Abstract A new correlation for the compressibility of sweet and sour natural gases ispresented. This correlation is derived from an equation of state whichadequately represents the Standing-Katz Z-Factor chart. The algebraicexpression for compressibility presented here is suitable for computercalculations. A FORTRAN subroutine to perform this computation is alsopresented, along with a graphical form of the correlation. INTRODUCTION IN THE PRESSURE ANALYSIS of transient or pseudo-steady-state flow Dataacquired during gas well testing, a knowledge of the variation of fluidcompressibility with pressure and temperature is essential. For liquid flow, the compressibility is small and is usually assumed to be constant. For gasflow, the compressibility is neither valid nor necessary of a real gas can becomputed readily. Trube (1957) has presented graphs from which the compressibility of natural gases may be obtained. This correlation is, however, difficult to usein a computer program. Recent developments have made possible a more consistentand convenient approach. The purpose of this paper, therefore, is to present An analytical technique forcalculating the compressibility of natural gases. The procedure may be readilycomputerized and was used to generate curves of pseudo-reduced compressibility, which are useful for manual calculations. Theory (Equation in full paper) Graphical Presentation The computer subroutines mentioned above were used to generate cr as a function of Pr and Tr. Figure 1 is aplot of c r versus pr for various values of Tr. In this figure, the curves are too close together for easy andunambiguous reading. In order to increase the separation of the isotherms, especially for the low-pr range, c r T r wasgenerated and plotted versus Pr for various values of Tr as shown in Figures 2 and 3. The separation between the isothermsin these figures is sufficient to make them easy to read and hence suitable forreasonably accurate manual calculations of compressibility. Sour Gases The correlation developed for c r in terms of (aZapr) and the graphical representation of cr Trare applicable to sour as well as sweet natural gases. A simple method has beendeveloped by Wichert and Aziz (1972) to account for the presence of H.S and CO2 in the use of the Standing-Katz Z-Factor chart. Inthis method, the pseudo-critical properties of a sour gas are adjusted togive: (Equation in full paper) The calculation procedures are then exactly the same as discussed previously, except that T12 and p1c must beused instead of T2 and po respectively. Discussion Figure 4 compares some of the isotherms for reduced compressibilitydeveloped by Trube (1957) with corresponding isotherms from Figure 1 Thedifference between the two methods is no doubt due to the different techniquesutilized to obtain Z and (aZ/a2r)Tr. Trube used the Standing-Katz Z-Factor chart re- produced by Brown et al.(1948, p.38) to obtain values of Z and (aZ/apr)substituted thesevalues into Equation (4), and calculated c, as a function of pr and Tr.
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