Article ID Journal Published Year Pages File Type
204266 Fluid Phase Equilibria 2012 12 Pages PDF
Abstract

At pressures below ∼55 MPa, the perturbed chain – statistically associated fluid theory (PC-SAFT) gives reliable density predictions within ±2% for n-alkanes and other hydrocarbons. However, PC-SAFT tends to over-predict density values by as much as 5% at higher pressures, particularly for normal and branched alkanes. For many compounds, literature values for the three pure-component PC-SAFT parameters m, σ, and ɛ/kB are typically obtained by fitting the equation to sub-critical PρT data or occasionally both sub-critical and supercritical density data. A new set of pure-component PC-SAFT parameters for density prediction at extreme conditions is reported here by fitting the PC-SAFT equation to single-component density data collected at temperatures from ambient to 533 K and pressures from ∼6.9 to 276 MPa, rather than sub-critical density data since these high temperature, high pressure (HTHP) conditions are similar to conditions typically associated with petroleum recovery from ultra-deep formations. Density predictions made using the new, HTHP PC-SAFT pure-component parameters at HTHP conditions are clearly superior to those obtained using the original PC-SAFT parameters. Although a correction term can be applied to the ɛ/kB parameter to make HTHP PC-SAFT pure-component density predictions at pressures below 6.9 MPa only slightly inferior to predictions with the original PC-SAFT parameters, vapor–liquid equilibrium predictions with the original PC-SAFT parameters are clearly superior to predictions made with the HTHP parameters. Correlations are developed to accurately predict the HTHP PC-SAFT parameters for normal and branched alkanes for which there are either incomplete or nonexistent experimental density data sets.

► Original PC-SAFT equation overpredicts hydrocarbon densities by up to 5% at 276 MPa. ► The equation was fit to experimental density data at pressures to 276 MPa. ► New PC-SAFT parameters presented for hydrocarbons up to carbon number 40. ► Resulting density predictions differ by <±1% from exp. values between 6.9 and 276 MPa. ► Applications in engineering of ultra-deep petroleum reservoirs.

Related Topics
Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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