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Thermodynamic Fluid Equations-Of-State

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Thermodynamic Fluid Equations-Of-State entropy Article Thermodynamic Fluid Equations-of-State Leslie V. Woodcock Department of Physics, University of Algarve, 8005-139 Faro, Portugal; [email protected] Received: 24 October 2017; Accepted: 30 December 2017; Published: 4 January 2018 Abstract: As experimental measurements of thermodynamic properties have improved in accuracy, to five or six figures, over the decades, cubic equations that are widely used for modern thermodynamic fluid property data banks require ever-increasing numbers of terms with more fitted parameters. Functional forms with continuity for Gibbs density surface ρ(p,T) which accommodate a critical-point singularity are fundamentally inappropriate in the vicinity of the critical temperature (Tc) and pressure (pc) and in the supercritical density mid-range between gas- and liquid-like states. A mesophase, confined within percolation transition loci that bound the gas- and liquid-state by third-order discontinuities in derivatives of the Gibbs energy, has been identified. There is no critical-point singularity at Tc on Gibbs density surface and no continuity of gas and liquid. When appropriate functional forms are used for each state separately, we find that the mesophase pressure functions are linear. The negative and positive deviations, for both gas and liquid states, on either side of the mesophase, are accurately represented by three or four-term virial expansions. All gaseous states require only known virial coefficients, and physical constants belonging to the fluid, i.e., Boyle temperature (TB), critical temperature (Tc), critical pressure (pc) and coexisting densities of gas (ρcG) and liquid (ρcL) along the critical isotherm. A notable finding for simple fluids is that for all gaseous states below TB, the contribution of the fourth virial term is negligible within experimental uncertainty. Use may be made of a symmetry between gas and liquid states in the state function rigidity (dp/dρ)T to specify lower-order liquid-state coefficients. Preliminary results for selected isotherms and isochores are presented for the exemplary fluids, CO2, argon, water and SF6, with focus on the supercritical mesophase and critical region. Keywords: equation-of-state; liquid-gas criticality; carbon dioxide; argon; water; SF6; virial coefficients 1. Introduction There is a long history and an extensive literature of cubic equations-of-state, going back 140 years, from van der Waals renowned two-term equation for Andrew’s original p-V-T data on carbon dioxide [1], to current research and compilations with hundreds of terms and parameters. As the thermodynamic experimental measurements have improved in accuracy, ever more complex equations have evolved [2]. These equations are used to represent experimental thermodynamic properties for modern data banks such as the NIST compilation for CO2 [2,3]. Over recent decades, ever-increasing numbers of terms and more fitted parameters are required. The Span–Wagner equation for CO2 [2], for example, contains hundreds of terms, each with many fitted parameters, and various adjustable fractional exponents. As even more accurate data become available from future research, these functional forms will need yet more adjustable parameters. The basic reason of this inconvenient modeling practice is the van der Waals gas-liquid continuity hypothesis [1]. Continuous cubic functional forms are inappropriate in the vicinity of Tc and in the supercritical mid-range between gas and liquid phases. A mesophase, confined within percolation loci that bound the existence of gas and liquid phases by higher-order discontinuities, has been identified [4–6]. A simple numerical differentiation of NIST equations-of-state [7] can demonstrate the supercritical mesophase and observe the phase bounds, along any isotherm, of any fluid (e.g., CO2 Entropy 2018, 20, 22; doi:10.3390/e20010022 www.mdpi.com/journal/entropy Entropy 2018, 20, 22 2 of 15 Entropy 2018, 20, 22 2 of 15 Figure1) for any of the 200 fluids in the NIST Thermophysical Property data bank. These boundaries any of the 200 fluids in the NIST Thermophysical Property data bank. These boundaries have been havesmoothed been smoothed over by over the equations-of-state by the equations-of-state used to parameterize used to parameterize the original experimental the original data. experimental data. CO2 supercritical isotherms 40 750 700 600 35 500 450 30 400 340 25 375 330 p 350 20 320 (MPa) 15 310 10 305 5 0 0 5 10 15 20 density (mol/L) Figure 1. Supercritical T(K) isotherms for CO2: the green dashed line is the percolation loci PB; the blue Figure 1. Supercritical T(K) isotherms for CO : the green dashed line is the percolation loci PB; the blue dashed line is the percolation loci