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  • 7/27/2019 Generalized Compressibility

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    EGR 334 Thermodynamics

    Chapter 3: Section 11

    Lecture 09:Generalized Compressibility Chart

    Quiz Today?

    http://localhost/var/www/apps/conversion/tmp/Quiz%20Choice%20on%20Monday.pptxhttp://localhost/var/www/apps/conversion/tmp/Quiz%20Choice%20on%20Monday.pptx
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    Todays main concepts: Universal Gas Constant, R Compressibility Factor, Z. Be able to use the Generalized Compressibility to solve problems Be able to use Z to determine if a gas can be considered to be an

    ideal gas. Be able to explain Equation of State

    Reading Assignment:

    Homework Assignment:

    Read Chap 3: Sections 12-14

    From Chap 3: 92, 93, 96, 99

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    Like c p and c v, todays topic is about compressible gases. This method does not work for two phase mixtures such aswater/steam. It only applies to gases .

    3

    Limitation:

    pv Z RT

    where absolute pressureabsolute temperature

    molar specific volume

    pT

    v

    mol

    f mol

    8.314 kJ/kmol K

    1.986 Btu/lb

    1545 ft lb /lb

    o

    o

    R R

    R

    and

    Compressibility Factor, Z

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    Universal Gas Constant

    4

    Substance Chem. Formula R (kJ/kg-K) R(Btu/lm-R)

    Air --- 0.2870 0.06855

    Ammonia NH 3 0.4882 0.11662Argon Ar 0.2082 0.04972

    Carbon Dioxide CO 2 0.1889 0.04513

    Carbon Monoxide CO 0.2968 0.07090

    Helium He 2.0769 0.49613Hydrogen H 2 4.1240 0.98512

    Methane CH 4 0.5183 0.12382

    Nitrogen N 2 0.2968 0.07090

    Oxygen O 2 0.2598 0.06206

    Water H 2O 0.4614 0.11021

    R can also be expresses on a per mole basis:

    R R M

    where M is the molecular weight (see Tables A-1 and A-1E)

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    5Sec 3.11 : Compressibility

    For low pressure gases it was noted from experiment that therewas a linear behavior between volume and pressure at constanttemperature.

    The constant R is called the Universal Gas Constant.Where does this constant come from?

    and the limit as P 0

    then RT

    Pv P 0lim

    The ideal gas model assumeslow Pmolecules are elastic spheresno forces between molecules

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    6Sec 3.11 : Compressibility

    To compensate for non-ideal behavior we can use other equations of state (EOS) or use compressibility

    RT Pv

    Z

    Define the compressibility factor Z,

    Z 1 when

    ideal gasnear critical pointT >> Tc or (T > 2T c)

    Step 1: Thus, analyze Z by first

    looking at the reduced variables

    C R

    C R

    T

    T T

    P P

    P Pc = Critical Pressure

    Tc = Critical Pressure

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    Step 2: Using the reduced pressure, p r and reduced temperature, T r determine Z from the Generalized compressibility charts.(see Figures A-1, A-2, and A-3 in appendix).

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    8

    Step 3: Use Z toa) state whether the substance behaves as an ideal gas, if Z 1

    b) calculate the specific volume of the gas using

    ' Rc

    c

    vv

    RT p

    vv M

    The figures also lets youdirectly read reducedspecific volume where

    RT v Z

    pwhere

    R R M

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    9Sec 3.11 : Compressibility

    Summarize:

    1) from given information,calculate any two of these:

    or M R R

    RC

    p p

    p R C

    T T

    T ' R

    c

    c

    vv

    RT p

    2) Using Figures A-1, A-2, and A-3,read the value of Z

    3) Calculate the missing property using

    pv Z

    RT pv

    Z RT

    where vv M

    (Note: p c and T c can be found onTables A-1 and A-1E)

    (Note: M for different gases can be foundon Table 3.1 on page 123.) mol

    f mol

    8.314 kJ/kmol K

    1.986 Btu/lb

    1545 ft lb /lb

    o

    o

    R R

    R

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    10

    Example: (3.95) A tank contains 2 m 3 of air at -93C and a gagepressure of 1.4 MPa. Determine the mass of air, in kg. The localatmospheric pressure is 1 atm.

