Relevant bibliographies by topics / Ternary liquid

Academic literature on the topic 'Ternary liquid'

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Published: 18 May 2024

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Journal articles on the topic "Ternary liquid"

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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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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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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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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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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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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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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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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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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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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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Dissertations / Theses on the topic "Ternary liquid"

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Das, Jitesh Chandra. "Correlations of certain physico - chemical properties of some ternary liquid mixtures with selected parameters of corresponding pure components." Thesis, University of North Bengal, 1989. http://hdl.handle.net/123456789/714.

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Lutsyk, V. I., and A. E. Zelenaya. "Ternary Systems for the Liquid Immiscibility Gap Technology." Thesis, Sumy State University, 2013. http://essuir.sumdu.edu.ua/handle/123456789/35368.

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The computer models for T-x-y diagrams with the mono- and invariant monotectic equilibrium, and monovariant syntectic equilibrium by means of kinematical simulation of phase regions boundaries are considered. The effect of syntectic equilibrium changing for monotectic one is investigated with the material balances visualization. When you are citing the document, use the following link http://essuir.sumdu.edu.ua/handle/123456789/35368
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Siddons, Daniel James. "Synthetic routes to binary and ternary nitrides." Thesis, University of Nottingham, 1997. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.363637.

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Kurosawa, Izumi. "Solid-Liquid Equilibrium in Multi Solute Systems." Diss., Georgia Institute of Technology, 2004. http://hdl.handle.net/1853/4993.

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Solid-liquid equilibrium in isomorphous amino acid systems has been investigated as a model for systems that form solid solutions. Solid- and liquid-phase compositions in L-valine + L-leucine, L-valine + L-isoleucine, and L-isoleucine + L-valine in water were measured over the entire range of solid composition, and it was shown (from mass balance and phase rule considerations) that these systems form solid solutions. The solid- phases resulting from isothermal and cooling crystallization experiments were also investigated using powder x-ray diffractometry which showed that homogeneous solid solutions could only be obtained in cooling crystallization experiments, whereas isothermal experiments generally produced inhomogeneous solids. This suggests that data reported in the literature from isothermal experiments may not represent true equilibrium values. Solid-phase activity coefficients were estimated using binary and ternary equilibrium data and the UNIFAC-Kuramochi model for liquid-phase nonidealities. The solid phases in the three systems investigated exhibited significant nonidealities that were correlated using the Margules model. The model parameters exhibited a linear relationship with the ratio of binary solubilities of the two solutes. Such simple relationship may be advantageous when solid-liquid equilibrium of thermally unstable solutes or components with unknown physical properties are crystallized.
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Galand, Quentin. "Experimental investigation of the diffusive properties of ternary liquid systems." Doctoral thesis, Universite Libre de Bruxelles, 2012. http://hdl.handle.net/2013/ULB-DIPOT:oai:dipot.ulb.ac.be:2013/209626.

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A fundamental step in the further developments of comprehensive modelling of the diffusive processes in liquids requires the possibility of obtaining reliable and accurate experimental data of the diffusion and thermodiffusion coefficients of multicomponent liquid systems. In the present work, we perform an experimental investigation of the diffusive properties of binary and ternary liquid systems. Two experimental techniques, the ‘Open Ended Capillary’ technique and the ‘Transient Interferometric Technique’ have been developed. Those techniques have been used for the experimental characterization of several systems composed of 1,2, 3,4-Tetrahydrnaphtalene, Isobutylbenzene and Dodecane at ambient temperature. Those particular species were selected as a simplified multicomponent system modelling the fluids contained in natural crude oils reservoirs.

For each of these techniques, experimental set-ups were designed, implemented and calibrated. The procedures for identifying the ternary diffusion coefficients from the measured compositions fields were studied in details.

The Open Ended Capillary Technique was applied under gravity condition to study isothermal diffusion binary and ternary systems. Difficulties related to a new procedure for interpreting the data collected at short times of the experiments are highlighted and its implication in the generalization of the technique for the study of multicomponent systems is discussed.

