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Journal articles on the topic 'Ternary liquid'

Author: Grafiati

Published: 18 May 2024

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1

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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2

Tripathi, Bhawana S., Anjali Awasthi, and Aashees Awasthi. "Estimation of acoustic nonlinearity parameter and molecular characteristics of ternary liquid mixtures at different temperatures." Canadian Journal of Physics 88, no. 4 (April 2010): 283–92. http://dx.doi.org/10.1139/p10-001.

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The acoustic nonlinearity parameter (B/A) of ternary liquid mixtures of heterocyclic compounds viz. pyridine and quinoline with phenol in benzene has been evaluated at 308.15, 318.15, and 328.15 K by three different methods viz. Tong–Dong method, Beyer’s method, and Beyer’s method using Tong–Dong coefficients. The molecular interactions in the liquid mixtures are explained on the basis of excess nonlinearity parameter ((B/A)E). Sehgal’s relations for calculating the molecular properties for pure liquids are extended to the ternary liquid mixtures.

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3

MINAGAWA, KEIJI, YASUNORI AOKI, TAKESHI MORI, and MASAMI TANAKA. "TERNARY ELECTRORHEOLOGICAL FLUIDS WITH COMPOSITE PARTICLES DISPERSED IN LIQUID BLENDS." International Journal of Modern Physics B 20, no. 25n27 (October 30, 2006): 3987–92. http://dx.doi.org/10.1142/s0217979206040738.

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The electrorheological (ER) properties were studied with ternary suspensions containing solid and liquid dispersoids in silicone oil (DMS). The solid dispersoid used was polyether/montmorillonite nanocomposite particles in which polyether molecules were intercalated between the layers of montmorillonite. The liquid dispersoid was urethane-modified polyether prepared from 4,4′-diphenylmethane diisocyanate (MDI) and poly(propylene glycol) (PPG). The steady shear viscosity and dynamic viscoelasticity were measured with a rotating parallel disc rheometer equipped with ER measurement system. The binary and ternary mixtures of these solid and liquid dispersoids with DMS, i.e. composite particle/DMS suspension, polyether/DMS liquid blend, and ternary blend containing both dispersoids, showed an increase of viscosity in response to an electric field (positive ER effect). The ER effect of a ternary suspension containing the particles and polyether liquids was larger than those of binary suspension or blend with one of these dispersoids. The ER effect was found to be improved by combination of the solid and liquid dispersoids, although the recovery time of viscosity after removing the electric field became rather longer, which would be due to the partly irreversible macroscopic aggregation of the dispersoids.

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4

MINAGAWA, KEIJI, TETSUO KANNO, HIROKAZU OKAMURA, TAKESHI MORI, SEIZO MASUDA, HIDENAO TAKAGI, KIYOHITO KOYAMA, and MASAKI TANAKA. "NOVEL ELECTRORHEOLOGICAL MATERIALS WITH TERNARY BLENDS CONTAINING POLYETHERS AND URETHANES." International Journal of Modern Physics B 16, no. 17n18 (July 20, 2002): 2481–86. http://dx.doi.org/10.1142/s0217979202012542.

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Ternary ER blends composed of two different liquids and solid dispersoid were prepared by blending silicone oil, viscous polyether liquid, and urethane powder at various compositions. The polyether liquid used here was polytetramethylene glycol modified with phenyl isocyanate, and the powder was urethane derivative of 4,4'-diphenylmethane diisocyanate. Under certain conditions, some of the ternary blends showed larger increase of viscosity under an electric field than those of binary mixtures prepared from each component of the ternary one. In this case, the viscous polyether and urethane powder act cooperativity by forming some particular structures within the blends. Microscopic observation revealed that each urethane particle was covered with polyether liquid in the absence of electric field, and that the binary droplets aggregated to form viscous bridges between the electrodes keeping powders within them.

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5

Novák, Josef P., Jaroslav Matouš, Květuše Říčná, and Vladimír Kubíček. "Liquid-liquid equilibrium in the water-ethanol-toluene system. Correlation of equilibrium data." Collection of Czechoslovak Chemical Communications 54, no. 3 (1989): 586–601. http://dx.doi.org/10.1135/cccc19890586.

