On the extrapolation behavior of empirical equations of state

Generally, the extrapolation behavior of empirical equations of state is regarded as poor, but it can be shown that state-of-the-art equations of state yield reliable results well beyond the range where they were fitted to experimental data. During the past years a new generation of highly accurate equations of state which yield reasonable results even up to the limits of chemical stability of the considered substances has been developed. In this paper, the positive influence of recent methods for the development of equations of state on their extrapolation behavior is discussed. The influence of the mathematical structure on the extrapolation characteristics is analyzed and requirements for a reasonable behavior up to extreme temperatures and pressures are formulated. As possible ways for assessment of the extrapolation behavior of an equation of state, comparisons with experimental data at very high pressures and temperatures and with theoretically predicted features of the so-called “ideal curves” of a fluid are discussed. Finally, the current status of our knowledge of the extrapolation behavior of empirical equations of state is summarized and its shortcomings are pointed out.

[1]  G. L. Schott Shock-compressed carbon dioxide: Liquid measurements and comparisons with selected models , 1991 .

[2]  B. Armstrong,et al.  A method of correlation using a search procedure, based on a step-wise least-squares technique, and its application to an equation of state for propylene , 1979 .

[3]  Richard T. Jacobsen,et al.  Thermodynamic Properties of Nitrogen Including Liquid and Vapor Phases from 63K to 2000K with Pressures to 10,000 Bar, , 1973 .

[4]  Daniel G. Friend,et al.  Thermophysical Properties of Ethane , 1991 .

[5]  E. C. Morris Improved and extended high‐pressure PVT measurements for argon , 1984 .

[6]  W. Wagner,et al.  A New Equation of State for Carbon Dioxide Covering the Fluid Region from the Triple‐Point Temperature to 1100 K at Pressures up to 800 MPa , 1996 .

[7]  W. M. Haynes,et al.  Isochoric (p, Vm, T) measurements on CO2 and on (0.982CO2+0.018N2) from 250 to 330 K at pressures to 35 MPa , 1989 .

[8]  D. Miller,et al.  Joule-Thomson Inversion Curve, Corresponding States, and Simpler Equations of State , 1970 .

[9]  William J. Nellis,et al.  Shock compression of liquid argon, nitrogen, and oxygen to 90 GPa (900 kbar) , 1980 .

[10]  S. Angus,et al.  International thermodynamic tables of the fluid state. 5. Methane , 1978 .

[11]  R. L. Mills,et al.  Sound velocity and the equation of state of N2 to 22 kbar , 1975 .

[12]  R. G. Wylie,et al.  Accurate method for high pressure PVT measurements and results for argon for T=−20 to +35 °C and p in the range 200–480 MPa , 1980 .

[13]  R. D. Gunn,et al.  Inversion temperatures and pressures for cryogenic gases and their mixtures , 1966 .

[14]  Wolfgang Wagner,et al.  A New Equation of State and Tables of Thermodynamic Properties for Methane Covering the Range from the Melting Line to 625 K at Pressures up to 100 MPa , 1991 .

[15]  W. Nellis,et al.  Equation of state of shock‐compressed liquids: Carbon dioxide and air , 1991 .

[16]  Richard T. Jacobsen,et al.  Thermodynamic Properties of Argon from the Triple Point to 1200 K with Pressures to 1000 MPa , 1989 .

[17]  H. Preston‐Thomas,et al.  The International Temperature Scale of 1990 (ITS-90) , 1990 .

[18]  K. Pitzer,et al.  EQUATIONS OF STATE VALID CONTINUOUSLY FROM ZERO TO EXTREME PRESSURES FOR H2O AND CO2 , 1994 .

[19]  K. Pitzer,et al.  Equations of state valid continuously from zero to extreme pressures with H2O and CO2 as examples , 1995 .

[20]  Richard T. Jacobsen,et al.  Thermodynamic Properties of Nitrogen from the Freezing Line to 2000 K at Pressures to 1000 MPa , 1986 .

[21]  Manson Benedict,et al.  An Empirical Equation for Thermodynamic Properties of Light Hydrocarbons and Their Mixtures I. Methane, Ethane, Propane and n‐Butane , 1940 .

[22]  Kenneth S. Pitzer,et al.  An equation of state for carbon dioxide valid from zero to extreme pressures , 1994 .

[23]  P. Kortbeek,et al.  Compressibility and sound velocity measurements on N2 up to 1 GPa , 1988 .

[24]  M. Lallemand,et al.  Variation of the polarizability of noble gases with density , 1977 .

[25]  John S. Rowlinson,et al.  The equation of state of dense systems , 1965 .

[26]  J. Ely,et al.  Application of a new selection algorithm to the development of a wide-range equation of state for refrigerant R134a , 1995 .

[27]  Wolfgang Wagner,et al.  A new method for optimizing the structure of thermodynamic correlation equations , 1989 .

[28]  R. Schmidt,et al.  A new form of the equation of state for pure substances and its application to oxygen , 1985 .

[29]  R. D. Gunn,et al.  Prediction of thermodynamic properties of dense gas mixtures containing one or more of the quantum gases , 1966 .

[30]  P. Kortbeek,et al.  Apparatus for the measurement of compressibility isotherms of gases up to 10 kbar: Experimental data for argon at 298.15 K , 1988 .

[31]  D. Straub Zur Theorie eines allgemeinen Korrespondenzprinzips der thermischen Eigenschaften fluider Stoffe , 1964 .

[32]  W. Sharp,et al.  CO2 fugacity at high temperatures and pressures from experimental decarbonation reactions , 1978 .

[33]  A. Michels,et al.  Isotherms of argon between 0°c and 150°c and pressures up to 2900 atmospheres , 1949 .

[34]  V. V. Sychev,et al.  Thermodynamic properties of helium , 1987 .