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Each point on a constant pressure curve corresponds to a certain temperature. Increasing the temperature, the liquid density decreases. A comparison between experimental and calculated densities using SAFT equation are presented in figures 7-10 versus pressure for different temperatures. 143%. 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.
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.
Bai 95# oil well localizes in the west slope of the basin, the other are in the south to the basin. The earth 48 Advances in Chemical Engineering strata belong to middle to shallow, upper Cretaceous Period. The thickness of inclusion thin slide is about 150 nm. Table 1 shows the information about the strata, depths, GOIs, average homogeneous temperatures ( Th s ) and salinities of the sand rocks. There are two episodes OGIs in these samples. The first episode is in the earlier stage of quartz overgrowth, the second in the later stage of the quartz overgrowth.