The Transient Interferometric Technique was used to perform an experimental study of three binary systems under gravity conditions. It was also applied for the investigation of ternary systems under microgravity condition in the frame of the DSC on SODI experiment, which took place aboard the International Space Station in 2011. The experimental results are reported and the analysis of the accuracy of the technique is presented. The TIT is the first technique ever providing accurate experimental measurements of the complete set of diffusion and thermodiffusion coefficients for ternary liquid systems.


Doctorat en Sciences de l'ingénieur
info:eu-repo/semantics/nonPublished

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Swisher, Mathew M. "Representing liquid-vapor equilibria of Ternary systems using neural networks." Thesis, Massachusetts Institute of Technology, 2015. http://hdl.handle.net/1721.1/97856.

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Thesis: S.M., Massachusetts Institute of Technology, Department of Mechanical Engineering, 2015.
Cataloged from PDF version of thesis.
Includes bibliographical references (pages 77-78).
We develop a method based on neural networks for efficiently interpolating equations of state (EOS) for liquid-vapor equilibria of ternary mixtures. We investigate the performance of neural networks both when experimental data are available and when only simulation data are available. Simulation data are obtained from Gibbs Ensemble Monte Carlo simulations, using the TraPPE-EH molecular model. Our investigation uses the mixture of carbon dioxide, methane, and ethane as a validation example, for which experimental data exist. Analysis of the error in a neural-network-generated liquid-vapor coexistence curve shows that the resulting interpolation is robust and accurate, even in the case where the network is trained on a few data points. We use this observation to construct a methodology for accurately locating liquid-vapor equilibria of ternary mixures wihout using any experimetnal data.
by Mathew M. Swisher.
S.M.
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Ivanov, Dimitry A. "Investigation of a ternary liquid mixture by the light scattering technique." [S.l.] : [s.n.], 2005. http://deposit.ddb.de/cgi-bin/dokserv?idn=98015216X.

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Taylor, Donald Fulton. "Measurement of binary phase equilibria and ternary/quaternary gas antisolvent (GAS) system measurement and analysis." Thesis, Available online, Georgia Institute of Technology, 2004:, 2004. http://etd.gatech.edu/theses/available/etd-07112004-194307/unrestricted/taylor%5Fonald%5Ff%5F200407%5FMS.pdf.

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Thesis (M.S.)--School of Chemical and Biomolecular Engineering, Georgia Institute of Technology, 2005. Directed by Charles Eckert.
Charles Eckert, Committee Chair ; Amyn Teja, Committee Member ; Pete Ludovice, Committee Member. Includes bibliographical references.
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Luna, Fabio. "Drying of Multicomponent Liquid Films." Doctoral thesis, KTH, Chemical Engineering and Technology, 2004. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-3778.

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The convective drying of thin layers of multicomponentliquid mixtures into an inert gas, and the influence ofdifferent process controlling mechanisms on drying selectivityis studied. Drying experiments under gas-phase-controlledconditions are performed by low intensity evaporation, fromfree liquid surfaces, of ternary mixtures without non-volatilesolutes. Liquid-side-controlled experiments are carried out bydrying a multicomponent polymeric solution containing twovolatile components, one non-volatile polymer and an optionalnonvolatile softening substance.

Mathematical models to describe gas- andliquid-side-controlled drying based on interactive diffusion inboth liquid and gas phases as the main mechanisms for masstransfer are developed. For gas-phase-controlled drying, astability analysis of the ordinary differential equations thatdescribes the evaporation process is performed. Isothermal andnon-isothermal drying processes are considered in batch andcontinuous modes. The mathematical model to describe thecomposition profiles during batch drying of the polymeric film,considering liquid resistance, is solved numerically. Due tothe lack of experimental data, properties for this polymericsystem are estimated by using established methods. Ananalytical solution of the diffusion equation, by assuming anisothermal drying process and a constant matrix ofmulticomponent diffusion coefficients is developed. For thecontinuous case, liquid-side resistance is studied by modellingevaporation of a multicomponent falling liquid film into aninert gas including indirect heating.

