Thermodynamics of complex systems (eg with associating molecules, multicomponent
mixtures, multiphase equilibria, wide ranges of conditions, estimation of many different …

The Riedel vapor pressure correlation is a useful model that has been employed for
decades. The shape of the temperature dependent correlation is a strong function of the …

Isothermal vapor–liquid equilibria at 333.15 K and 353.15 K for four binary mixtures of
benzene+ nonane, toluene+ o-xylene, m-xylene+ sulfolane and o-xylene+ sulfolane have …

In this study, vapor–liquid and liquid–liquid equilibrium in mixtures containing glycol ether
surfactant, non-polar and polar compounds are calculated using Perturbed Hard Sphere …

In this study, the perturbed chain statistical associating fluid theory (PC-SAFT) equation of
state (EoS) has been utilized for thermodynamic modeling of vapor–liquid and liquid–liquid …

Vapor–liquid equilibria (VLE) for the n-heptane+ ethylene glycol monopropyl ether and n-
octane+ ethylene glycol monopropyl ether systems were measured. Isobaric VLE …

Fluid properties and phase behavior of systems such as glycol ethers, carboxylic acids, and
proteins are affected by the competition between intra-and intermolecular hydrogen …

Isothermal vapor–liquid equilibrium measurements (pressure–temperature–liquid and vapor
composition) were conducted for water (1)+ propan-1-ol (2), n-hexane (1)+ butan-2-ol (2) …

Isothermal vapor liquid equilibria for the binary system of ethylene glycol monopropyl ether
with 2, 2-dimehylbutane and 2, 3-dimethylbutane were measured in a circulating water bath …

Isothermal vapor–liquid equilibria at 333.15 K, 343.15 K and 353.15 K for three binary
mixtures of o-xylene, m-xylene and p-xylene individually mixed with N-methylformamide …