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Numer. , Vol. 56, No. 8, pp. 1077–1091. Buenrostro-Gonzales, E. & Lira-Galeana, C. (2004). Asphaltene Precipitation in Crude Oils, Ttheory and Experiments. , Vol. 50, pp. 2552-2570. D. C. (1981). Numerical analysis (Second Edition), Prindle, Weber & Schmidt, Boston. E. R. (1990). Measurement and Modeling of Asphaltene Precipitation. J. , Vol. 1440. Chaback JJ. (1991). Discussion on Measurement and Modeling of Asphaltene Precipitation. Journal of Petroleum Technology. Vol. 43, pp. 1519-1520. ; Jackson, G.

6. Contributions to Z-factor of ethanol at different pressures and temperatures according to SAFT EoS. Application of Chebyshev Polynomials to Calculate Density and Fugacity Using SAFT Equation of State to Predict Asphaltene Precipitation Conditions 29 Fig. 7. 0 mole% of ethanol. Fig. 8. 5 mole% of ethanol. 30 Advances in Chemical Engineering Fig. 9. 5 mole% of ethanol. Fig. 10. 0 mole% of ethanol. Application of Chebyshev Polynomials to Calculate Density and Fugacity Using SAFT Equation of State to Predict Asphaltene Precipitation Conditions 31 Fig.

Conclusion In this study a model based on statistical association fluid theory (SAFT) has been developed to predict phase behavior of hydrocarbon systems containing asphaltene and associating components. A robust, fast and accurate method based on Chebyshev polynomial approximation was proposed to find density using SAFT EoS which plays an important role in the calculation of the fugacity coefficients. The model was first evaluated using binary systems of ethanol and toluene. A good agreement between experimental and calculated liquid densities at different pressures, temperatures and compositions was obtained.

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