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By Z. Nawaz, et. al.

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390. M. W. (2004). Thermodynamics of Fluid-Phase Equilibria for Standard Chemical Engineering Operations. , Vol. 4, pp. 739–761. Redlich, O. S. (1949). On the Thermodynamics of Solutions. V. An Equation of Sate. Fugacities of Gaseous Solutions. Chem. , Vol. 44, pp. 233–244. S. P. (1997). Modeling of Live Oil Asphaltene, Precipitation Proceedings of AIChE Spring Meeting, Houston, March 9-13, 1997. ; Llovell, F. F. (2008). An Accurate Direct Technique for Parameterizing Cubic Equations of State. Part II.

Figure 11 represents relative deviations for different mixtures of ethanol and toluene on a 3D diagram. Fig. 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.

1998, 2000). The superiors of the above FMP are simple and low cost. But there are still some shortcomings. The first is one can only gain visible spectra (400-780 nm) for the exciting light is at 365nm. But some aromatic hydrocarbons emit UV fluorescence which can not be measured by above method. 15 mm) to limit the incident light spot often larger than the under studied OGI. Not only the under studied OGI emits fluorescence, but also other OGIs, the cements around the mineral grain trapping the OGI and even the mineral grain itself.

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