Relevant bibliographies by topics / Liquid-liquid equilibrum

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  1. Journal articles

Academic literature on the topic 'Liquid-liquid equilibrum'

Author: Grafiati
Published: 4 June 2021
Last updated: 7 February 2022

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Journal articles on the topic "Liquid-liquid equilibrum"

1

Komori, Toshiyuki, and Shuzo Ohe. "Vapor-liquid equilibrum data for the system: Cyclohexane-n-heptane at atmospheric pressure." KAGAKU KOGAKU RONBUNSHU 16, no. 2 (1990): 384–87. http://dx.doi.org/10.1252/kakoronbunshu.16.384.

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Jena, Vinod, Sanjay Ghosh, Sapana Gupta, Piyush Thakur, Noorjahan Ansari, and Natalija Matić. "LIQUID-LIQUID EQUILIBRIA OF THE PHOSPHORIC ACID, ESTER AND WATER TERNARY SYSTEM." Rudarsko-geološko-naftni zbornik 35, no. 2 (2020): 85–90. http://dx.doi.org/10.17794/rgn.2020.2.8.

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3

Jin, Yi. "Electrochemical Properties of GaCl3 in Ionic Liquid [C2mim][GaCl4]." Advanced Materials Research 634-638 (January 2013): 2596–99. http://dx.doi.org/10.4028/www.scientific.net/amr.634-638.2596.

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Under dry argon atmosphere, the colourless and transparent ionic liquid [C2mim][GaCl4] was synthesized. Using [C2mim][GaCl4] as solvent, a solution of GaCl3with molarity 5.227×10-3 mol/cm3 was prepared at 303.15 K and there is a equilibrum between the solute and the solvent: GaCl3+ [C2mim][GaCl4] → [C2mim][Ga2Cl7]. The cyclic voltammogram of the solution had been carried out relative to Al/Al3+reference electrode, with GC working electrode and Ga counter electrode, with various scan rates from 30 to 700mV/s, in a temperature range of 303.15 to 343.15 K, respectively. The results indicated that
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4

Lozano, L. J., F. J. Alguacil, M. Alonso, and C. Godínez. "Review of algorithms for modeling metal distribution equilibria in liquid-liquid extraction processes." Revista de Metalurgia 41, no. 5 (2005): 374–83. http://dx.doi.org/10.3989/revmetalm.2005.v41.i5.227.

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5

Kua, Y. L., S. Gan, A. Morris, and H. K. Ng. "Liquid-Liquid Equilibrium Data for the Ternary Systems of Palm Oil + Ethyl Lactate + Phytonutrients (Carotenes and Tocols) at 303.15 K." International Journal of Chemical Engineering and Applications 8, no. 3 (2017): 215–20. http://dx.doi.org/10.18178/ijcea.2017.8.3.659.

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6

Walker, Christoph. "Asymptotic behaviour of liquid–liquid dispersions." Proceedings of the Royal Society of Edinburgh: Section A Mathematics 134, no. 4 (2004): 753–72. http://dx.doi.org/10.1017/s0308210500003462.

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Based on earlier results on existence, we study the asymptotic behaviour of solutions to the coalescence-breakage equations, including the volume-scattering phenomenon and high-energy collisions. The solutions are shown to converge towards one particular equilibrium, provided the kernels satisfy a kind of reversibility. We also derive stability of these equilibria in a suitable topology.
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7

Yan, B., R. Guo, and J. Zhang. "A study on phase equilibria in the CaO-Al2O3-SiO2-“Nb2O5”(5 mass pct) system in reducing atmosphere." Journal of Mining and Metallurgy, Section B: Metallurgy 49, no. 2 (2013): 145–51. http://dx.doi.org/10.2298/jmmb120823013y.

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Phase equilibria in 5 mass% ?Nb2O5? plane of CaO-Al2O3-SiO2-?Nb2O5? system at 1873 K in an oxygen partial pressure of 1.78?10-6 Pa have been investigated through isothermal equilibration and quenching followed by EPMA examinations. In order to characterize the effect of niobium oxide on the phase relationship of the CaO-Al2O3-SiO2 system, Nb2O5-containing and Nb2O5-free samples with the same CaO/Al2O3/SiO2 weight ratio were investigated simultaneously. The ratios of CaO/Al2O3/SiO2 were selected from the CaO?2Al2O3-liquid two-phase equilibrium region in the CaO-Al2O3- SiO2 system at1873 K. It w
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8

Oktavian, Rama, Agung Ari Wibowo, and Zuraidah Fitriah. "Study on Particle Swarm Optimization Variant and Simulated Annealing in Vapor Liquid Equilibrium Calculation." Reaktor 19, no. 2 (2019): 77–83. http://dx.doi.org/10.14710/reaktor.19.2.77-83.

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Phase equilibrium calculation plays a major rule in optimization of separation process in chemical processing. Phase equilibrium calculation is still very challenging due to highly nonlinear and non-convex of mathematical models. Recently, stochastic optimization method has been widely used to solve those problems. One of the promising stochastic methods is Particle Swarm Optimization (PSO) due to its simplicity and robustness. This study presents the capability of particle swarm optimization for correlating isothermal vapor liquid equilibrium data of water with methanol and ethanol system by
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9

Islam, Akand, and Vinayak Kabadi. "Universal liquid mixture model for vapor-liquid and liquid-liquid equilibria in hexane-butanol-water system over the temperature range 10 - 100 °C." Chemical and Process Engineering 32, no. 2 (2011): 101–15. http://dx.doi.org/10.2478/v10176-011-0009-3.

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Universal liquid mixture model for vapor-liquid and liquid-liquid equilibria in hexane-butanol-water system over the temperature range 10 - 100 °C This is an extended research of the paper (Islam et al., 2011) conducted to obtain a universal set of interaction parameters of the model NRTL over the temperature range 10 - 100 °C for hexane-butanol-water system; meaning for binary pairs hexane-butanol, butanol-water and hexane-water; and for ternary system hexane-butanol-water. Thorough investigations of data selections for all binary pairs (Vapor-Liquid Equilibrium (VLE), Liquid-Liquid Equilibri
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10

Domanska, Urszula, and Juan Antonio Gonzalez. "Thermodynamics of mixtures containing a very strongly polar compound. Part II. Solid-liquid equilibria for sulfolane + nitrile systems and characterization of the sulfolane-nitrile and sulfolane-1-alkyne interactions in terms of DISQUAC." Canadian Journal of Chemistry 80, no. 5 (2002): 476–82. http://dx.doi.org/10.1139/v02-066.

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Equilibrium temperatures for solid–liquid transitions of mixtures formed by sulfolane and ethanenitrile, propanenitrile, butanenitrile, or pentanenitrile were measured by a dynamic method. The solid–liquid equilibria phase diagrams show positive deviations from Raoult's law, except for the system with ethanenitrile, which is nearly ideal. The sulfolane–nitrile and sulfolane–1-alkyne interactions have been characterized in terms of the DISQUAC group contribution model. DISQUAC properly represents a complete set of thermodynamic properties: solid–liquid equilibria, molar excess enthalpies, and n
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