presentation on steam

Upload: jagath-wickramasinghe

Post on 05-Apr-2018

219 views

Category:

Documents


0 download

TRANSCRIPT

  • 7/31/2019 Presentation on Steam

    1/37

    BASICS OF STEAM What is steam?

    -Gaseous phase of H2O At atmospheric pressure,

    - Evaporates at 100 deg. C

    - Solidifies at 0 deg.C

    When pressure increases,- Temperature of evaporation increases.

    - Specific volume reduces

    Will steam be completely gaseous?

    No. It will carry water droplets. ie: wet steam

    What is dry steam?

    - Steam with no water droplets.

  • 7/31/2019 Presentation on Steam

    2/37

  • 7/31/2019 Presentation on Steam

    3/37

    Enthalpy hf - Liquid enthalpy or sensible heat

    Heat energy required to raise the temperature from a datum of 0 deg. C to

    current temperature.

    hfg Enthalpy of evaporation

    Amount of heat required to change the state f water at its boiling

    temperature into steam

    hg Total enthalpy of saturated steam

    Total energy required to change the state to saturated steam from a datumof 0 deg.C

    hg = hf+ hfg

    Dryness fraction

    What is dryness fraction?

    Fraction of mass of dry steam out of total mass- Actual enthalpy =hf+hfg.X

    - Actual specific volume = Vg.X

  • 7/31/2019 Presentation on Steam

    4/37

  • 7/31/2019 Presentation on Steam

    5/37

    Flash steam

    Proportion of flash steam=(hf at P1)-(hf at P2)

    hfg at P2

  • 7/31/2019 Presentation on Steam

    6/37

    Disadvantages of wet steam

    - High line losses

    - Cavitations in turbine blades

    - Less thermodynamic efficiencies

    ( Carnot cycle, Rankine cycle)

    Solution?

    Superheated steam

  • 7/31/2019 Presentation on Steam

    7/37

    SUPERHEATED STEAM

    Less line losses Less cavitations in turbine blades

    Higher thermodynamic efficiencies

    Advantages of superheated steam

    How superheated steam is generated ?

    - Can it be done in a boiler?

  • 7/31/2019 Presentation on Steam

    8/37

    Disadvantages of superheated

    steam

    Poor heat transfer

    Temperature drop in heat transfer

  • 7/31/2019 Presentation on Steam

    9/37

  • 7/31/2019 Presentation on Steam

    10/37

    What is entropy?

    Can it be measured with a gauge?

    No

    A calculated value from the things that can be

    measured

    Entropy at the latter condition is always high

    Entropy = Enthalpy / Absolute temperature

  • 7/31/2019 Presentation on Steam

    11/37

    Sat water line Sat. steam line

    Constant

    pressure lines

    Constant dryness fraction

  • 7/31/2019 Presentation on Steam

    12/37

    Steam flow metering

  • 7/31/2019 Presentation on Steam

    13/37

    Important parameters

    Repeatability-indicating same value for identical flow

    Uncertainty

    - Deviation of true value Accuracy

    -Indication of correct flow rate against the true value

    obtained by extensive calibration procedure

    Turn down- Range of flowrates over which the meter will work within

    the accuracy and repeatability

  • 7/31/2019 Presentation on Steam

    14/37

    Example

  • 7/31/2019 Presentation on Steam

    15/37

    Example

    Maximum flow rate = 1000 kg/hr

    Turndown =4:1

    = 1000/4=250 kg/hr

  • 7/31/2019 Presentation on Steam

    16/37

    Turn down ratios of different

    flowmeters

  • 7/31/2019 Presentation on Steam

    17/37

    Types of flow meters

    Orifice plate flowmeter

    Pitot tube

    Turbine flowmeter Variable area flowmeter

    Vortex shedding flowmeter

  • 7/31/2019 Presentation on Steam

    18/37

    Orifice plate flow meter

  • 7/31/2019 Presentation on Steam

    19/37

    Orifice plate flow meter

  • 7/31/2019 Presentation on Steam

    20/37

    Orifice plate flow meter

  • 7/31/2019 Presentation on Steam

    21/37

    Theory

    Assume

    and

    By substituting flow, Q in V1 and V2,

    and

    Then,

  • 7/31/2019 Presentation on Steam

    22/37

    Theory ..

    Substituting,

    Where,

    C: Coefficient of discharge

    e: Coefficient of expansion

  • 7/31/2019 Presentation on Steam

    23/37

    Theory.

    As per ISO 5167,

    Where,Beta= D2/D1 L1 and L2 are functions on tap type

    and it is:

    L1=L2=0 for corner taps

    L1=1 L2=0.47 for D & D/2 taps

    L1=L2=0.0254/D D[m] for 1" taps

  • 7/31/2019 Presentation on Steam

    24/37

    Theory

  • 7/31/2019 Presentation on Steam

    25/37

    Computer Program for calibrating

    orifice plates

    - Based on ISO5167

    - Need to give data on Fluid properties

    - Fluid

    - Density

    - Viscosity- Pressure

    - Temperature

    Pipe properties

    - Pipe diameter

    - Roughness

    - Material Orifice plate properties

    - Diameter

    - Type of tapping

    - Material

  • 7/31/2019 Presentation on Steam

    26/37

    Sizing the orifice plate

    Select 70% of usual full scale flow for 50% dp.

    - gives more accurate reading

    - Protect from dp reading exceeding the limit.

    Select suitable full scale dp Select suitable beta value

    - Values between 0.4 and 0.7 is preferred

    - Smaller values give higher pressure drops

    - Larger values reduces the accuracyCalculate dp for different flows

  • 7/31/2019 Presentation on Steam

    27/37

    Typical installation of a orifice plate

    flow meter

  • 7/31/2019 Presentation on Steam

    28/37

    Guide for installing an orifice plate

    Use small bore pipes as tappings

    Do not tap from the bottom of the line

    Keep sufficient straight lengths in up and down streams

    Keep the orifice plate exactly concentric with the pipe

    Prevent from packing gasket misalignments

    Place the orifice plate in the correct orientation

    Mark the flow direction on the plate handle

    Mark the size of the opening on the handle

  • 7/31/2019 Presentation on Steam

    29/37

    Guide for installing an orifice plate.....

  • 7/31/2019 Presentation on Steam

    30/37

    Guide for installing an orifice

    plate.....

  • 7/31/2019 Presentation on Steam

    31/37

    Advantages of orifice flowmeters

    Simple and rugged

    Good accuracy

    Low cost No calibration is required provided

    calculations, tolarances and installation

    comply with ISO 5167

  • 7/31/2019 Presentation on Steam

    32/37

    Disadvantages of orifice plate

    flowmeters

    Turndown is limited to 4:1

    Orifice plate can buckle due to water

    hammer

    Erosion of the square edge with time

    High unobstructed straight length is

    required

  • 7/31/2019 Presentation on Steam

    33/37

    POWER GENERATION

  • 7/31/2019 Presentation on Steam

    34/37

  • 7/31/2019 Presentation on Steam

    35/37

  • 7/31/2019 Presentation on Steam

    36/37

    Efficiency

  • 7/31/2019 Presentation on Steam

    37/37

    Types of turbines based on output

    conditions Non condensing or back pressure

    Exhaust steam is used for processes

    Controlled by a back end pressure regulator

    Condensing Used when primary objective is power

    Dryness fraction of exhaust is more than 90%

    Reheat Steam is extracted at the middle and supplied to the next stage after re-

    heating

    Used for power generation plants

    Extracting Steam is extracted in intermediate stages

    Induce Low pressure steam is introduced at intermediate stages

    To get more power