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Liquid-liquid equilibrium data in the water-ethanol-toluene system were correlated by the superposition of the Wilson and Redlich-Kister equations with a ternary term. The correlation of both homogeneous binary systems was taken from the literature. The ternary liquid-liquid equilibrium data were at all temperatures satisfactorily described on using only three ternary parameters determined from the equilibrium data at 50 °C. The parameters obtained by the correlation yield also a good estimate of boiling point and composition of homogeneous azeotropic mixture.

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6

Kubíček, Vladimír, Josef P. Novák, and Jaroslav Matouš. "Liquid-Liquid Equilibrium in the Water-Methyl tert-Butyl Ether-Nitromethane-Ethylene Glycol System." Collection of Czechoslovak Chemical Communications 58, no. 5 (1993): 983–95. http://dx.doi.org/10.1135/cccc19930983.

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The liquid-liquid equilibrium was measured at 20 °C in the title quaternary system and in the three nitromethane-containing ternary subsystems. The data were compared with those predicted by a superposition of the Wilson and Redlich-Kister equations including the ternary parameters. The agreement between the observed and calculated data is very good both for the quaternary system and for the three ternary systems.

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7

Kacem, Rami Haj, Mohamed Dallal, Nuhed Al-Omair, Ahlam Al-Arfaj, Nora Alzamel, and Noureddine Ouerfelli. "Analysis of correlation between viscosity Arrhenius parameters: Extension to ternary liquid mixtures." Mediterranean Journal of Chemistry 6, no. 5 (November 14, 2017): 208–15. http://dx.doi.org/10.13171/mjc65/0171114633rhk.

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The study of viscosity-temperature dependence is important for the design and the optimization of several industrial processes and products. In this context, an interesting equation is recently proposed for pure solvents correlating the two parameters of the viscosity Arrhenius-type equation, as knowing the activation energy (Ea) and the pre-exponential factor (As), allowing the simplification of the viscosity Arrhenius equation to become an expression depending on only one parameter instead of two. The present work investigates the validity of the simplified Arrhenius-type equation for ternary fluids mixtures. The extension of the proposed equation to ternary liquid mixtures is very important since it simplifies the estimation of viscous behavior and the ensuing calculations. Using statistical methods and 114 experimental data from the literature on viscosity for 5 ternary liquid mixtures over different temperature ranges at atmospheric pressure, we found that the validation of the proposed equation depends significantly on the density of liquids and is validated only for 4 studied ternary liquid mixtures. This result opens the way to investigate the sensitivity of the equation’s parameters for more specific mixtures.

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8

Oh, Suk Yung, and Young Chan Bae. "Liquid–liquid equilibria for ternary polymer mixtures." Chemical Physics 379, no. 1-3 (January 2011): 128–33. http://dx.doi.org/10.1016/j.chemphys.2010.12.002.

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9

Krishna, R., C. Y. Low, D. M. T. Newsham, C. G. Olivera-Fuentes, and G. L. Standart. "Ternary mass transfer in liquid-liquid extraction." Chemical Engineering Science 40, no. 6 (1985): 893–903. http://dx.doi.org/10.1016/0009-2509(85)85003-x.

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10

Islam, Akand, Anand Zavvadi, and Vinayak Kabadi. "Analysis of Partition Coefficients of Ternary Liquid-Liquid Equilibrium Systems and Finding Consistency Using Uniquac Model." Chemical and Process Engineering 33, no. 2 (June 1, 2012): 243–53. http://dx.doi.org/10.2478/v10176-012-0022-1.