    Sec 3.11 : Compressibility

    V = 2 m 3 T = -93Cpgage = 1.4 MPapatm = 0.101 MPa

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    11

    Example: (3.95) Determine the mass of air, in kg

    Sec 3.11 : Compressibility

    V = 2 m 3 T = -93C = 180 Kp = p gauge + p atm = 1.4 MPa + 0.101 MPa = 1.5 MPa = 15 bar

    From Table A-1 (p. 816): For Air: 16) T c = 133 K p c = 37.7 bar

    150.40

    37.7180

    1.35133

    R C

    RC

    p p

    pT

    T T

    V

    m p pv Z RT RT

    25 315 10 2 1 1

    61.1

    1000 10.95 8.314 18028.97

    N m

    kJ kmol kmol K kg

    m kJ J m kg

    J N m K

    Z=0.95ViewCompressibility Figure

    pV pV m

    R ZRT Z T M

    http://localhost/var/www/apps/conversion/tmp/Generalized%20Compressibility%20Figures.pptxhttp://localhost/var/www/apps/conversion/tmp/Generalized%20Compressibility%20Figures.pptxhttp://localhost/var/www/apps/conversion/tmp/Generalized%20Compressibility%20Figures.pptx
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    12Sec 3.11.4 : Equations of State & Sec 3.12 : Ideal Gas Model

    Ideal Gas pv RT

    Equations of State: Relate the state variables T, p, V

    Alternate Expressions pV mRT

    pv mRT

    When the gas follows the ideal gas law,Z = 1p > T c

    T uu and h h T u T pv u T RT

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    13Sec 3.11.4 : Equations of State & Sec 3.12 : Ideal Gas Model

    Ideal Gas pv RT

    Equations of State: Relate the state variables T, P, V

    Van der Waals 2

    2

    n a p V nb nRT

    V

    a attraction between particles

    b volume of particles

    Redlich Kwong

    Peng-Robinson

    m m m

    RT a p

    V b TV V b

    2 22m m m

    RT a p

    V b V bV b

    virial 2 31 ..... Z B T p C T p D T p

    .....1 32 v

    T Dv

    T C vT B

    Z

    B Two molecule interactions C Three molecule interactions

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    14

    Example: (3.105) A tank contains 10 lb of air at 70F with a pressure of 30 psi. Determine the volume of the air, in ft 3. Verify that ideal gasbehavior can be assumed for air under these conditions.

    m = 10 lbT = 70Fp = 30 psi

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    15

    Example: (3.105) Determine the volume of the air, in ft 3. Verify thatideal gas behavior can be assumed for air under these conditions.

    Sec 3.12 : Ideal Gas

    m = 10 lbT = 70F = 530Rp = 30 psi= 2.04 atm

    For Air, (Table A-1E, p 864)Tc = 239 R and p c = 37.2 atm

    2.04 0.05537.2

    5302.22

    239

    RC

    RC

    p p p

    T T

    T

    Z= 1.0 (Figure A-1)

    pv pV Z RT mRT

    2

    2 2

    1

    3

    144

    1545 28.97(10 )(1.0) / 53065.4

    (30 )

    f mol

    mol m

    f

    ft lb

    lb R

    lbm lb

    lb inin ft

    lb RV ft

    ViewCompressibility Figure

    R

    M mZ T mZRT V p p

    http://localhost/var/www/apps/conversion/tmp/Generalized%20Compressibility%20Figures.pptxhttp://localhost/var/www/apps/conversion/tmp/Generalized%20Compressibility%20Figures.pptxhttp://localhost/var/www/apps/conversion/tmp/Generalized%20Compressibility%20Figures.pptx
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    16

    Example 3:Nitrogen gas is originally at p = 200 atm, T = 252.4 K.It is cooled at constant volume to T = 189.3 K.What is the pressure at the lower temperature?

    SOLUTION:From Table A-1 for Nitrogen p cr = 33.5 atm, T cr = 126.2 K

    At State 1, p r,1 = 200/33.5 = 5.97 and T r,1 = 252.4/126.2 = 2.

    According to compressibility factor chart , Z = 0.95 v r' = 0.34.

    Following the constant v r' line until it intersects with the line atTr,2 = 189.3/126.2 = 1.5

    gives

    Pr,2 = 3.55.

    Thus P 2 = 3.55 x 33.5 = 119 atm.

    Since the chart shows Z drops down to around 0.8 at State 2, so it would notbe appropriate to treat it as an ideal gas law for this model.

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    End of Slides for Lecture 09

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