The results of the gas-phase-controlled model are in goodagreement with experimental results. For the polymeric film,the agreement is only qualitative since the model does notaccount for a membrane that develops on the film surface. Thestability analysis permits the prediction of trajectories andfinal state of a liquid mixture in a gas-phase-controlleddrying process. For isothermal evaporation of ternary mixturesinto pure gas, the solutions are trajectories in the phaseplane represented by a triangular diagram of compositions. Thepredicted ternary dynamic azeotropic points are unstable orsaddle. On the other hand, binary azeotropes are stable whenthe combination of the selectivities of the correspondingcomponents is negative. In addition, pure component singularpoints are stable when they are contained within theirrespective isolated negative selectivity zones. Undernon-isothermal conditions, maximum temperature valuescharacterise stable azeotropes. Incremental loading of the gaswith one or more of the components leads to a node-saddlebifurcation, where a saddle azeotrope and a stable azeotropecoalesce and disappear. For continuous drying, the singularpoints are infinite and represent dynamic equilibrium pointswhose stability is mainly dependent on the ratio of inletgas-to-liquid flow rates. As long as the process isgas-phasecontrolled, these results also apply to a porous solidcontaining a liquid mixture.

In general, liquid-side control makes the drying processless selective but it is difficult to maintain this conditionduring the whole process. Under the influence of its owndynamics, a process starting as liquid-side-controlled tendstowards a gas-phase-controlled process. The presence ofnon-volatile components and indirect heating may delay thisdevelopment. Considering the evolution of the processcontrolling steps and its influence on selectivity, a modelaimed at describing the complete trajectory of a drying orevaporation process must include the coexistence of allrelevant mechanisms.

Keywords:ternary mixture, falling film, diffusionequation, gas-phase control, liquid-phase control, selectivity,stability analysis, polymeric solution, evaporation, azeotrope,batch drying, continuous drying.

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Clements, Patricia J. "Critical point behaviour in binary and ternary liquid mixtures with particular reference to rheological and interfacial properties in model mixtures for microemulsions." Thesis, University of Sheffield, 1997. http://etheses.whiterose.ac.uk/10187/.

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The phase behaviour, rheological effects and interfacial properties of binary and ternary liquid mixtures have been studied near critical points. In particular, measurements have been made of the viscosity-at the bulk macroscopic level by capillary viscometry and at the microscopic level by fluorescence depolarisatiorr-and of critical-point wetting and adsorptiorr-at the solid-liquid interface using evanescent-wave-generated fluorescence spectroscopy and at the liquid-vapour interface using specular neutron reflection. The systems investigated have been mostly alkane + perfluoroalkane mixtures or 2-butoxyethanol + H20 or D20 mixtures, although in some cases hexamethyldisiloxane, propanenitrile and perfluorooctyloctane have also been the components of mixtures. The main outcomes of this study are: • Macroscopic viscosity: The divergence to infinity in the shear viscosity of hexane + perfluorohexane at the critical endpoint for approach along the path of constant critical composition both from the single phase and along both limbs of the coexistence curve is described well using the Renormalisation Group Theory critical exponent y = 0.04. The correlation length amplitude obtained by fitting the sheargradient dependence of the viscosity is ~o = (S.S±l.S) A. • Microscopic viscosity: The product of the rotational correlation time and the temperature 'tR"T, often taken as a measure of the microscopic viscosity, exhibits an anomaly as the critical point is approached as a function of temperature. This anomaly mirrors that in the macroscopic viscosity for some fluorescent dye probes, but for others the anomaly is in the opposite sense indicating that other effects such as solvent structure must playa part in the near-critical behaviour of'tR·T. • Critical-point wetting at the solid-liquid interface: The wetting transition temperature has been identified for heptane + perfluorohexane at the quartz-liquid interface from fluorescence lifetime measurements of a probe. The wetting layer is of the same composition as the bulk heptane-rich phase and the transition is tentatively identified as first-order. • Adsorption and wetting at the liquid-vapour interface: The surface structure of several mixtures has been determined by neutron reflection. The results are in general agreement with the expectations of critical-point wetting and adsorption. The surface is complex and in some mixtures an oscillatory scattering length density profile through the interface is required to model the reflectivity data. • Ternary mixtures: The phase behaviour of three mixtures exhibiting tunnel phase behaviour has been studied experimentally and various characteristics of the shape of the twmel identified. A theoretical study on one of the mixtures predicts the drop in temperature for the locus of maximum phase separation temperatures which is observed experimentally.
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Books on the topic "Ternary liquid"

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Macedo, E. A. Liquid-liquid equilibrium data collection: Tables, diagrams,and model parameters for binary, ternary, and quaternarysystems. Frankfurt/Main: DECHEMA, 1987.