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Analysis of Partition Coefficients of Ternary Liquid-Liquid Equilibrium Systems and Finding Consistency Using Uniquac Model The objective of this study is to investigate the change in partition coefficient with a change in the concentration of the solute in a liquid system consisting of two relatively immiscible solvents. To investigate the changes in the partition coefficients, the data of the partition coefficients at infinite dilution and the ternary Liquid-Liquid Equilibrium (LLE) data at finite concentrations of the solute should be consistent. In this study, 29 ternary systems that are found in literature and for which the partition coefficients at infinite dilution and the ternary LLE data cannot be predicted accurately by the universal quasi-chemical (UNIQUAC) model are identified. On the basis of this model, some consistent and inconsistent ternary systems are introduced. Three inconsistent systems, namely hexane-butanol-water, CCl4 (carbon tetrachloride)-PA (propanoic acid)-water, and hexane-PA-water, are chosen for detailed analysis in this study. The UNIQUAC activity coefficient model is used to represent these data over a range of concentrations. The results show large errors, exhibiting the inability of this model to correlate the data. Furthermore, some ternary systems in which cross behavior of solutes between two phases observed are identified.

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11

Zhang, Tian Fei, Chuan Yi Pan, Sheng Hu, and Heng De Li. "Ternary Liquid-Liquid Equillibria for (Water + Methanol + β-Citronellol) at 283.15 and 313.15 K." Advanced Materials Research 396-398 (November 2011): 977–80. http://dx.doi.org/10.4028/www.scientific.net/amr.396-398.977.

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Liquid-liquid equilibrium tie-line data are reported for ternary mixture of (water + methanol +β-citronellol) at 283.15 and 313.15 K. The miscibility for the ternary (water + methanol + β-citronellol) LLE was increasing as the the temperature increased. The experimental liquid–liquid equilibrium data have been satisfactorily represented by using an extended UNIQUAC model.

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12

Eshed, E., M. Bamberger, and A. Katsman. "Diffusional Decomposition and Glass Forming Ability of Solidifying Ternary Liquids." MRS Advances 1, no. 26 (2016): 1935–40. http://dx.doi.org/10.1557/adv.2016.62.

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ABSTRACTAn innovative model based on spinodal-like decomposition of supercooled multi-component liquids was developed for prediction of the glass forming ability (GFA) of ternary alloys. The up-hill diffusion in the initially homogeneous freezing ternary liquid was considered as a necessary condition for solidification of crystalline phases. New generalized criteria of spinodal decomposition of ternary alloys for time/space correlated fluctuations were formulated. These criteria take into account both thermodynamic and kinetic properties of the system. The introduced criteria were found to provide adequate GFA evaluation of different compositions in the Mg-based ternary alloys.

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13

Cai, Fufeng, and Guomin Xiao. "Liquid–liquid equilibria for ternary systems ethanol+heptane+phosphoric-based ionic liquids." Fluid Phase Equilibria 386 (January 2015): 155–61. http://dx.doi.org/10.1016/j.fluid.2014.12.007.

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14

Yan, Xing Yue, Yong Chun Cheng, and Xiao Ping Hu. "Liquid-Liquid Equilibrium for (Water + Palm Oil Biodiesel + Methanol) Ternary System at Different Temperatures." Advanced Materials Research 455-456 (January 2012): 867–71. http://dx.doi.org/10.4028/www.scientific.net/amr.455-456.867.

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The liquid-liquid equilibrium (LLE) of ternary mixtures (water + palm oil biodiesel + methanol) was measured under atmospheric pressure and temperatures of 303.15K, 313.15K and 323.15K. The mutual solubility of biodiesel and water increased as the increasing of ratio of methanol. Also, the mutual dissolution of the mixture was slightly promoted by increasing temperature. The phase diagrams and tie lines for the ternary system were determined by high-temperature gas chromatography (HTGC). NRTL and UINQUAC models were applied to fit the experimental data for the ternary system, and the binary interaction parameters were obtained by regression on the experimental data. Both models could describe the LLE behavior of the systems fairly well.

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15

Radu, Tudose, and Gabriela Lisa. "The determination of individual mass transfer coefficients in liquid-liquid extraction." Chemical Industry 57, no. 9 (2003): 393–98. http://dx.doi.org/10.2298/hemind0309393r.

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An improved Lewis cell has been used as an efficient method to determine the mass transfer coefficient for any ternary multi-component system. In this paper the individual mass transfer coefficients were determined for three ternary systems: water-acetone-carbon tetrachloride water-acetone-chloroform and water-acetone-toluene, using the improved Lewis cell. Criteria! equations were developed to calculate the mass transfer coefficients when one or both (organic and aqueous) phases were agitated and when solute transfer occurs in both directions.

