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    Irreversible Flow from Turbine Exit to Condenser

    P M V Subbarao

    Professor

    Mechanical Engineering Department

    I I T Delhi

    Irreversibilities due to Closed Cycle Policy ..

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    The Last Stage of LP Turbine

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    First Stage of A Turbine : Governing Stage

    A governing stage is the first stage in a turbine with nozzle

    steam distribution. The principal design feature of a governing stage is that its

    degree of partiality changes with variations of flow rate throughthe turbine.

    The nozzles of a governing stages are combined into groups,

    each of them being supplied with steam from a separategoverning valve.

    A governing stage is separated by a spacious chamber from thesubsequent non-controlled stages.

    Governing stages may be of a single-row or two-row type.

    Single row impulse governing stage is employed for an enthalpydrop of 80-120 kJ/kg.

    Two row governing stages are used when enthalpy drop is high,100 250 kJ/kg.

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    Governing Stage

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    Selection of Enthalpy Drop & Type of Governing

    stage

    The enthalpy drop & type of governing stages are selected by

    considering the probable effect of the governing stage on the

    design and efficiency of the turbine.

    Higher the number of governing stages, lower will be the

    number of other stages.

    A high enthalpy drop in governing stage ensures a lower

    temperature of steam in its chamber and permits application of

    less expensive materials.

    In high capacity steam turbines, a single-row governing stages

    are preferred, since the advantages of elevated enthalpy drop

    are justified economically.

    The efficiency of governing stages,

    in

    inVustageg

    T

    p

    m

    k0002.0

    83.0/,

    in

    inVustagesg

    T

    p

    m

    k0002.0

    8.0/2,

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    Steam Path in Non-Controlled Stages

    Estimate approximate mass flow rate of steam by assuming an

    overall turbine internal efficiency of 0.85.

    Calculate flow through the condenser, using optimum of number

    of FWHs. (Using Cycle Calculations).

    Calculate Modified Efficiency of Low volume and intermediate

    volume stages.

    For a group of stages between two successive FWHs.

    Z

    h

    m

    lgroup

    iso

    steam

    avgroup

    listages

    ,1

    2sin1

    2000

    6001

    5.0925.0

    groupegroupiav ..

    Average density is calculated as

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    The efficiency of groups of very high volume stages:

    While designing the steam path, it is essential to consider the

    pressure losses in the following:

    Pressure loss in reheater: 0.1 prh.

    Pressure loss in connecting pipes between turbine

    cylinders:0.2ppipe.

    group

    iso

    ev

    group

    isogegigroup

    hvh

    hhxx

    10000

    4001

    28.01870.0

    ,,

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    Internal Reheating due to Irreversibilities

    3

    4s

    4IIs

    4IIIs

    4Is

    4Vs

    4IVs

    4Ia

    4IIa

    4IIIa

    4IVa

    4Va

    4VIs4VIa

    T

    s

    Governing group

    Group 1

    Group 2

    Group 3

    Group 4

    Group 5

    Macro available enthalpy:

    Micro available enthalpy:

    shh 43

    ...444443

    sasas IIIIIIIII

    hhhhhh

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    Macro available enthalpy:

    Micro available enthalpy:

    s

    hh43

    N

    Ijsas jjI

    hhhh 14443

    Reheat Factor:

    N

    Ijsas

    sh

    jjI hhhh

    hhR

    14443

    43

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    Internal Reheating due to Irreversibilities : HP

    3

    4s

    4IIs

    4IIIs

    4Is

    4Vs

    4IVs

    4Ia

    4IIa

    4IIIa

    4IVa

    4Va

    4VIs4VIa

    T

    s

    Governing stage

    Stage 1

    Stage 2

    Stage 3

    Stage 4

    Stage 5

    22.33 MPa,3379.0

    15.74 MPa,3303.0 k J/kg

    13.77 MPa, 3269.0 k J/kg

    12.12 MPa, 3236.5.0 k J/kg

    10.56 MPa, 3203.8 k J/kg

    9.2 MPa, 3171.0 k J/kg

    7.94 MPa, 3140.4 k J/kg

    4VIIa6.9 MPa, 3104.9 k J/kg

    4VIIIa

    5.17 MPa, 3036.7 k J/kg4IX

    a

    5.95 MPa, 3070.9 k J/

    Pho=5 %

    Pho=19.5%

    Pho=21%

    Pho=22%

    Pho=23.5%

    Pho=25%

    Pho=30%

    Pho=32%

    Stage 6

    Stage 7

    Stage 8

    Pho=35%

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    0

    2

    4

    6

    8

    10

    12

    14

    HP1(1s

    tSt.)

