ME 63-Lecture 2-AY 20112012

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    Lecture 2

    Chapter 3

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    Pure Substance

    a substance that has a homogeneous and invariable chemicalcomposition

    may exist in more than one phase (i.e., mixture of phases) butchemical composition is similar in all phases

    Example: A mixture of ice and liquid water

    A mixture of liquid water and vapor (steam)

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    Phase and State Changes of a

    Substance A pure substance can exist in different phases (solid,

    liquid, or gas)

    It can exist in equilibrium as a mixture of differentphases

    When a pure substance exists as a mixture of two ormore phases, it is in phase equilibrium when there isno tendency for the mass of each phase to change

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    Phase and State Changes of a

    Substance

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    T-v diagram for the heating process of water at

    constant pressure.

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    Definitions:

    Saturation Temperature

    - the temperature at which vaporization takes placefor a given pressure

    Saturation Pressure

    - the pressure at which vaporization takes place for agiven temperature

    For a pure substance, there is a definite relation

    between the saturation temperature and saturationpressure which can be shown by the vapor-pressurecurve.

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    A substance can exist in any of the

    following phases

    Compressed Liquid

    Subcooled Liquid

    Saturated Liquid

    Saturated Vapor

    Saturated Mixture

    Superheated Vapor

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    Compressed Liquid

    a liquid whose pressure is higher than the saturation pressure

    for the existing liquid temperature (sat. temp.)Subcooled Liquid

    another term for compressed liquid; a liquid whosetemperature is lower than the saturation temperature for theexisting liquid pressure (the saturation pressure)

    Saturated Liquidsubstance that exists as liquid only at saturation temperatureAND saturation pressure

    Saturated Vapor

    substance that exists as vapor only at saturation temperature

    AND saturation pressure

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    Saturated Mixture

    substance that exists as a mixture of liquid and vapor for a

    given temperature (saturation temperature) AND pressure(saturation pressure)

    The liquid component in the mixture has the same propertiesas saturated liquid for the given temperature or pressure

    The vapor component in the mixture has the same propertiesas saturated vapor for the given temperature or pressure

    For a liquid-vapor mixture, a property that relates the mass ofvapor to the mass of the mixture is defined:

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    Superheated Vapor

    substance in vapor phase whose temperature is higherthan the saturation temperature for the existing

    pressure

    OR

    substance in vapor phase whose pressure is lower than

    the saturation pressure for the existing temperature

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    Quality - the ratio of the mass of vapor component to thetotal mass of the liquid-vapor mixture

    x = mg / m = mass of vapor / total mass of liquid-vapormixture

    where

    mf = mass of liquid component

    mg = mass of vapor component

    m = mf + mg

    Note that

    x = 0 for saturated liquid

    x = 1 for saturated vapor

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    Property Relationships

    *note

    liq gV V V

    liq f g gmv m v m v

    fg g f v v v

    (1 ) f g f fgv x v x v v x v

    specific volume

    =specific volume of a saturated liquid

    =specific volume of a saturated gas

    fg

    f

    g

    v average

    v

    v

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    Critical Point

    The state wherein the saturated liquid and saturated

    vapor states are identical

    It is specified by the critical temperature Tc , critical

    pressure Pc , or critical specific volumeAt pressures above the critical pressure, the liquid

    and vapor phases do not exist in equilibrium

    At supercritical pressures, the substance is simply

    called a fluid

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    T-v Diagram

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    P-V Diagram

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    Processes that involve phase change

    Sublimation direct phase change from solid to vapor along the sublimation line, the solid and vapor phases (solid-

    vapor mixture) exist in equilibriumFusion direct phase change from solid to liquid along the fusion line, the solid and liquid phases (solid-liquid

    mixture) exist in equilibriumVaporization direct phase change from liquid to vapor along the vaporization line, the liquid and vapor phases

    (liquid-vapor mixture) exist in equilibrium

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    Triple Point

    the state in which three phases are present in

    equilibrium

    for a pure substance, there may be many

    triple points but only one triple point where

    the solid, liquid, and vapor phases exist in

    equilibrium

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    Tables of Thermodynamic Properties

    The thermodynamic tables lists other properties of asubstance (e.g., v, u, h, s) as a function of two independentproperties, commonly T and P

    1. Saturated Liquid

    Saturated Vapor Region Tabulates properties of saturated liquid-vapor mixtures for a

    given temperature ( which is also equal to Tsat ) or a givenpressure ( which is also equal to Psat )

    Quality - An independent property of the liquid-vapor mixture

    which can be used to specify its state, defined as

    vapor vapor g

    mixture vapor liquid g f

    m m mx

    m m m m m

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    Property Relationships

    liq vapV V V

    liq f vap gmv m v m v

    fg g f v v v

    (1 ) f g f fgv x v x v v x v

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    3. Compressed or Subcooled Liquid Region

    Tabulates properties of compressed or subcooledliquid

    Tests

    1. For a given T and P, see if P > Psat) T or T 1 actual density is less than predicted from

    ideal gas equation due to greater intermolecular

    repulsive force caused by much reduced

    intermolecular distances

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    GENERALIZED COMPRESSIBILITY CHART

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    Pr = P / Pc = reduced pressure

    Tr = T / Tc = reduced temperature

    Pc = critical pressure

    Tc = critical temperature

    See Table A.2 for Pc and Tc ofvarious substances

    This plot of the generalizedcompressibility factor Z in termsof the reduced pressure Pr andreduced temperature Tr is

    applicable to various simplesubstances.

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    The generalized compressibility chart indicates that

    ideal gas behavior can be assumed when P 2Tc up to P 4 to 5 times Pc

    For other conditions, especially in the superheated

    vapor region, it is more accurate to use thethermodynamic tables

    May be used to estimate P-v-T data of substances ifno tables are available