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Vapor-Liquid Equilibria of Low Boiling Substances: Ternary Systems 2. Dechema, 1987.

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(Editor), H. Knapp, R. Doring (Editor), L. Oellrich (Editor), U. Plocker (Editor), J. M. Prausnitz (Editor), R. Langhorst (Editor), and S. Zeck (Editor), eds. Vapor-Liquid Equilibria of Low Boiling Substances: Ternary Systems 1. Dechema, 1987.

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(Editor), H. Knapp, R. Doring (Editor), L. Oellrich (Editor), U. Plocker (Editor), J. M. Prausnitz (Editor), R. Langhorst (Editor), and S. Zeck (Editor), eds. Vapor-Liquid Equilibria of Low Boiling Substances: Ternary Systems 3. Dechema, 1987.

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Vapor-liquid equilibria for mixtures of low boiling substances: Ternary systems. Frankfurt am Main: DECHEMA, 1989.

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Vapor-liquid equilibria for mixtures of low boiling substances: Ternary systems. Frankfurt am Main: DECHEMA, 1989.

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Vapor-liquid equilibria for mixtures of low boiling substances: Ternary mixtures. Frankfurt am Main: DECHEMA, 1989.

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Chʻen, Hsiao. A new general method for the optimization of HPLC ternary of pseudo-quaternary mobile phases and the separation of two new metabolites of nefopam from greyhound urine. 1990.

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National Aeronautics and Space Administration (NASA) Staff. Synthesis and Characterization of the First Liquid Single Source Precursors for the Deposition of Ternary Chalcopyrite (Cuins2) Thin Film Materials. Independently Published, 2018.

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Book chapters on the topic "Ternary liquid"

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Bülow, Mark, Andreas Danzer, and Christoph Held. "Liquid-Liquid Equilibria of Binary and Ternary Systems Containing Ionic Liquids." In Encyclopedia of Ionic Liquids, 1–7. Singapore: Springer Singapore, 2020. http://dx.doi.org/10.1007/978-981-10-6739-6_108-1.

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Bülow, Mark, Andreas Danzer, and Christoph Held. "Liquid-Liquid Equilibria of Binary and Ternary Systems Containing Ionic Liquids." In Encyclopedia of Ionic Liquids, 821–27. Singapore: Springer Nature Singapore, 2022. http://dx.doi.org/10.1007/978-981-33-4221-7_108.

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Park, Jang Min, Roberto Mauri, and Patrick D. Anderson. "Phase separation of viscous ternary liquid mixtures." In Multiphase Microfluidics: The Diffuse Interface Model, 73–91. Vienna: Springer Vienna, 2012. http://dx.doi.org/10.1007/978-3-7091-1227-4_2.

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Ott, K., M. Kiehl, M. Haghani, M. Hartrott, P. Maxim, C. A. Paulick, and D. Quitmann. "Nuclear Quadrupolar Relaxation and Thermodynamics in Liquid Ternary Alloys." In Amorphous and Liquid Materials, 312–14. Dordrecht: Springer Netherlands, 1987. http://dx.doi.org/10.1007/978-94-009-3505-1_24.

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Simić, Zoran, Ivona Radović, and Mirjana Kijevčanin. "Experimental Determination of Liquid-Liquid Equilibrium Data on Ternary Water Systems." In Experimental Research and Numerical Simulation in Applied Sciences, 183–97. Cham: Springer International Publishing, 2022. http://dx.doi.org/10.1007/978-3-031-19499-3_10.

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Lin, Wang, Xu Dan, Feng Jianxin, Cui Hanlong, Wang Wenhui, and Zhu Yingxi. "Solid-Liquid Equilibria of Ternary Systems UO2(NO3)2 + HNO3 + H2O and UF4 + HF + H2O at 298 K." In Springer Proceedings in Physics, 480–89. Singapore: Springer Nature Singapore, 2023. http://dx.doi.org/10.1007/978-981-99-1023-6_42.

