posted on 2020-08-06, 22:18authored byJean-Noël Jaubert, Yohann Le Guennec, Andrés Piña-Martinez, Nicolas Ramirez-Velez, Silvia Lasala, Bastian Schmid, Ilias K. Nikolaidis, Ioannis G. Economou, Romain Privat
In the last two centuries, equations
of state (EoSs) have become
a key tool for the correlation and prediction of thermodynamic properties
of fluids. They not only can be applied to pure substances as well as to mixtures but
also constitute the heart of commercially available computer-aided-process-design
software. In the last 20 years, thousands of publications have been
devoted to the development of sophisticated models or to the improvement
of already existing EoSs. Chemical engineering thermodynamics is thus
a field under steady development, and to assess the accuracy of a
thermodynamic model or to cross-compare two models, it is necessary
to confront model predictions with experimental data. In this context,
the importance of a reliable free-to-access benchmark database is
pivotal and becomes absolutely necessary. The goal of this paper is
thus to present a database, specifically designed to assess the accuracy
of a thermodynamic model or cross-compare models, to explain how it
was developed and to enlighten how to use it. A total of 200 nonelectrolytic
binary systems have been selected and divided into nine groups according
to the associating character of the components, i.e., their ability
to be involved in a hydrogen bond (the nature and strength of the
association phenomena are indeed considered a measure of the complexity
to model the thermodynamic properties of mixtures). The methodology
for assessing the performance of a given model is then described.
As an illustration, the Peng–Robinson EoS with classical van
der Waals mixing rules and a temperature-dependent binary interaction
parameter (kij) have been used to correlate
the numerous data included in the proposed database, and its performance
has been assessed following the proposed methodology.