A fixed reduction of all binary interaction coefficients may be a simple practical step to predict phase behavior of complex reservoir fluids. Summary Phase behavior prediction by an equation of state in the near-critical region shows extreme sensitivity to the binary interaction coefficients. For binary mixtures, these coefficients have a systematic decreasing trend as the critical point is approached. Such a trend can be used to calculate the phase behavior of binary mixtures in the critical region. For complex near-critical reservoir fluids, a variable interaction coefficient may not provide satisfactory results. A fixed reduction of the binary interaction coefficients is a simple practical step towards EOS prediction of phase behavior of complex reservoir fluids. Introduction A sizable number of gas condensate and volatile oil reservoirs contain fluids which are near the critical point. Closeness to the critical condition strongly affects the reservoir performance. As an example, GOR production of volatile oil reservoirs increases rapidly below the bubble point pressure. The intensity of the rise in GOR depends on the distance to the critical point. Compositional grading is also pronounced in retrograde condensate and other reservoirs containing near-critical fluids. Equations of state (EOS) are often used to study near-critical reservoir fluids and to carry out compositional simulation. A major deficiency of these equations is their inability to predict reliable vapor liquid equilibrium (VLE) in the critical region. The current industry practice is to adjust several parameters of the EOS to make up for this deficiency. Adjustment of some parameters could be interpreted as changing the critical properties of selected components. The process of tuning is also time consuming and depends on the level of the experience of the user. Tuning when based on VLE data (i.e., bubble point), could be detrimental to volumetric productions. Therefore, both the phase and volumetric data are regressed (adjustment if limited to the interaction coefficients alone, may not require inclusion of volumetric data). Various efforts have been made to improve prediction capability of the popular EOS. These include the move from two-constant to three-constant equations to achieve volumetric calculation accuracy enhancement. Phase behavior of reservoir fluids in the near-critical region is mainly related to VLE prediction capability and, therefore, improvement in volumetric prediction often does not have a significant effect. Besides the line of attack by Coats and Smart who tuned " ", and " " parameters of selected components, as well as selected binary interaction coefficients. Slot-Peterson proposed a different approach. In a study to compute the phase behavior of near-critical reservoir fluids, he concluded that adjustment of various binary interaction coefficients were crucial. Slot-Peterson outlined a systematic approach to obtain various binary-interaction coefficients. In his approach, the binary interaction coefficients of the same pair varied from one reservoir fluid to another. They were also different from the values obtained from the binary VLE data. Slot-Peterson concluded that a large amount of laboratory data (including constant composition expansion, differential liberation, or constant-volume depletion) are crucial to determine the proper binary interaction coefficients for near-critical reservoir fluids. The above short review of the literature shows the desirability of a more predictive capability for the equations of state. In a recent paper, we have demonstrated that near-critical phase behavior prediction of binary and ternary hydrocarbon mixtures follows a systematic decreasing trend as the critical point is approached (at constant temperature). Accounting of the variation of the interaction coefficient is apparently key to near-critical phase behavior prediction. In Ref. 5, we proposed to relate the variation of the interaction coefficient to a distance parameter to the critical point. The dimensionless bulk modulus (related to the inverse of the isothermal compressibility) defined by (Equation 1) was used as the distance parameter. It was shown that " " has the desirable characteristics for linkage to the interaction coefficient. We, then, proposed a functional form for the variation of the interaction coefficient in the form of (Equation 2) where and are constants. Fugacity relations for the Peng Robinson EOS (PR-EOS) based on Eq. 2 were derived. The model (with = 15) was applied to a number of binary and ternary mixtures. The results showed significant improvement in the critical region over the conventional PR-EOS. In this paper, further testing for three binary hydrocarbon systems of C1/n C9, C1/n C20, and C1/n C24, and selected CO2/n-alkanes and N2/n-alkanes systems will be made. The major goal of the paper is, however, to examine the use of the variable interaction coefficient approach (given by Eq. 2) for near-critical reservoir fluids phase behavior prediction by an EOS. Use of an EOS for reservoir fluids and even, simple mixtures requires critical property data. These data are subject to uncertainty. In the following, the reliability of critical data are discussed first. Critical Properties Measured Critical properties of the normal alkanes and isomeric alkanols are available only to normal octadecane (n C18) and (C12), respectively. Estimation of the critical properties for heavier hydrocarbons are from correlations. Four such correlations which are commonly used will be examined. The input to all of these correlations are boiling point temperature (Tb) and specific gravity (Sg). The empirical relations of Lee and Kesler are based on the 3-parameter corresponding states principle. The correlations of Riazi and Daubert for estimation of a critical property are in the simple form of in which the primed parameters are the correlation constants. The empirical relations of Twu...