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AbstractUO2(NO3)2 and UF4 are significant intermediates that connect different chemical unit operations (such as dissolution, evaporation, concentration, extraction and etc.) in uranium chemical industry. Commonly, there is a basic physicochemical question about phase equilibrium of ternary systems UO2(NO3)2 + HNO3 + H2O and UF4 + HF + H2O, it is crucial to understand the phase behavior and thermodynamic properties of them with the continuous development of uranium chemical industry. In this study, solid-liquid phase equilibria of ternary systems UO2(NO3)2 + HNO3 + H2O and UF4 + HF + H2O at 298 K were studied by means of isothermal dissolution method, the solubilities and densities of equilibria liquid phase were investigated experimentally for two systems, the composition of equilibria solid phase of system UO2(NO3)2 + HNO3 + H2O at 298 K were determined by Scherinemakers’ wet residue method, and the method of X-ray diffraction was used to determine the composition of equilibria solid phase for system UF4 + HF + H2O at 298 K. Phase diagrams and diagrams of density-composition were constructed for systems UO2(NO3)2 + HNO3 + H2O and UF4 + HF + H2O at 298 K. Results show that there are unique isothermal dissolution curve for two ternary systems, and corresponding crystallization zone are UO2(NO3)2·6H2O and UF4·2.5H2O, respectively.
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Goworek, J., A. Dąbrowski, and A. Nieradka. "Adsorption from Ternary Liquid Mixtures on Porous Silica Gels." In The Kluwer International Series in Engineering and Computer Science, 321–28. Boston, MA: Springer US, 1996. http://dx.doi.org/10.1007/978-1-4613-1375-5_40.

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Aselage, T. L., K. M. Chang, and T. J. Anderson. "Solid-Liquid Equilibrium in Ternary Group III-V Semiconductor Materials." In ACS Symposium Series, 276–96. Washington, D.C.: American Chemical Society, 1985. http://dx.doi.org/10.1021/bk-1985-0290.ch014.

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White, James L., and Kwang-Jea Kim. "Ternary Systems: Polymer Blends plus Liquid Additives and Compatibilizing Agents." In Thermoplastic and Rubber Compounds, 181–99. München: Carl Hanser Verlag GmbH & Co. KG, 2008. http://dx.doi.org/10.3139/9783446418561.006.

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Morales, J., O. A. Moldes, M. A. Iglesias-Otero, J. C. Mejuto, G. Astray, and A. Cid. "Density Prediction of Ternary Mixtures of Ethanol + Water + Ionic Liquid Using Backpropagation Artificial Neural Networks." In Ionic Liquid-Based Surfactant Science, 447–58. Hoboken, NJ: John Wiley & Sons, Inc, 2015. http://dx.doi.org/10.1002/9781118854501.ch21.

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Conference papers on the topic "Ternary liquid"

1

Rogalski, Antoni. "New ternary alloy systems for infrared detectors." In Liquid and Solid State Crystals: Physics, Technology, and Applications, edited by Jozef Zmija. SPIE, 1993. http://dx.doi.org/10.1117/12.156938.

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Fardhyanti, Dewi Selvia, Haniif Prasetiawan, Hermawan, and Lelita Sakina Sari. "Ternary liquid-liquid equilibria for the phenolic compounds extraction from artificial textile industrial waste." In ENGINEERING INTERNATIONAL CONFERENCE (EIC) 2016: Proceedings of the 5th International Conference on Education, Concept, and Application of Green Technology. Author(s), 2017. http://dx.doi.org/10.1063/1.4976877.

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Ginting, Rizqy Romadhona, Asalil Mustain, Rizki Tetrisyanda, Ignatius Gunardi, and Gede Wibawa. "Ternary liquid-liquid equilibria of dimethyl carbonate + 2-propanol + water system at 303.15 and 313.15 K." In INTERNATIONAL CONFERENCE OF CHEMICAL AND MATERIAL ENGINEERING (ICCME) 2015: Green Technology for Sustainable Chemical Products and Processes. AIP Publishing LLC, 2015. http://dx.doi.org/10.1063/1.4938342.

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Sucipto, Retno Kumala Hesti, Kuswandi, and Gede Wibawa. "Ternary liquid-liquid equilibrium for eugenol + tert-butanol + water system at 303.15 and 323.15K and atmospheric pressure." In INTERNATIONAL SEMINAR ON FUNDAMENTAL AND APPLICATION OF CHEMICAL ENGINEERING 2016 (ISFAChE 2016): Proceedings of the 3rd International Seminar on Fundamental and Application of Chemical Engineering 2016. Author(s), 2017. http://dx.doi.org/10.1063/1.4982330.

