Real gas

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Real gases – as opposed to a perfect or ideal gas – exhibit properties that cannot be explained entirely using the ideal gas law. To understand the behaviour of real gases, the following must be taken into account:

For most applications, such a detailed analysis is unnecessary, and the ideal gas approximation can be used with reasonable accuracy. On the other hand, real-gas models have to be used near the condensation point of gases, near critical points, at very high pressures, to explain the Joule–Thomson effect and in other less usual cases.

Models[edit]

Isotherms of real gas (sketchy)

Dark blue curves – isotherms below the critical temperature. Green sections – metastable states.

The section to the left of point F – normal liquid.
Point F – boiling point.
Line FG – equilibrium of liquid and gaseous phases.
Section FA – superheated liquid.
Section F′A – stretched liquid (p<0).
Section AC – analytic continuation of isotherm, physically impossible.
Section CG – supercooled vapor.
Point G – dew point.
The plot to the right of point G – normal gas.
Areas FAB and GCB are equal.

Red curve – Critical isotherm.
Point K – critical point.

Light blue curves – supercritical isotherms
Main article: Equation of state

van der Waals model[edit]

Real gases are often modeled by taking into account their molar weight and molar volume

RT=\left(P+\frac{a}{V_m^2}\right)(V_m-b)

Where P is the pressure, T is the temperature, R the ideal gas constant, and Vm the molar volume. a and b are parameters that are determined empirically for each gas, but are sometimes estimated from their critical temperature (Tc) and critical pressure (Pc) using these relations:

a=\frac{27R^2T_c^2}{64P_c}
b=\frac{RT_c}{8P_c}

Redlich–Kwong model[edit]

The Redlich–Kwong equation is another two-parameter equation that is used to model real gases. It is almost always more accurate than the van der Waals equation, and often more accurate than some equations with more than two parameters. The equation is

RT=P(V_m-b)+\frac{a}{V_m(V_m+b)T^\frac{1}{2}}(V_m-b)

where a and b two empirical parameters that are not the same parameters as in the van der Waals equation. These parameters can be determined:

a=0.4275\frac{R^2T_c^{2.5}}{P_c}

b=0.0867\frac{RT_c}{P_c}

Berthelot and modified Berthelot model[edit]

The Berthelot equation (named after D. Berthelot[1] is very rarely used,

P=\frac{RT}{V_m-b}-\frac{a}{TV_m^2}

but the modified version is somewhat more accurate

P=\frac{RT}{V_m}\left[1+\frac{9P/P_c}{128T/T_c}\left(1-\frac{6}{(T/T_c)^2}\right)\right]

Dieterici model[edit]

This model (named after C. Dieterici[2]) fell out of usage in recent years

P=RT\frac{\exp{(\frac{-a}{V_mRT})}}{V_m-b}.

Clausius model[edit]

The Clausius equation (named after Rudolf Clausius) is a very simple three-parameter equation used to model gases.

RT=\left(P+\frac{a}{T(V_m+c)^2}\right)(V_m-b)

where

a=\frac{27R^2T_c^3}{64P_c}

b=V_c-\frac{RT_c}{4P_c}

c=\frac{3RT_c}{8P_c}-V_c

where Vc is critical volume.

Virial model[edit]

The Virial equation derives from a perturbative treatment of statistical mechanics.

PV_m=RT\left(1+\frac{B(T)}{V_m}+\frac{C(T)}{V_m^2}+\frac{D(T)}{V_m^3}+...\right)

or alternatively

PV_m=RT\left(1+\frac{B^\prime(T)}{P}+\frac{C^\prime(T)}{P^2}+\frac{D^\prime(T)}{P^3}+...\right)

where A, B, C, A′, B′, and C′ are temperature dependent constants.

Peng–Robinson model[edit]

Peng–Robinson equation of state (named after D.-Y. Peng and D. B. Robinson[3]) has the interesting property being useful in modeling some liquids as well as real gases.

P=\frac{RT}{V_m-b}-\frac{a(T)}{V_m(V_m+b)+b(V_m-b)}

Wohl model[edit]

The Wohl equation (named after A. Wohl[4]) is formulated in terms of critical values, making it useful when real gas constants are not available.

RT=\left(P+\frac{a}{TV_m(V_m-b)}-\frac{c}{T^2V_m^3}\right)(V_m-b)

where

a=6P_cT_cV_c^2

b=\frac{V_c}{4}

c=4P_cT_c^2V_c^3.

Beattie–Bridgman model[edit]

[5]

This equation is based on five experimentally determined constants. It is expressed as

P=\frac{RT}{v^2}\left(1-\frac{c}{vT^3}\right)(v+B)-\frac{A}{v^2}

where

A = A_0 \left(1 - \frac{a}{v} \right)
B = B_0 \left(1 - \frac{b}{v} \right)

This equation is known to be reasonably accurate for densities up to about 0.8 ρcr, where ρcr is the density of the substance at its critical point. The constants appearing in the above equation are available in following table when P is in KPa, v is in \frac{m^3}{Kmol}, T is in K and R=8.314\frac{kPa.m^3}{Kmol.K}[6]

Gas A0 a B0 b c
Air 131.8441 0.01931 0.04611 -0.001101 4.34×10^4
Argon, Ar 130.7802 0.02328 0.03931 0.0 5.99×10^4
Carbon Dioxide, CO2 507.2836 0.07132 0.10476 0.07235 6.60×10^5
Helium, He 2.1886 0.05984 0.01400 0.0 40
Hydrogen, H2 20.0117 -0.00506 0.02096 -0.04359 504
Nitrogen, N2 136.2315 0.02617 0.05046 -0.00691 4.20×10^4
Oxygen, O2 151.0857 0.02562 0.04624 0.004208 4.80×10^4

Benedict–Webb–Rubin model[edit]

The BWR equation, sometimes referred to as the BWRS equation,

P=RTd+d^2\left(RT(B+bd)-(A+ad-a{\alpha}d^4)-\frac{1}{T^2}[C-cd(1+{\gamma}d^2)\exp(-{\gamma}d^2)]\right)

where d is the molar density and where a, b, c, A, B, C, α, and γ are empirical constants. Note that the γ constant is a derivative of constant α and therefore almost identical to 1.

See also[edit]

References[edit]

  1. ^ D. Berthelot in Travaux et Mémoires du Bureau international des Poids et Mesures – Tome XIII (Paris: Gauthier-Villars, 1907)
  2. ^ C. Dieterici, Ann. Phys. Chem. Wiedemanns Ann. 69, 685 (1899)
  3. ^ Peng, D. Y., and Robinson, D. B. (1976). "A New Two-Constant Equation of State". Industrial and Engineering Chemistry: Fundamentals 15: 59–64. doi:10.1021/i160057a011. 
  4. ^ A. Wohl "Investigation of the condition equation", Zeitschrift für Physikalische Chemie (Leipzig) 87 pp. 1–39 (1914)
  5. ^ Yunus A. Cengel and Michael A. Boles, Thermodynamics: An Engineering Approach 7th Edition, McGraw-Hill, 2010, ISBN 007-352932-X
  6. ^ Gordan J. Van Wylen and Richard E. Sonntage, Fundamental of Classical Thermodynamics, 3rd ed, New York, John Wiley & Sons, 1986 P46 table 3.3

External links[edit]