Sammendrag
The spinodal represents the limit of thermodynamic stability of a homogeneous fluid. In this work, we present a robust methodology
to obtain the spinodal of multicomponent fluids described even with the most sophisticated equations of state (EoS) available. We
elaborate how information about the spinodal and its uncertainty can contribute both in the development of modern EoS and to
estimate their uncertainty in the metastable regions. Inequality constraints are presented that can be exploited in the fitting of
modern EoS of single-component fluids to avoid inadmissible pseudo-stable states between the vapor and liquid spinodals. We find
that even cubic EoS violate some of these constraints.
Using a selection of EoS representative of modern applications, we compare vapor and liquid spinodal curves, superheat and
supersaturation limits from classic nucleation theory (CNT), and available experimental data for the superheat limit. Computations
are performed with pure species found in natural gas, binary mixtures herein, as well as a multi-component natural gas mixture in
order to demonstrate the scalability of the approach. We demonstrate that there are large inconsistencies in predicted spinodals from
a wide range of EoS such as cubic EoS, extended corresponding state EoS, SAFT and multiparameter EoS. The overall standard
deviation in the prediction of the spinodal temperatures were 1.4 K and 2.7 K for single- and multi-component liquid-spinodals and
6.3 K and 26.9 K for single- and multi-component vapor spinodals.
The relationship between the measurable limit of superheat, or supersaturation, and the theoretical concept of the spinodal is
discussed. While nucleation rates from CNT can deviate orders of magnitude from experiments, we find that limit of superheat
experiments agree within 1.0 K and 2.4 K with predictions from CNT for single- and multi-component fluids respectively. We
demonstrate that a large part of the metastable domain of the phase diagram is currently unavailable to experiments, in particular
for metastable vapor. Novel techniques, experimental or with computational simulations should be developed to characterize the
thermodynamic properties in these regions, and to identify the thermodynamic states that define the spinodal.
to obtain the spinodal of multicomponent fluids described even with the most sophisticated equations of state (EoS) available. We
elaborate how information about the spinodal and its uncertainty can contribute both in the development of modern EoS and to
estimate their uncertainty in the metastable regions. Inequality constraints are presented that can be exploited in the fitting of
modern EoS of single-component fluids to avoid inadmissible pseudo-stable states between the vapor and liquid spinodals. We find
that even cubic EoS violate some of these constraints.
Using a selection of EoS representative of modern applications, we compare vapor and liquid spinodal curves, superheat and
supersaturation limits from classic nucleation theory (CNT), and available experimental data for the superheat limit. Computations
are performed with pure species found in natural gas, binary mixtures herein, as well as a multi-component natural gas mixture in
order to demonstrate the scalability of the approach. We demonstrate that there are large inconsistencies in predicted spinodals from
a wide range of EoS such as cubic EoS, extended corresponding state EoS, SAFT and multiparameter EoS. The overall standard
deviation in the prediction of the spinodal temperatures were 1.4 K and 2.7 K for single- and multi-component liquid-spinodals and
6.3 K and 26.9 K for single- and multi-component vapor spinodals.
The relationship between the measurable limit of superheat, or supersaturation, and the theoretical concept of the spinodal is
discussed. While nucleation rates from CNT can deviate orders of magnitude from experiments, we find that limit of superheat
experiments agree within 1.0 K and 2.4 K with predictions from CNT for single- and multi-component fluids respectively. We
demonstrate that a large part of the metastable domain of the phase diagram is currently unavailable to experiments, in particular
for metastable vapor. Novel techniques, experimental or with computational simulations should be developed to characterize the
thermodynamic properties in these regions, and to identify the thermodynamic states that define the spinodal.