PA; the green2 and blue solid circles are the maximum experimentally dashed line is the percolation loci PA; the green and blue solid circles are the maximum experimentally observable coexisting gas density, and minimum coexisting liquid density along Tc i.e., 305 K (purple). observable coexisting gas density, and minimum coexisting liquid density along Tc i.e., 305 K (purple). Within the uncertainties, p(ρ,T) is a linear function of ρ in the mesophase region. The origin of Withinthe linearity the uncertainties, is the colloidal p(natureρ,T) isof athe linear supercritical function mesophase of ρ in the [6,8] mesophase with a linear region. combination The origin rule of the linearityfor thermodynamic is the colloidal state nature functions, of the supercriticalsimilar to subcritical mesophase lever [rule6,8] for with the a inhomogeneous linear combination 2-phase rule for region. When appropriate functional forms are used for gaseous and liquid states separately, we find thermodynamic state functions, similar to subcritical lever rule for the inhomogeneous 2-phase region. that all other isothermal thermodynamic state functions in the mesophase are linear functions of When appropriate functional forms are used for gaseous and liquid states separately, we find that all density. In the case of pressure, the negative and positive adjacent deviations for liquid and gas on othereither isothermal side are thermodynamic quadratic. The parameterizations state functions in re thequire mesophase only physical are linearconstants functions belonging of density.to the In the casespecific of pressure, fluid, Boyle the negativetemperature and (T positiveB), critical adjacent temperature deviations (TC), and for coexisting liquid and densities gas on eitheralong the side are quadratic.critical The isotherm, parameterizations and known virial require coefficients only physical b2(T) and constants b3(T) etc. belonging A remarkable to the finding specific is that fluid, for Boyle temperaturethe gas phases (TB), critical below T temperatureB, the coefficient (TC ),b4 andis effectively coexisting zero densities within the along experimental the critical uncertainty. isotherm, and knownThere virial is rigidity coefficients symmetry b2(T) between and b3(T) gas etc. and A liquid remarkable phases findingon either is side that of for the the mesophase gas phases reported below TB, previously [9], that relates the lower coefficients of the liquid equation to properties of the gas in the the coefficient b4 is effectively zero within the experimental uncertainty. There is rigidity symmetry betweenvicinity gas of and the liquid percolation phases loci. on either side of the mesophase reported previously [9], that relates the The objective of this research is to investigate the extent that these findings can be used to describe lower coefficients of the liquid equation to properties of the gas in the vicinity of the percolation loci. experimental thermodynamic properties of a pure fluid over the whole range of equilibrium existence. The objective of this research is to investigate the extent that these findings can be used to describe Here, we investigate equations-of-state for gas, liquid and mesophase separately, each of which, in experimentalan initial thermodynamicapproximation, require properties only ofmeasurable a pure fluid physical over theconstants whole specific range ofto equilibrium particular fluids. existence. Here,Comparisons we investigate with equations-of-stateexperimental data are for made gas, vi liquida the NIST and mesophasethermo-physical separately, databank each [3]. NIST of which, in antabulations initial approximation, reproduce experimental require only data measurable with 100% physicalaccuracy, constantsand therefore, specific provide to particular a foremost fluids. Comparisonscriteria for with testing experimental the alternative data description are made to viavan the der NIST Waals thermo-physical underlying science databank of critical [ 3and]. NIST tabulationssupercritical reproduce behavior experimental of fluids as datadescribed with in 100% references accuracy, [4–9]. and therefore, provide a foremost criteria for testing the alternative description to van der Waals underlying science of critical and supercritical behavior of fluids as described in references [4–9]. Entropy 2018, 20, 22 3 of 15 2. Rigidity and Fluid-State Bounds Rigidity, (!)T, is the work required to isothermally and reversibly increase the density of a fluid. With dimensions of a molar energy, this simple state function relates directly to the change in Gibbs energy (G) with density at constant T Entropy 2018, 20, 22 3 of 15 2. Rigidity and Fluid-State Bounds! T = (dp/dρ)T = ρ(dG/dρ)T (1) The inequalitiesRigidity, that (ω)T distinguish, is the work gasrequired from to liquid isothermally are: and reversibly increase
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