Abstract

With his publication in 1873 [1] J. W. Gibbs formulated the thermodynamic theory. It describes almost all macroscopically observed properties of matter and could also describe all phenomena if only the free energy U - ST were explicitly known numerically. The thermodynamic uniqueness of the free energy obviously depends on that of the internal energy U and the entropy S, which in both cases Gibbs had been unable to specify. This uncertainty, lasting more than 100 years, was not eliminated either by Nernst’s hypothesis S = 0 at T = 0. This was not achieved till the advent of additional proof of the thermodynamic relation U = 0 at T = Tc. It is noteworthy that from purely thermodynamic consideration of intensive and extensive quantities it is possible to derive both Gibbs’s formulations of entropy and internal energy and their now established absolute reference values. Further proofs of the vanishing value of the internal energy at the critical point emanate from the fact that in the case of the saturated fluid both the internal energy and its phase-specific components can be represented as functions of the evaporation energy. Combining the differential expressions in Gibbs’s equation for the internal energy, d(μ/T)/d(1/T) and d(p/T)/d(1/T), to a new variable d(μ/T)/d(p/T) leads to a volume equation with the lower limit vc as boundary condition. By means of a variable transformation one obtains a functional equation for the sum of two dimensionless variables, each of them being related to an identical form of local interaction forces between fluid particles, but the different particle densities in the vapor and liquid spaces produce different interaction effects. The same functional equation also appears in another context relating to the internal energy. The solution of this equation can be given in analytic form and has been published [2] [3]. Using the solutions emerging in different sets of problems, one can calculate absolutely the internal energy as a function of temperature-dependent, phase-specific volumes and vapor pressure.

Highlights

  • The purpose of this paper is to show that Gibbs’s theory [1] contains intrinsically “natural” reference values of entropy and internal energy that are reciprocal and represent thermodynamic reference values [4]

  • The same applies to other extensive quantities such as the entropy S, internal energy U, enthalpy H, free energy F, and heat capacity C

  • One obtains the following characteristic thermodynamic reference values, which are valid for every gas: u (0) = ul (0) = −(uv − ul )(0), uv (0) = 0, u (Tc ) = ul (Tc ) = uv (Tc ) = 0. (2.2)

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Summary

Elsner

U (M ,V ,Tc ) = 0 , Critical Volume V= M ⋅ d (μ T ) d ( p T ) c , Two-Phase Equilibrium −M (uv − ul )(0) ≤ ST + M=μ M vv + vl − (vv − vl ) ln (vv vl ) ⋅d ( p T ) d (1 T ) + Vdp dT ⋅T = U + Vp ≤ Vp ≤ Vpc , Chemical Potential Negative, M μ (T ) ≤ M μ (0)= U (M ,V , 0)= M ⋅ −(uv − ul )(0) < 0

Introduction
Elsner DOI
Intensive and Extensive Quantities of the Saturated Fluid
Interdependence of Extensive and Intensive Quantities
Entropy and Internal Energy Relations
Heat Capacity Relations
Chemical Potential Relations
Internal Fluid Energy as a Function of the Condensation Energy
Internal Fluid Energy as an Expression of Measurable Quantities
Phase-Specific Energy as a Function of the Evaporation Energy
Results and Discussion
Full Text
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