    HP4

    HP7

    HP10

    HP13

    HP16 IP

    1IP

    4IP

    7IP

    10

    IP13

    LP2

    LP5

    Stages

    Loss

    (kJ/kg) Cumulative loss

    Cumulative Losses for All Stages : 500 MW

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    Definition of Efficiency

    Relative blade efficiency is calculated as:

    Internal Relative Efficiency is calculated as:

    dropEnthalpyEffective

    lossBladeMoving&Nozzle-dropEntalpyEffectiverel

    dropEnthalpyEffectivelossprofile-lossleakage-lossesBladeMoving&Nozzle-dropEntalpyEffectiveint, rel

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    Blade Efficiency & Internal Relative Efficiency: 800 MW

    0.5

    0.55

    0.6

    0.65

    0.7

    0.75

    0.8

    0.85

    0.9

    0.95

    1

    0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25

    Efficiency

    Stage No

    Relative Blade efficiencyRelative internal efficiency

    LP Cylinder

    efficiency=78.0

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    LP Turbine Exhaust System

    In a condensing steam turbine, the low-pressure exhaust hood,consisting of a diffuser and a collector or volute!, connects the last

    stage turbine and the condenser. The function of the hood is to transfer the turbine leaving kinetic

    energy to potential energy while guiding the flow from the turbineexit plane to the condenser.

    Most of exhaust hoods discharge towards the downward condenser.

    Flow inside the hood therefore must turn about 90 deg from theaxial direction to the radial direction before exhausting into thecondenser.

    The 90-deg turning results in vortical flow in the upper half part ofthe collector and also high losses.

    The exhaust hood is one of the few steam turbine components thathas the considerable aerodynamic losses.

    It is a challenge for engineers to operate a hood with high pressurerecovery and low total pressure loss in a compact axial length.

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    Exhaust Hood

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    Exhaust Diffuser For L P Turbine

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    Steam Turbine Exhaust Size Selection

    The steam leaving the last stage of a

    condensing steam turbine can carry

    considerably useful power to the

    condenser as kinetic energy.

    The turbine performance analysis needs to

    identify an exhaust area for a particular

    load that provides a balance between

    exhaust loss and capital investment inturbine equipment.

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    Path Lines in Exhaust Hood

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    Exhaust Losses

    Exhaust losses are losses which occur between last

    stage of turbine and condenser.

    Exhaust losses made up of four components:

    Actual leaving losses Gross hood loss

    Annulus restriction loss

    Turn up loss

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    Residual velocity loss

    Steam leaving the last stage of the turbine has certain velocity, which

    represent the amount of kinetic energy that cannot be imparted to theturbine shaft and thus it is wasted

    Exhaust end loss

    1. Exhaust end loss occur between the last stage of low pressure turbineand condenser inlet.

    2. Exhaust loss depends on the absolute steam velocity.

    Turbine Exhaust end loss

    = Expansion-line -end point - Used energy at end point.

    T i l h t l h i di t ib ti f t l

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    Turn-up loss

    Total Exhaust

    Loss

    Gross hoodloss

    Actual leaving

    loss

    Annulus

    restriction loss

    Annulus Velocity (m/s)

    ExhaustLoss,

    kJ/k

    gofdryflow

    0 120 150 180 240 300 360

    10

    20

    30

    40

    50Annulus velocity (m/s)

    Condenser flow

    rateAnnulus area

    Percentage of Moisture atthe Expansion line endpoint

    Typical exhaust loss curve showing distribution of component loss

    SP.Volume

    an

    steamexan

    A

    xvmV

    3600

    01.01.

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    Optimal Design of Exhaust Hood

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    Performance Analysis of Power Plant

    Condensers

    P M V Subbarao

    Professor

    Mechanical Engineering DepartmentI I T Delhi

    A Device Which makes Power Plant A True Cycle..

    A Device Which set the limit on minimum cycle

    pressure..

    T S Di R ki C l ith FWH

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    T-S Diagram : Rankine Cycle with FWHs.

    ?,, exitcondincond pp

    inCWT ,outCWT ,

    ?TTD

    exhaustturbinep ,

    hoodp

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    A Device to Convert Dead Steam into Live Water

    Water ready to take

    Rebirth

    Dead Steam

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    Steam Condenser

    Steam condenser is a closed space into which steam exits the turbine and is forcedto give up its latent heat of vaporization.

    It is a necessary component of a steam power plant because of two reasons. It converts dead steam into live feed water.

    It lowers the cost of supply of cleaning and treating of working fluid.

    It is far easier to pump a liquid than a steam.

    It increases the efficiency of the cycle by allowing the plant to operate on largest

    possible temperature difference between source and sink.

    The steams latent heat of condensation is passed to the water flowing through thetubes of condenser.

    After steam condenses, the saturated water continues to transfer heat to coolingwater as it falls to the bottom of the condenser called, hotwell.

    The difference between saturation temperature corresponding to condenservaccum and temperature of condensate in hotwellis called condensate depression.

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    Two-Pass Surface Condenser

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    Layouts of A Condenser

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    Layouts of A Condenser

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    An Integral Steam Turbine and Condenser System