Fugacity expressions for pure gases
Fugacity coefficient (and hence fugacity) of pure gases may be conveniently evaluated by applying eqn. 6.80 to a volume-explicit equation of state. The truncated virial EOS is an example of the latter type, for which the compressibility factor of pure species (i) is given by:
Thus, on using eqn. 6.80:
Hence, ...(6.98)
Derivation of fugacity coefficient expression for cubic EOS: Starting from eqn. 5.38:
...(6.99)
...(6.100)
Using Eqn. 6.100 in 6.99:
On simplifying:
...(6.101)
Here: V∞ = molar volume at P → 0, orV∞ = ideal gas volume
Therefore: V / V∞ = Z ...(6.102)
Using eqn. 6.102 in 6.101 one arrives at:
...(6.103)
Equation 6.103 is a generalized expression for obtaining pure component fugacity from a pressure explicit EOS. We show below the expressions for fugacity coefficients that derive on application of the above equation to various cubic EOSs. (The reader may refer to section 2.3.3 for various forms of cubic
EOS).
VdW EOS:
...(6.104)
RK-EOS:
...(6.105)
SRK EOS:
...(6.106)
PR-EOS:
...(6.107)
1. What is fugacity and why is it important in civil engineering? |
2. How is fugacity different from pressure in civil engineering applications? |
3. Can fugacity be directly measured in civil engineering projects? |
4. How does fugacity affect the design of ventilation systems in buildings? |
5. Are fugacity calculations only relevant for air pollutants in civil engineering? |
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