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Empirical correction to the Peng–Robinson equation of state for the saturated region
Institution:1. Department of Chemical Engineering, School of Chemical and Petroleum Engineering, Shiraz University, Shiraz 71345, Iran;2. Gas Center of Excellence, Shiraz University, Shiraz 71345, Iran;1. Texas A&M University, College Station, TX 77843, United States of America;2. University of Maryland, Center for Environmental Science, Cambridge, MD 21613, United States of America;3. New Jersey Institute of Technology, Newark, NJ 07102;4. ExxonMobil Biomedical Sciences, Inc., Spring, TX 77339, United States of America;5. Massachusetts Institute of Technology, Cambridge, MA 02139, United States of America
Abstract:This work presents an empirical correction to improve the Peng–Robinson equation of state (PR EOS) for representing the densities of pure liquids and liquid mixtures in the saturated region using the volume translation method. A temperature-dependent volume correction is employed to improve the original PR EOS so that it can match the true critical point of pure fluids. The volume correction is generalized as a function of the critical parameters and the reduced temperature. The volume translation PR (VTPR) EOS with the generalized volume correction accurately represents the saturated liquid densities for different polar and non-polar fluids, including alkanes, cycloparaffins, halogenated hydrocarbons, olefins, cyclic olefins, aromatics and inorganic molecules. The average relative deviations for 91 pure compounds was 1.37%. The generalized VTPR EOS was also used to predict the saturated liquid density of 53 binary mixtures with a relative deviation of 0.98%. The generalized VTPR EOS can also be extended to other materials. The accuracy of the generalized VTPR EOS compares well with other methods and equations of state.
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