Equilibrium tie-line in PrOy–BaO–CuO ternary phase diagram around peritectic temperature of Pr1+xBa2−xCu3O7−δ

1998 ◽  
Vol 13 (1) ◽  
pp. 118-125 ◽  
Author(s):  
Minoru Tagami ◽  
Makoto Kambara ◽  
Takateru Umeda ◽  
Yuh Shiohara
Keyword(s):  
Phase Diagram ◽  
Ternary Phase ◽  
Ternary Phase Diagram ◽  
Peritectic Temperature ◽  
Air Atmosphere ◽  
Epma Analysis ◽  
Tie Lines ◽  
Growth Method ◽  
Quantitative Epma ◽  
Tie Line

This paper presents tie-lines between Pr1+xBa2−xCu3O7−δ and liquid on a PrOy –BaO–CuO ternary phase diagram at 965, 970, 975, 980, and 990 °C in air atmosphere, for which knowledge is necessary to fabricate composition controlled Pr1+xBa2−xCu3O7−δ single crystals by the solution growth method. Liquidus faces have been investigated by dipping MgO single crystal rods into the thermal equilibrium melt at various temperatures and analyzing the composition of the adhering melt by ICP. The compositions of Pr1+xBa2−xCu3O7−δ solid solution coexisting with various compositions of liquids were obtained by quantitative EPMA analysis of quenched melts. Tie-lines were calculated by applying the lever rule to these experimental data for solid compositions and liquidus faces. Furthermore, the relationships between solid solubilities and peritectic temperatures of Pr1+xBa2−xCu3O7−δ are reported.

scholarly journals Application of a ternary phase diagram to the liquid-liquid extraction of ethanoic acid using ethyl ethanoate

2019 ◽  
Vol 44 (3) ◽  
pp. 43-49
Author(s):  
Aline Amaral Madeira
Keyword(s):  
Phase Diagram ◽  
Ternary Phase ◽  
Ternary Phase Diagram ◽  
Extraction Process ◽  
Distribution Coefficients ◽  
Liquid Extraction ◽  
Ethanoic Acid ◽  
Liquid Liquid Extraction ◽  
Equilibrium Data ◽  
Tie Lines

This article was elaborated in an approach to the liquid-liquid equilibrium of the extraction process of ethanoic acid (C2H4O2) in aqueous phase using ethyl ethanoate as solvent. The liquid-liquid extraction was modeled by the construction of a ternary phase diagram for the water-ethanoic acid- ethyl ethanoate system with the aid of the Origin software. The equilibrium data were obtained experimentally by titration at room temperature (298.15 K) and atmospheric pressure (101325 Pa) using four mixtures of water, ethanoic acid, and ethyl ethanoate. The determination of the composition of the extract and residue portions in the equilibrium of each mixture by of the tie-lines method allowed to examine the percentages of liquid-liquid extraction achieved. The distribution coefficients and separation factors calculated made it possible an evaluation of the distribution and of the mutual solubility of the solute in the aqueous and organic phases. The results showed a good performance of ethyl ethanoate in the extraction of ethanoic acid for concentrations of solute until 16% of the feed.

Cu titration in CuInSe2: exploration of the ternary phase diagram along new tie-lines

Ionics ◽  
1997 ◽  
Vol 3 (1-2) ◽  
pp. 149-154 ◽  
Author(s):  
M. Jean ◽  
S. Peulon ◽  
J. -F. Guillemoles ◽  
J. Vedel
Keyword(s):  
Phase Diagram ◽  
Ternary Phase ◽  
Ternary Phase Diagram ◽  
Tie Lines

Phase Stability of Molybdenum-Silicon Nitride-Silicon Mis Schottky Diode at High Temperatures

1990 ◽  
Vol 181 ◽  
Author(s):  
Heungsoo Park ◽  
C.R. Helms
Keyword(s):  
Phase Diagram ◽  
Barrier Height ◽  
Schottky Diode ◽  
Ternary Phase ◽  
Schottky Barrier Height ◽  
Ternary Phase Diagram ◽  
Full Range ◽  
P Type ◽  
Tie Line ◽  
Silicon Oxygen

ABSTRACTPreviously our group[1,2] has demonstrated metal-thin insulator- silicon Schottky diode structures which allow the Si Schottky barrier height to be adjusted over nearly the full range of the silicon band gap by appropriate choice of insulator thickness and metal. However, previous attempts to achieve a structure with a high barrier height to p-type that is stable above 400C(using primarily Titanium) have failed. In this paper we report on results for a metal, Molybdenum, which has a stable tie line to Sio2 and Si3N4 in metal-silicon-oxygen(nitrogen) ternary phase diagram which leads to a more stable system.

Using phase boundary mapping to resolve discrepancies in the Mg2Si–Mg2Sn miscibility gap

2021 ◽  
Author(s):  
Rachel Orenstein ◽  
James P. Male ◽  
Michael Toriyama ◽  
Shashwat Anand ◽  
G. Jeffrey Snyder
Keyword(s):  
Phase Diagram ◽  
Phase Boundary ◽  
Ternary Phase ◽  
Ternary Phase Diagram ◽  
Miscibility Gap ◽  
Boundary Mapping

A new understanding of the MgSi–MgSn miscibility gap is reached through phase boundary mapping the Mg–Si–Sn ternary phase diagram.

Calculation of phase diagrams and thermodynamic properties of 14 additive and reciprocal ternary systems containing Li2CO3, Na2CO3, K2CO3, Li2SO4, Na2SO4, K2SO4, LiOH, NaOH, and KOH

1984 ◽  
Vol 62 (3) ◽  
pp. 457-474 ◽  
Author(s):  
A. D. Pelton ◽  
C. W. Bale ◽  
P. L. Lin
Keyword(s):  
Phase Diagram ◽  
Thermodynamic Properties ◽  
Molten Salt ◽  
Phase Diagrams ◽  
Binary Systems ◽  
Ternary Phase ◽  
Ternary Phase Diagram ◽  
Ternary Systems ◽  
Maximum Error ◽  
Critical Assessment

Phase diagrams and thermodynamic properties of five additive molten salt ternary systems and nine reciprocal molten salt ternary systems containing the ions Li+, Na+, [Formula: see text], OH− are calculated from the thermodynamic properties of their binary subsystems which were obtained previously by a critical assessment of the thermodynamic data and the phase diagrams in these binary systems. Thermodynamic properties of ternary liquid phases are estimated from the binary properties by means of the Conformal Ionic Solution Theory. The ternary phase diagrams are then calculated from these thermodynamic properties by means of computer programs designed for the purpose. It is found that a ternary phase diagram can generally be calculated in this way with a maximum error about twice that of the maximum error in the binary phase diagrams upon which the calculations are based. If, in addition, some reliable ternary phase diagram measurements are available, these can be used to obtain small ternary correction terms. In this way, ternary phase diagram measurements can be smoothed and the isotherms drawn in a thermodynamically correct way. The thermodynamic approach permits experimental data to be critically assessed in the light of thermodynamic principles and accepted solution models. A critical assessment of error limits on all the calculated ternary diagrams is made, and suggestions as to which composition regions merit further experimental study are given.

Sign in / Sign up

Export Citation Format

Share Document