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Tetrisyanda, Rizky, Kuswandi, and Gede Wibawa. "Liquid-liquid equilibrium measurement of ternary system containing β-caryophyllene in the water and 2-propanol mixture." In INTERNATIONAL CONFERENCE ON ENGINEERING, SCIENCE AND NANOTECHNOLOGY 2016 (ICESNANO 2016). Author(s), 2017. http://dx.doi.org/10.1063/1.4968331.

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Honma, Michinori, Tatsuya Miura, and Toshiaki Nose. "Optical Properties of Liquid Crystal Gratings with Ternary Orientation Domains for Stokes Polarimetry." In Novel Optical Materials and Applications. Washington, D.C.: OSA, 2017. http://dx.doi.org/10.1364/noma.2017.noth1c.4.

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Kossov, Vladimir, Yuri I. Zhavrin, Olga Fedorenko, and Aliya Akzholova. "OCCURRENCE OF CONVECTIVE FLOWS IN TERNARY LIQUID AND GASEOUS MIXTURES UNDER ISOTHERMAL CONDITIONS." In Proceedings of CHT-15. 6th International Symposium on ADVANCES IN COMPUTATIONAL HEAT TRANSFER , May 25-29, 2015, Rutgers University, New Brunswick, NJ, USA. Connecticut: Begellhouse, 2015. http://dx.doi.org/10.1615/ichmt.2015.intsympadvcomputheattransf.410.

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Ginting, Rizqy Romadhona, Asalil Mustain, Ignatius Gunardi, and Gede Wibawa. "Ternary (liquid + liquid) equilibria of (diethyl carbonate + ethanol or 1-propanol + water) systems at 303.15 K under atmospheric pressure." In INTERNATIONAL CONFERENCE ON ENGINEERING, SCIENCE AND NANOTECHNOLOGY 2016 (ICESNANO 2016). Author(s), 2017. http://dx.doi.org/10.1063/1.4968272.

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9

Simić, Zoran. "Analysis of different possibilities for determining tie lines in liquid-liquid equilibria." In 35th International Congress on Process Industry. SMEITS, 2022. http://dx.doi.org/10.24094/ptk.022.319.

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Abstract:
Due to the global trend of increasing environmental pollution, green solvents are being implemented in various branches of the chemical industry to, which would replace standard industrial solvents with harmful characteristics. In order to examine the possibilities of using green solvents, the possibility of appropriate replacement and process design, it is necessary to determine thermodynamic data such as liquid-liquid equilibria, i.e. tie lines in liquid- liquid extraction (LLE), and the corresponding binodal curve. Solubility of components are of great importance for the separation processes (especially for extraction) applied in the chemical industry. Tie lines are a very important thermodynamic data, which are mostly determined by chromatographic analysis depending on the nature of the components in the mixture. Tie lines are mostly determined by chromatographic analysis. Chromatographic analysis is one of the methods that not every laboratory can afford, due to the high cost of the apparatus and high operational costs. In this paper some of the alternative methods for determining tie lines in liquid-liquid equilibria are presented. On the example of the ternary system water+dimethyl adipate+2-propanol, the determination of tie lines via the refractive index and the density of the mixture are shown. These analytical methods are often used in various branches of industry. Based on the obtained results, a mutual comparison of the results obtained through these three methods is performed.
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Parameswari, Zahrida D., Andre M. Kurniawan, Gede Wibawa, and Kuswandi Kuswandi. "Ternary liquid-liquid equilibria of Eugenol + Isobutanol + H2O and β-Caryophyllene + Isobutanol + H2O systems at temperatures 303.15 and 323.15 K." In INTERNATIONAL SEMINAR ON FUNDAMENTAL AND APPLICATION OF CHEMICAL ENGINEERING 2016 (ISFAChE 2016): Proceedings of the 3rd International Seminar on Fundamental and Application of Chemical Engineering 2016. Author(s), 2017. http://dx.doi.org/10.1063/1.4982329.

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