Results 1 to 10 of about 385 (155)

Droplet Evaporation Process of a Fluorobenzene + n-Octane + Polystyrene Mixture [PDF]

open access: yesMolecules, 2023
The vapor–liquid equilibrium of the fluorobenzene–polystyrene binary polymer solution at 303.15 K was measured using a static pressure device. The vapor–liquid equilibrium of the fluorobenzene–n-octane–polystyrene ternary solution in a partial ...
Wei Wang, Zhendong Zhou, Bo Zhou
doaj   +2 more sources

Experimental investigation and thermodynamic correlation of chlordiazepoxide solubility in supercritical CO₂ [PDF]

open access: yesScientific Reports
This study investigated the solubility of chlordiazepoxide in supercritical carbon dioxide (SCCO₂) at pressures ranging from 12 to 30 (MPa) and temperatures ranging from 308 to 338 (K). The measured solubilities ranged from 19.8 to 576 parts per million (
Nedasadat Saadati Ardestani   +4 more
doaj   +2 more sources

Using the group contribution method to predict the flash temperature of biodiesel and ethanol mixtures [PDF]

open access: yesHeliyon
This article presents a novel approach to predict the flash temperature of biodiesel and ethanol mixtures using the Group Contribution Method (GCM). Expanding on the pioneering work by Liaw et al.
Esmaeil Bahrani   +2 more
doaj   +2 more sources

Implementation of the UNIQUAC model in the OpenCalphad software

open access: yesFluid Phase Equilibria, 2020
The UNIQUAC model is often used, for example in engineering, to obtain activity coefficients in multicomponentsystems, while the CALPHAD method is known for its capability in phase stability assessmentand equilibrium calculations. In this work, we combine them by representing the UNIQUAC model accordingto the CALPHAD method and implementing it in the ...
Bo Sundman   +2 more
exaly   +3 more sources

Identification of UNIQUAC binary interaction parameters in liquid-liquid equilibrium [PDF]

open access: yesFluid Phase Equilibria, 2020
Abstract An algorithm is presented for the estimation of the UNIQUAC interaction parameters for liquid-liquid equilibrium of ternary systems. The algorithm is based on two optimization levels. In the inner level the algorithm performs the minimization of an objective function based on the isoactivity conditions.
Sebastiano Tomassetti   +2 more
exaly   +3 more sources

Liquid-Liquid Equilibrium for Ternary Systems Containing Biodiesel+ Glycerol+ Alcohol (Ethanol or Methanol): Thermodynamic Modeling [PDF]

open access: yesJournal of Chemical and Petroleum Engineering, 2020
Biodiesel is a substitute for fossil fuels which is produced through a transesterification reaction between vegetable oils or animal fats and light alcohols such as methanol or ethanol.
Majid Mohadesi
doaj   +3 more sources

Liquid-Liquid Extraction in a Microextractor: A Laboratory Examination and Thermodynamic Modeling of N-Hexane + Benzene + Sulfolane System [PDF]

open access: yesIranian Journal of Chemistry & Chemical Engineering, 2021
This study aimed at investigating liquid-liquid extraction of the three-component n-hexane + benzene + sulfolane system in a micro extractor. Experiments were carried out in a microtube with a diameter of 800μm using a T-shaped micromixer at a residence ...
Majid Mohadesi   +2 more
doaj   +1 more source

Phase Diagrams for the Aqueous Solutions of Carboxylic Acid with Dipropyl Ether: Experimental and Correlated Data [PDF]

open access: yesIranian Journal of Chemistry & Chemical Engineering, 2020
In this research, liquid-liquid equilibrium (LLE) data were experimentally obtained for the ternary systems of (water + carboxylic acid + dipropyl ether) at T = 298.2 K and P = 101.3 kPa.
Dilek Özmen, Sezin Bekri
doaj   +1 more source

Machine Learning Approaches for Prediction of Phase Equilibria in Poly (Ethylene Glycol) + Sodium Phosphate Aqueous Two-Phase Systems [PDF]

open access: yesIranian Journal of Chemistry & Chemical Engineering, 2020
In this research, liquid-liquid equilibrium (LLE) data were experimentally obtained for the ternary systems of (water + carboxylic acid + dipropyl ether) at T = 298.2 K and P = 101.3 kPa.
Mohsen Pirdashti   +3 more
doaj   +1 more source

Experimental Investigation and Thermodynamic Modeling in Liquid-Liquid Equilibrium of Water + Propionic Acid + Cyclic Alcohols at T= 303.2, 313.2 and 323.2 K [PDF]

open access: yesJournal of Chemical and Petroleum Engineering, 2022
Recovery of propionic acid from aqueous solution is economically and environmentally important. In this study, the liquid-liquid equilibrium data of water + propionic acid + cyclic alcohols (cyclopentanol and cyclohexanol) ternary system was obtained at ...
Faezeh Shahbazi, Majid Mohadesi
doaj   +3 more sources

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