Equation of State Real Gas Relationships. Relates PVT properties of a pure substance/mixture via...
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![Page 1: Equation of State Real Gas Relationships. Relates PVT properties of a pure substance/mixture via Theoratical and empirical relations Source of information:](https://reader036.fdocuments.in/reader036/viewer/2022072117/56649f395503460f94c5583f/html5/thumbnails/1.jpg)
Equation of State
Real Gas Relationships
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• Relates PVT properties of a pure substance/mixture via Theoratical and empirical relations
• Source of information: computer databases• Effective Eq. of state: experimental data with
good precision
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Van-der Waals Equation• Simple, explains computational
problems.• Also illustrates Theoretical
developments
• Fortan computer Programs for non linear equations
• One Code: Newton Method, Other Minimization
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Critical Temperature and Pressure
• The highest temperature at which a species can coexist in two phases (liquid vapor) is the critical temperature of that species, Tc, and the corresponding pressure is the critical pressure, Pc.
• A substance at Tc and Pc is said to be at its critical state.• A vapor is a gaseous species below its critical temperature, and a gas
is a species above its critical temperature at a pressure low enough for the species to be more like a vapor than a liquid (i.e., a density closer to 1 g/L than 1000 g/L).
• Substances at temperatures above Tc and pressures above Pc are referred to as supercritical fluids.
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Cubic Equation of State
• Fit the experimental data with as few constants in equation as possible
• Concise summary of a large of experimental data• Accurate interpolation between experimental data
points• Provide a continuous function to facilitate
calculation of physical properties involving differentiation and integration.
• Point of departure for the treatment of thermodynamic properties of mixtures.
![Page 8: Equation of State Real Gas Relationships. Relates PVT properties of a pure substance/mixture via Theoratical and empirical relations Source of information:](https://reader036.fdocuments.in/reader036/viewer/2022072117/56649f395503460f94c5583f/html5/thumbnails/8.jpg)
Virial Equation of state• A virial equation of state expresses the quantity PV/
RT as a power series in the inverse of specific volume:
• B, C, and D are functions of temperature …known as the second, third, and fourth virial coefficients,
• Theoretical basis in statistical mechanics • procedures for estimating the coefficients are not well
developed, those beyond B.• The ideal gas equation of state is obtained if B=C=D…
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• For polar compounds (asymmetrical compounds with a nonzero dipole moment, such as water).
• Can estimate V or P for a given T for a nonpolar species (one with a dipole moment close to zero, such as hydrogen and oxygen and all other molecularly symmetrical compounds).
• Solution for P is straightforward. • For V, the equation can be rearranged into a quadratic and
solved using the quadratic formula. • One of the two solutions is reasonable and the other is not
and should be discarded; • if there is any doubt, estimate V from the ideal gas equation
of state and accept the virial equation solution that comes closest to V ideal'
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Steps Involved
• Look up the critical temperature and pressure (Tc and Pc) for the species of interest
• Pitzer acentric factor, w. a parameter that reflects the geometry and polarity of a molecule.
• Calculate the reduced temperature, Tr = TITc.• Estimate B using the following equations
• Substitute into Equation the values of B and whichever of the variables P and V is known and solve for the other variable
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Cubic equations ofstate (SRK)
• Empirical but have proved remarkably robust in describing a 'Wide variety of systems.
• SRK equation of state is• Empirical functions of critical temperature and
Pressure
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Correlations
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Calculating volume
By Spreadsheet Software data
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Considerations
• SRK equation of state (and every other equation of state) is itself an
• approximation.• All equations of state have parameters obtained by fitting
empirical expressions to experimental PVT data. • The fit may be excellent in the temperature and pressure ranges
where the data were obtained but may be terrible elsewhere. • Always try to ascertain the region of validity of any equation of
state intend to be used. • No assurance of the accuracy of the equation for condition far
from acceptable region.