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are crucial for understanding real gas behavior. They measure how actual gases deviate from ideal gas models, helping engineers predict and analyze real-world systems more accurately.

and are key concepts in this topic. They provide practical tools for calculating properties of , essential for designing and optimizing processes in industries like chemical engineering and HVAC.

Residual Properties

Relationship between Residual Properties and Ideal Gas State

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  • Residual properties quantify the deviation of a real gas from the behavior of an ideal gas at the same temperature and pressure
  • Calculated by subtracting the property value for an ideal gas from the actual property value of the real gas
  • serves as a reference point for comparing the behavior of real gases
    • In an ideal gas, molecules have no intermolecular forces and occupy negligible volume
    • Real gases deviate from ideal gas behavior due to intermolecular interactions and finite molecular volume

Residual Gibbs Free Energy, Enthalpy, and Entropy

  • (GRG^R) represents the difference between the actual Gibbs free energy of a real gas and that of an ideal gas at the same temperature and pressure
    • Quantifies the non-ideality of a gas in terms of Gibbs free energy
    • Positive GRG^R indicates a higher Gibbs free energy than an ideal gas, while negative GRG^R indicates a lower Gibbs free energy
  • (HRH^R) is the difference between the actual enthalpy of a real gas and that of an ideal gas at the same temperature and pressure
    • Measures the additional enthalpy due to intermolecular interactions in a real gas
    • Positive HRH^R indicates higher enthalpy than an ideal gas, while negative HRH^R indicates lower enthalpy
  • (SRS^R) represents the difference between the actual entropy of a real gas and that of an ideal gas at the same temperature and pressure
    • Quantifies the entropy change associated with the non-ideality of a gas
    • Negative SRS^R indicates a lower entropy than an ideal gas, while positive SRS^R indicates a higher entropy (less common)

Departure Functions and Their Applications

  • express the difference between the actual property value of a real gas and that of an ideal gas at the same temperature and pressure
    • Denoted by the superscript "D" (e.g., GDG^D, HDH^D, SDS^D)
    • Related to residual properties: GD=GRG^D = G^R, HD=HRH^D = H^R, SD=SRS^D = S^R
  • Departure functions are useful for estimating the properties of real gases when direct experimental data is unavailable
    • Can be calculated using equations of state (EOS) or generalized correlations
    • Example: can be used to calculate departure functions for hydrocarbons and their mixtures
  • Departure functions find applications in , equipment sizing, and thermodynamic analysis of real gas systems
    • Example: Calculating the required compressor power for a natural gas pipeline considering the non-ideal behavior of the gas

Fugacity and Compressibility

Fugacity and Fugacity Coefficient

  • Fugacity (ff) is a thermodynamic property that represents the effective pressure of a real gas, accounting for its non-ideal behavior
    • Has units of pressure (e.g., Pa, bar)
    • For an ideal gas, fugacity equals the actual pressure
    • For a real gas, fugacity can be higher or lower than the actual pressure, depending on the gas and the conditions
  • (ϕ\phi) is the ratio of a gas's fugacity to its actual pressure at a given temperature and pressure
    • Dimensionless quantity
    • For an ideal gas, ϕ=1\phi = 1
    • For a real gas, ϕ\phi can be greater than or less than 1, indicating positive or negative deviations from ideal behavior
  • Fugacity and fugacity coefficient are related by: f=ϕPf = \phi P
    • PP is the actual pressure of the gas
    • Fugacity coefficient can be calculated using equations of state or experimentally measured

Compressibility Factor and Its Relation to Fugacity

  • Compressibility factor (ZZ) is the ratio of the actual volume of a gas to the volume it would occupy if it behaved as an ideal gas at the same temperature and pressure
    • Dimensionless quantity
    • For an ideal gas, Z=1Z = 1
    • For a real gas, ZZ can be greater than or less than 1, indicating positive or negative deviations from ideal behavior
  • Compressibility factor is related to the fugacity coefficient by: lnϕ=0PZ1PdP\ln \phi = \int_0^P \frac{Z-1}{P} dP
    • This relationship allows the calculation of fugacity coefficient from compressibility factor data
    • Example: Using the virial equation of state to express ZZ as a function of pressure and calculating ϕ\phi by integration
  • Compressibility factor is used to characterize the behavior of real gases and to estimate their properties
    • Can be obtained from experimental data (e.g., PVT measurements) or calculated using equations of state
    • (e.g., Nelson-Obert charts) provide ZZ values for various gases as a function of reduced temperature and pressure
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© 2024 Fiveable Inc. All rights reserved.
AP® and SAT® are trademarks registered by the College Board, which is not affiliated with, and does not endorse this website.

© 2024 Fiveable Inc. All rights reserved.
AP® and SAT® are trademarks registered by the College Board, which is not affiliated with, and does not endorse this website.
Glossary
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