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16

Rowley, Richard L., Gary L. White, and Mudau Chiu. "Ternary liquid mixture thermal conductivities." Chemical Engineering Science 43, no. 2 (1988): 361–71. http://dx.doi.org/10.1016/0009-2509(88)85049-8.

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17

Pandey, J. D., Siddharth Pandey, Shikha Gupta, and A. K. Shukla. "Viscosity of ternary liquid mixtures." Journal of Solution Chemistry 23, no. 9 (September 1994): 1049–59. http://dx.doi.org/10.1007/bf00974102.

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18

Maduro, Raquel M., and Martín Aznar. "Liquid–liquid equilibrium of ternary systems containing nicotine." Fluid Phase Equilibria 259, no. 1 (October 2007): 83–88. http://dx.doi.org/10.1016/j.fluid.2007.02.016.

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19

Kim, Yeong-Cheol, Jong-Duk Kim, and Hwayong Kim. "Ternary liquid-liquid phase behavior by decorated-uniquac." Korean Journal of Chemical Engineering 13, no. 5 (September 1996): 439–47. http://dx.doi.org/10.1007/bf02705991.

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20

Kruber, Kai Fabian, Marius Krapoth, and Tim Zeiner. "Interfacial mass transfer in ternary liquid-liquid systems." Fluid Phase Equilibria 440 (May 2017): 54–63. http://dx.doi.org/10.1016/j.fluid.2017.02.013.

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21

Mirarabrazi, Meysam, Olga Stolarska, Marcin Smiglak, and Christian Robelin. "Solid–liquid equilibria for a pyrrolidinium-based common-cation ternary ionic liquid system, and for a pyridinium-based ternary reciprocal ionic liquid system: an experimental study and a thermodynamic model." Physical Chemistry Chemical Physics 20, no. 1 (2018): 637–57. http://dx.doi.org/10.1039/c7cp04678b.

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22

Nagata, Isamu. "Simultaneous correlation of ternary vapour-liquid and liquid-liquid equilibria." Thermochimica Acta 164 (July 1990): 119–26. http://dx.doi.org/10.1016/0040-6031(90)80428-2.

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23

Knezevic-Stevanovic, Andjela, Goran Babic, Mirjana Kijevcanin, Slobodan Serbanovic, and Dusan Grozdanic. "Correlation of the liquid mixture viscosities." Journal of the Serbian Chemical Society 77, no. 8 (2012): 1083–89. http://dx.doi.org/10.2298/jsc120127038k.

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In this paper forty two selected correlation models for liquid mixture viscosities of organic compounds were tested on 219 binary and 41 ternary sets of experimental data taken from literature. The binary sets contained 3675 experimental data points for 70 different compounds. The ternary sets contained 2879 experimental data points for 29 different compounds. The Heric I, Heric-Brewer II, and Krishnan-Laddha models demonstrated the best correlative characteristics for binary mixtures (overall absolute average deviation < 2%). The Heric I, Heric-Brewer II, Krishnan-Laddha and Heric II models demonstrated the best correlative characteristics for ternary mixtures (overall absolute average deviation < 3%).

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24

Kanibolotsky, Dmitry S., Valentina A. Stukalo, Volodymyr M. Dubyna, Olena A. Bieloborodova, and Vladyslav V. Lisnyak. "EMF study of liquid Al–Fe–Ge alloys." International Journal of Materials Research 94, no. 12 (December 1, 2003): 1293–95. http://dx.doi.org/10.1515/ijmr-2003-0233.

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Abstract The thermodynamic properties of ternary liquid Al–Fe–Ge alloys have been studied in the temperature range of 1050 – 1250 K by the electromotive force (EMF) technique with a liquid electrolyte. The ternary alloys are characterized by negative deviations from Raoult’s law.

