Title of article :
Some useful expressions for deriving component fugacity coefficients from mixture fugacity coefficient
Author/Authors :
Hu، نويسنده , , Jiawen and Wang، نويسنده , , Rong-Rong Mao، نويسنده , , Shide، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2008
Pages :
7
From page :
7
To page :
13
Abstract :
It is proved that the fugacity coefficient (ϕ) of a mixture and the fugacity coefficient of component i ( ϕ ˆ i ) follow the relation ln   ϕ ˆ i = ∂ ( n ln   ϕ ) / ∂ n i T , P , n j ( j ≠ i ) , = ∂ ( n ln   ϕ ) / ∂ n i T , P , V t , n j ( j ≠ i ) , where ni is the amount-of-substance of component i, and T, P, Vt and n are the temperature, pressure, total volume and total amount-of-substance of the system, respectively. This relation is very useful for the derivation of ϕ ˆ i . It allows the ϕ function to contain both P and V, so ϕ can be expressed with various equations of state (either volume-explicit or pressure-explicit). This approach can also use the similarity of the ϕ expressions of pure fluids and mixtures to simplify the derivation of ϕ ˆ i . Besides, ϕ ˆ i can also be directly derived from equation of state through a variation of the approach above. These approaches are much easier than the commonly used ones when the equation of state for fluids is complex.
Keywords :
Mixture fugacity coefficient , Component fugacity coefficient , equation of state , Pressure-explicit , Volume-explicit
Journal title :
Fluid Phase Equilibria
Serial Year :
2008
Journal title :
Fluid Phase Equilibria
Record number :
1986979
Link To Document :
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