Application of the excess entropy scaling to the transport properties of n-alkanes, jet fuels, and a biodiesel over the entire vapor–liquid phase equilibria

• New excess entropy scaling approach was developed to cover entire fluid region for the transport properties. • Universal exponents were proposed for thermal conductivity and viscosity of organic molecules. • Comparison was made between LJ molecular simulation viscosity data and the universal correlation. • Transport properties of hydrogen-containing systems were predicted based on the pure-component excess entropy scaling. • Transport properties of biodiesel B100 were estimated based on low-pressure data. In this study, the entropy scaling developed for the transport properties, namely the thermal conductivity, dynamic viscosity, and self-diffusion coefficient, has been extended and applied to the dense gas and liquid regions, when the configurational entropy is the only requirement. Two approaches are proposed in the excess entropy scaling. First, the general formula Γ Γ 0 Γ / Γ 0 H S = b e x p aS e x k B T with reducing quantity Γ 0 – representing the Boltzmann dilute gas properties – is used to provide universal exponents for the thermal conductivity and viscosity. Model predictions with excess entropies calculated simultaneously via the multiparameter Helmholtz energy equations of state (EoS) and the Peng-Robinson (PR) cubic EoS were compared to the experimental data by achieving qualitative agreement over the entire phase diagram. In the second approach, for a single-component model derivation, the transport property formula was decomposed into dilute, background, and critical enhancement terms. The excess entropy is hidden in the background term, which was regressed against the density. Moreover, the proposed universal formula for the excess entropy scaling was tested against the molecular dynamics’ viscosity data for the Lennard-Jones fluid. The viscosity and thermal conductivity of carbon dioxide + hydrogen and methane + hydrogen were also predicted using the entropy scaling of pure-compounds. The methods were developed and examined based on a broad variety of fluids including refrigerants, alcohols, ethers, alkanes, jet fuels, and a biodiesel.

Authors

Institutions

Publication Details

Journal
Fuel
Published
2025-05-08
DOI
https://doi.org/10.1016/j.fuel.2025.135583
Primary Topic
Phase Equilibria and Thermodynamics
Type
article
Field-Weighted Citation Impact
0.00

Funders

Controls
|||
ALL TIME
JAN
FEB
MAR
APR
MAY
JUN
JUL
AUG
SEP
OCT
article

Application of the excess entropy scaling to the transport properties of n-alkanes, jet fuels, and a biodiesel over the entire vapor–liquid phase equilibria

Ali Aminian, Václav Vinš
1 links
Fuel
Phase Equilibria and Thermodynamics
article

Application of the excess entropy scaling to the transport properties of n-alkanes, jet fuels, and a biodiesel over the entire vapor–liquid phase equilibria

Ali Aminian, Václav Vinš
article en

Abstract

• New excess entropy scaling approach was developed to cover entire fluid region for the transport properties. • Universal exponents were proposed for thermal conductivity and viscosity of organic molecules. • Comparison was made between LJ molecular simulation viscosity data and the universal correlation. • Transport properties of hydrogen-containing systems were predicted based on the pure-component excess entropy scaling. • Transport properties of biodiesel B100 were estimated based on low-pressure data. In this study, the entropy scaling developed for the transport properties, namely the thermal conductivity, dynamic viscosity, and self-diffusion coefficient, has been extended and applied to the dense gas and liquid regions, when the configurational entropy is the only requirement. Two approaches are proposed in the excess entropy scaling. First, the general formula Γ Γ 0 Γ / Γ 0 H S = b e x p aS e x k B T with reducing quantity Γ 0 – representing the Boltzmann dilute gas properties – is used to provide universal exponents for the thermal conductivity and viscosity. Model predictions with excess entropies calculated simultaneously via the multiparameter Helmholtz energy equations of state (EoS) and the Peng-Robinson (PR) cubic EoS were compared to the experimental data by achieving qualitative agreement over the entire phase diagram. In the second approach, for a single-component model derivation, the transport property formula was decomposed into dilute, background, and critical enhancement terms. The excess entropy is hidden in the background term, which was regressed against the density. Moreover, the proposed universal formula for the excess entropy scaling was tested against the molecular dynamics’ viscosity data for the Lennard-Jones fluid. The viscosity and thermal conductivity of carbon dioxide + hydrogen and methane + hydrogen were also predicted using the entropy scaling of pure-compounds. The methods were developed and examined based on a broad variety of fluids including refrigerants, alcohols, ethers, alkanes, jet fuels, and a biodiesel.

FuelVol. 398
Czech Academy of Sciences, Institute of Thermomechanics (CZ)
European Commission, Ministerstvo Školství, Mládeže a Tělovýchovy, Grantová Agentura České Republiky, Ústav termomechaniky, Akademie Věd České Republiky
Affordable and clean energy
Openalex Percentile: Top 91%
Phase Equilibria and Thermodynamics
AI Navigator

Ask Laika to Summarize, Analyze, and Connect papers live on the map.

Summarize Papers & Methodologies

Extract key findings, datasets, and comparative methods across publications.

Benchmark Rankings & Visual Analytics

Rank top research institutions, authors, funders, topics, and journals by Field-Weighted Citation Impact (FWCI) and paper volume with instant charts.

Connect Distant Disciplines

Bridge topological clusters on the map to find hidden collaborative intersections.