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25

Marciniak, Andrzej, and Marek Królikowski. "Ternary liquid–liquid equilibria of bis(trifluoromethylsulfonyl)-amide based ionic liquids+methanol+heptane." Fluid Phase Equilibria 318 (March 2012): 56–60. http://dx.doi.org/10.1016/j.fluid.2012.01.018.

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26

Wlazło, Michał, and Andrzej Marciniak. "Ternary liquid–liquid equilibria of trifluorotris(perfluoroethyl)phosphate based ionic liquids+methanol+heptane." Fluid Phase Equilibria 338 (January 2013): 253–56. http://dx.doi.org/10.1016/j.fluid.2012.11.014.

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27

Wlazło, Michał, and Andrzej Marciniak. "Ternary liquid–liquid equilibria of trifluorotris(perfluoroethyl)phosphate based ionic liquids+benzothiophene+heptane." Fluid Phase Equilibria 361 (January 2014): 54–59. http://dx.doi.org/10.1016/j.fluid.2013.10.028.

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28

Marciniak, Andrzej, and Marek Królikowski. "Ternary (liquid+liquid) equilibria of {trifluorotris(perfluoroethyl)phosphate based ionic liquids+thiophene+heptane}." Journal of Chemical Thermodynamics 49 (June 2012): 154–58. http://dx.doi.org/10.1016/j.jct.2012.01.026.

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29

Kubíček, Vladimír, Jaroslav Matouš, and Josef P. Novák. "Phase Equilibria in the Water-Methyl Alcohol-Methyl tert-Butyl Ether-Ethylene Glycol System." Collection of Czechoslovak Chemical Communications 57, no. 10 (1992): 2021–41. http://dx.doi.org/10.1135/cccc19922021.

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Liquid-liquid equilibria were measured at 20 °C in the W-MeOH-MTBE-EG quaternary system (W is water, MeOH is methyl alcohol, MTBE is methyl tert-butyl ether, and EG is ethylene glycol) and in the W-MeOH-MTBE, W-MTBE-EG and MeOH-MTBE-EG ternary systems. In the W-MeOH-MTBE-EG, W-MeOH-MTBE, and MeOH-MTBE-EG systems, the vapour-liquid equilibria at atmospheric pressure were also measured. The experimental data of the quaternary system were compared with those modelled by superposition of the Wilson and Redlich-Kister equations with the ternary term, whose parameters were determined based on the corresponding binary and, in some cases, ternary systems. A very good agreement was obtained for both the liquid-liquid and vapour-liquid equilibria.

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30

Mehta, U., S. K. Yadav, I. Koirala, and D. Adhikari. "Surface Properties of Al–Fe–Si Liquid Alloy Using Thermodynamic Database." Journal of Nepal Physical Society 6, no. 2 (December 31, 2020): 10–19. http://dx.doi.org/10.3126/jnphyssoc.v6i2.34849.

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Temperature-dependent interaction parameters for excess free energies of mixing of sub-binary systems of Al-Fe-Si ternary liquid alloys were optimised using the experiment data in the frame of Redlich-Kister (R-K) polynomials. These optimised parameters were then used to compute the partial excess free energy of sub-binary and ternary liquid alloys. The surface tension and surface concentration of sub-binary and the ternary liquid alloys were computed using Butler equation. The temperature dependent coefficients of R-K polynomials for excess surface tensions of the sub-binary systems were optimised which were then used to estimate the surface tension of ternary alloy using Chou, Kohler and Toop modelling equations at temperatures 1773, 1873, 1973 and 2073 K. The surface tension of the ternary alloy obtained using aforementioned models were found to be in good agreement from Fe and Al corners but some deviations were observed from Si corner.

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31

Graczová, Elena, Július Surový, and Soňa Bafrncová. "Ternary Corrections in the Liquid-Liquid Equilibria Computation for Three-Component Systems Containing Components of Mixed Solvent N-Methylpyrrolidone-Ethylene Glycol." Collection of Czechoslovak Chemical Communications 57, no. 1 (1992): 7–15. http://dx.doi.org/10.1135/cccc19920007.

