Correlation of Viscosity of Aqueous Solutions of Alkanolamine Mixtures Based on the Eyring's Theory and Wong-Sandler Mixing Rule [PDF]
Iranian Journal of Chemistry & Chemical Engineering, 2013 A viscosity model, based on Eyring’s absolute rate theory combined with a cubic PR equation of state and Wong-Sandler mixing rule, has been proposed in order to correlate viscosities of aqueous solutions of alkanolamine mixtures at atmospheric pressure ...
Sara Ahmad Kelayeh +3 more
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Applicability of NRTL Model for Prediction of the Viscosity of Alkanolamine + Water Mixtures [PDF]
Linköping Electronic Conference Proceedings, 2020 Linkoping University Electronic Press use a Creative Commons licensing system. Readers may download, read, distribute and use material from published publication on LiU E-press for non-commercial use only as long as they give complete attribution to the authors i.e. full reference to the author and the original publication.
Karunarathne, Sumudu S., Øi, Lars Erik
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Isobaric Vapor - Liquid Equilibria of Gasoline Additives Systems At 101.3 kPa [PDF]
Engineering and Technology Journal, 2010 In this study, isobaric vapor-liquid equilibrium of gasoline additives for threeternary systems: “MTBE + Ethanol + 2-Methyl-2-propanol”, “Ethanol + 2-Methyl-2-propanol + Octane”, and “MTBE + Ethanol + Octane” at 101.3kPa arestudied.
Khalid Farhod Chasib Al-Jiboury +1 more
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Determination and Calculation of Phase Equilibrium for Aqueous Ternary System (NH2)2CO+KCl+H2O at 283.15K [PDF]
E3S Web of Conferences, 2020 The solid-liquid phase equilibrium for ternary system (NH2)2CO+KCl+H2O was determined by isothermal saturation method at 283.15K under atmosphere pressure. The isothermal phase diagrams was drawn in according to the measured solubility data.
Hu Xue +5 more
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Measurement and Modeling of Solubility of Galactose in Aqueous Ionic Liquids, 1-Butyl-3-Methyl Imidazolium Bromide, 1-Hexyl-3-Methyl Imidazolium Bromide and 1-Butyl-3-Methylimidazolium Chloride at T = (298.15 And 308.15) K [PDF]
Pharmaceutical Sciences, 2019 Background: Saccharides are considered as abundant, cheap and renewable starting materials for chemicals and fuels. Recently, ionic liquids have been used as green solvents for saccharides.
Mohammad Taghi Zafarani Moattar +2 more
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Temperature Effect on the Interaction Parameters of GC-NRTL Model Using the Genetic Algorithm
Chemical Engineering Transactions, 2013 Liquid-liquid equilibrium data is imperatively needed for the design of separation processes, particularly solvent extraction. The experimental measuring approach is complex and costly for a great number of chemical systems, and hence the need for ...
N. Bouneb, A.H. Meniai
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Measurement and Correlation of Liquid-Liquid Equilibrium Data of Mesityl oxide-Diethoxymethane-Water System [PDF]
E3S Web of Conferences, 2021 To provide essential data for the separation of diethoxymethane and system water using mesityl oxide as the extractant, in this paper, the liquid-liquid equilibrium data of the ternary system of ‘mesityl oxide + diethoxymethane + water’ was measured at ...
Guo Hongyue +3 more
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A Modified van der Waals Mixture Theory for Associating Fluids: Application to Ternary Aqueous Mixtures [PDF]
Iranian Journal of Chemistry & Chemical Engineering, 2012 In this study a simple and general chemical association theory is introduced. The concept of infinite equilibrium model is re-examined and true mole fractions of associated species are calculated. The theory is applied to derive the distribution function
Seyed Foad Aghamiri +3 more
doaj
Chemical Engineering Transactions, 2019 Gamma-valerolactone (GVL) is used in green technology to produce chemicals and biofuels. Separation of GVL from mixtures within a process is a recurring challenge in chemical plants.
Valter Nunes Trindade-Junior +3 more
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Thermo, 2022 Thermodynamics, as a scientific tool, advises on the control of variables involved in processes of different nature and is particularly useful in the design of equipment, or to obtain previous simulations. However, to generate more accurate models, an exact science is required.
Luis Fernández +2 more
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