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PDF] Two Simple yet Accurate Equations for Calculating the Fugacity Coefficient Phi and the Gas Compressibility Factor

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PDF] Two Simple yet Accurate Equations for Calculating the Fugacity  Coefficient Phi and the Gas Compressibility Factor

Two Simple yet Accurate Equations for Calculating the Fugacity Coefficient Phi and the Gas Compressibility Factor Z . by A.E. for mychemengmusings.wordpress.com In this post two new powerful equations are presented one for the Gas Compressibility Factor ‘Z’ and one for the Gas Fugacity Coefficient ‘phi’. Both give excellent prediction results for the sub-critical reduced pressure region and superheated vapor region. These two equations are surprisingly simple, allow direct calculation without the need for iterations hence easy to implement in spreadsheets or used on handheld devices and calculators! The two form a thermodynamically consistent pair. Three Charts have been prepared mapping out the predictions made with these equations. Numerical calculation examples are given including for superheated Steam, Ethane, Propane and Propylene. The basis for each of these equations is presented in Part III of this post giving ample attention to the basis on which these equations rest and their validation against measured data.

PDF) Calculating the vapor-liquid phase equilibrium for multicomponent  systems using the Soave-Redlich-Kwong equation

PDF) Calculating the vapor-liquid phase equilibrium for multicomponent systems using the Soave-Redlich-Kwong equation

Fugacity and Fugacity Coeff, PDF, Materials Science

Fugacity and Fugacity Coeff, PDF, Materials Science

Compressibility factor - Wikipedia

Compressibility factor - Wikipedia

The 'Lewis line': A proposed new ideal curve of fluids - ScienceDirect

The 'Lewis line': A proposed new ideal curve of fluids - ScienceDirect

Fugacity Coefficient Phi vs Pr Chart

Fugacity Coefficient Phi vs Pr Chart

A compositional model for CO2 flooding including CO2 equilibria between  water and oil using the Peng–Robinson equation of state with the  Wong–Sandler mixing rule

A compositional model for CO2 flooding including CO2 equilibria between water and oil using the Peng–Robinson equation of state with the Wong–Sandler mixing rule

Comparison of pure component thermodynamic properties from CHEMCAD with  direct calculation using the Peng-Robinson equation of state - ScienceDirect

Comparison of pure component thermodynamic properties from CHEMCAD with direct calculation using the Peng-Robinson equation of state - ScienceDirect

Compressibility Factor Z for sub-critical pressures for Lee-Kesler's “Simple,  Normal Fluids” Z-LK with a new set of equations for Excel Spreadsheets

Compressibility Factor Z for sub-critical pressures for Lee-Kesler's “Simple, Normal Fluids” Z-LK with a new set of equations for Excel Spreadsheets

Virial Equation - an overview

Virial Equation - an overview

Functional-Segment Activity Coefficient Equation of State: F-SAC-Phi

Functional-Segment Activity Coefficient Equation of State: F-SAC-Phi

Solved 3. (a) Explain the concepts of fugacity and fugacity

Solved 3. (a) Explain the concepts of fugacity and fugacity

Why is fugacity, or z, always less than 1? - Quora

Why is fugacity, or z, always less than 1? - Quora