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Presented are the liquid-liquid (L-L) equilibrium data for three-component heterogeneous systems toluene-N-methylpyrrolidone-ethylene glycol, heptane-N-methylpyrrolidone-ethylene glycol and heptane-toluene-ethylene glycol at 50 °C. Equations for the excess Gibbs energy (NRTL. Novák modification of Wilson equation and Redlich-Kister 4th order expansion) extended by ternary universal contribution were employed for correlating the L-L equilibrium data. The binary equation parameters were independently evaluated from the binary equilibrium data. The presented ternary data served for evaluation of parameters of the universal ternary contribution.

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32

Durski, Marcin, Paramespri Naidoo, Deresh Ramjugernath, and Urszula Domańska. "Ternary liquid-liquid phase equilibria of {ionic liquid + thiophene + (octane/hexadecane)}." Journal of Chemical Thermodynamics 134 (July 2019): 157–63. http://dx.doi.org/10.1016/j.jct.2019.03.017.

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33

Rodríguez-Escontrela, Iria, Iago Rodríguez-Palmeiro, Oscar Rodríguez, Alberto Arce, and Ana Soto. "Liquid–liquid–liquid equilibria for water+[P66614][DCA]+dodecane ternary system." Fluid Phase Equilibria 405 (November 2015): 124–31. http://dx.doi.org/10.1016/j.fluid.2015.07.022.

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34

Novák, Josef P., Karel Řehák, Petr Voňka, and Jaroslav Matouš. "Critical curves of liquid–liquid equilibria in ternary systems." Fluid Phase Equilibria 208, no. 1-2 (June 2003): 199–221. http://dx.doi.org/10.1016/s0378-3812(03)00037-2.

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35

Olaya, M. M., J. A. Reyes-Labarta, R. Velasco, I. Ibarra, and A. Marcilla. "Modelling liquid–liquid equilibria for island type ternary systems." Fluid Phase Equilibria 265, no. 1-2 (March 2008): 184–91. http://dx.doi.org/10.1016/j.fluid.2007.12.010.

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36

Liu, Jianguo, Zhangfeng Qin, and Jianguo Wang. "Liquid−Liquid Equilibria for Methanol + Water + Hexane Ternary Mixtures." Journal of Chemical & Engineering Data 47, no. 5 (September 2002): 1243–45. http://dx.doi.org/10.1021/je0255269.

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37

Backes, H. M., Ma Jing Jun, Bender E., and Maurer G. "Interfacial tensions in binary and ternary liquid—liquid systems." Chemical Engineering Science 45, no. 1 (1990): 275–86. http://dx.doi.org/10.1016/0009-2509(90)87099-e.

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38

Connemann, M., J. Gaube, L. Karrer, A. Pfennig, and U. Reuter. "Measurement and representation of ternary vapour—liquid—liquid equilibria." Fluid Phase Equilibria 60, no. 1-2 (October 1990): 99–118. http://dx.doi.org/10.1016/0378-3812(90)85045-c.

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39

Morley, R., and M. Minceva. "Ternary separations in liquid-liquid chromatography: Which mode when?" Chemie Ingenieur Technik 90, no. 9 (August 24, 2018): 1319–20. http://dx.doi.org/10.1002/cite.201855405.

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40

Coca, José, and Ramona M. Díaz. "Ternary liquid-liquid equilibrium in tetrahydrofuran-water-solvent systems." Journal of Chemical Technology and Biotechnology 29, no. 11 (April 24, 2007): 694–702. http://dx.doi.org/10.1002/jctb.503291105.

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41

Bairagya, Priyotosh, Debashis Kundu, and Tamal Banerjee. "A priori prediction of complex liquid–liquid–liquid equilibria in organic systems using a continuum solvation model." Physical Chemistry Chemical Physics 22, no. 38 (2020): 22023–34. http://dx.doi.org/10.1039/d0cp03225e.

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Application of Rachford–Rice LLLE (RRL3E) and Henley–Rosen LLLE (HRL3E) algorithms for the prediction of liquid–liquid–liquid equilibria phase behavior of ternary and quaternary systems invoking COnductor like Screening MOdel-Segment Activity Coefficient model.

