variation is also

    possible.There are two types of power transmitting devices using a fluid.

    i) Fluid Couplingii) Torque Converter or Torque Multiplier

    i) Fluid Coupling

    A sectional view of a Fluid Coupling is as shown in thefigure. In this device the driving and driven shafts are notrigidly connected. The drive shaft carries a pump withradial vanes and the driven shaft carries a turbine runner.Both of these are enclosed in a casing filled with oil ofsuitable viscosity. The pump accelerates the oil by

    imparting energy to it.

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    i) Fluid Coupling

    The oil is then directed to hit the turbine vanes where

    energy is absorbed and the oil is decelerated. Thedecelerated oil now enters the pump and the cycle isrepeated. There is no flow of fluid to or from the outside.The oil transfers energy from the drive shaft to the drivenshaft. As there is no mechanical connection between theshafts, shock loads or vibration will not be transmittedfrom one to the other. The turbine will start rotating onlyafter a certain level of energy is picked up by the oil fromthe pump.

    ii) Torque ConverterIn case of Fluid Coupling the torque on the driver and

    driven members are equal. The application is for direct-drive machines. But there are cases where the torquerequired at the driven member should be more than thetorque on the driver or in other words, the speed requiredat the driven member should be less than the speed onthe driver. Such an application is widely used in

    automobile transmission systems.

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    ii) Torque Converter

    One advantage of Torque Converter is that the speedvariation is smooth as compared to mechanicalconnection (Gear Drive) as shown in the figure.

    A sectional view of Torque Converter is as shown in thefigure. Torque Converter consists of three elements:Pump impeller, Turbine runner and a Guide wheel orStator.The pump is connected to the drive shaft. The guidevanes are fixed. The turbine runner is connected to thedriven shaft. All the three are enclosed in a casing filledwith a suitable transmission oil. When the engine starts tooperate, mechanical energy from the crankshaft istransmitted to the driven shaft and then to the pump

    impeller. The impeller then imparts energy to the oil.

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    ii) Torque ConverterDue to centrifugal force, the oil moves out of the impellerto strike the turbine runner. In doing so the fluid impartsmomentum to the turbine and the turbine together with thedriving shaft starts to rotate and transmit the power to theplanetary gear box. The oil after being expended itsenergy in the turbine runner made to flow back to thepump impeller through a stator or guide vane. This

    produces a reactive torque on the pump which increasesthe torque to be transmitted.

    Pump ImpellerTurbine Runner

    Automatic transmissionVideo-4

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    http://video/Torque%20converter%20(Automatic%20transmission)(Video-4).wmvhttp://video/Torque%20converter%20(Automatic%20transmission)(Video-4).wmvhttp://video/Torque%20converter%20(Automatic%20transmission)(Video-4).wmvhttp://video/Torque%20converter%20(Automatic%20transmission)(Video-4).wmv
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    ii) Torque Converter

    Automatic transmission

    Manual transmission

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    Endof

    the Course

    Final Examination !