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42

Yamaguchi, Tsuyoshi, Song-Ho Chong, and Norio Yoshida. "Phase equilibrium of three-component liquid systems composed of water, alcohol, and sodium chloride studied by the reference interaction-site model integral equation theory." Journal of Chemical Physics 158, no. 8 (February 28, 2023): 084502. http://dx.doi.org/10.1063/5.0142256.

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A theoretical method for calculating the thermodynamic properties and phase equilibria of a binary liquid mixture using the reference interaction-site model (RISM) integral equation theory, which we had proposed recently, was extended to ternary liquid systems containing salt. A novel dielectric correction of the RISM theory for a mixture of solvents was also proposed. The theory was applied to mixtures composed of water, alcohol, and NaCl, where the alcohol was either methanol or ethanol. The decrease in NaCl solubility with increasing alcohol molar fractions in the solvent was calculated. In the ethanol system, the theory yielded salt-induced liquid–liquid phase separation, which was observed experimentally in a ternary mixture of water, 1-propanol, and NaCl. The phase diagram of the ternary system was determined theoretically.

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43

Erkoç, Tuğba, Lutfullah M. Sevgili, and Selva Çavuş. "Liquid−Liquid Extraction of Linalool from Methyl Eugenol with 1-Ethyl-3-methylimidazolium Hydrogen Sulfate [EMIM][HSO4] Ionic Liquid." Open Chemistry 17, no. 1 (August 24, 2019): 564–70. http://dx.doi.org/10.1515/chem-2019-0067.

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AbstractThe liquid–liquid equilibrium (LLE) data for a ternary system {methyl eugenol + linalool +1-ethyl-3-methylimidazolium hydrogen sulfate [EMIM][HSO4]} (Meu-Lin-IL) were measured at 298.2 K and atmospheric pressure. The Othmer–Tobias correlation was used to verify the reliability of the experimental tie-line data. The solubility curves were obtained using the cloud point titration indicating the liquid-liquid equilibrium of the ternary system was in Type II class where two immiscible curve pairs were attained. Distribution coefficients, separation factors and selectivity were calculated for the immiscibility regions. The calculated results were compared with the experimental data. Characterization studies were performed by Fourier transform infrared spectroscopy (FTIR), thermal gravimetric analysis (TGA) and proton nuclear magnetic resonance spectroscopy (1H-NMR) techniques.

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44

Sklyarchuk, Vasyl, and Yuriy Plevachuk. "Thermophysical properties of liquid ternary chalcogenides." High Temperatures-High Pressures 34, no. 1 (2002): 29–34. http://dx.doi.org/10.1068/htwu4.

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Pandey, J. D., N. K. Soni, V. K. Singh, and V. Sanguri. "Surface Tension of Ternary Liquid Mixtures." Physics and Chemistry of Liquids 39, no. 6 (November 2001): 763–72. http://dx.doi.org/10.1080/00319100108031691.

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Butt, M. T. Z., and C. Bodsworth. "Liquid immiscibility in ternary metallic alloys." Materials Science and Technology 7, no. 9 (September 1991): 795–802. http://dx.doi.org/10.1179/mst.1991.7.9.795.

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Yang, Jianjian, Fernando Vereda, Jose R. Morillas, and Juan de Vicente. "Ternary solid-ferrofluid-liquid magnetorheological fluids." Smart Materials and Structures 27, no. 7 (May 31, 2018): 075017. http://dx.doi.org/10.1088/1361-665x/aac4c9.

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Stead, Rebecca J., and Keith Stead. "Phase diagrams for ternary liquid systems." Journal of Chemical Education 67, no. 5 (May 1990): 385. http://dx.doi.org/10.1021/ed067p385.

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Mikula, A., and S. Knott. "Thermodynamic investigations of ternary liquid alloys." Journal of Physics: Condensed Matter 20, no. 11 (February 20, 2008): 114109. http://dx.doi.org/10.1088/0953-8984/20/11/114109.

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Sklyarchuk, V., and Yu Plevachuk. "Thermophysical properties of liquid ternary chalcogenides." Journal of Physical Studies 4, no. 2 (2000): 155–58. http://dx.doi.org/10.30970/jps.04.155.

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