scholarly journals Phase diagrams in ternary systems poly(oxyethylene) hexadecyl ether-1-hexanol-water.

1986 ◽  
pp. 629-632 ◽  
Author(s):  
Norio WATANABE ◽  
Mitiko SUZUKI ◽  
Takashi INO
1984 ◽  
Vol 62 (3) ◽  
pp. 457-474 ◽  
Author(s):  
A. D. Pelton ◽  
C. W. Bale ◽  
P. L. Lin

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.


1987 ◽  
Vol 70 (2) ◽  
pp. 178-184 ◽  
Author(s):  
F. Weitzer ◽  
J.C. Schuster

Author(s):  
A. V. Frolkova ◽  
M. A. Ablizin ◽  
M. A. Mayevskiy ◽  
A. K. Frolkova

An approach to the determination of free variables required for calculating the material balance of the flowsheet of ternary mixtures separation is presented. Phase diagrams of the considered ternary systems are characterized by the presence of a two-phase splitting area and by the presence of different amounts of azeotropes (classes 3.1.0, 3.1.1, 3.2.1 and 3.3.1). For all the systems flowsheets containing three rectification columns and a florentine vessel for separation were suggested. The multivariance of the solution of the balance problem was shown. The approach was illustrated by the example of real ternary systems characterized by different phase diagrams (methanol - chloroform - water, butyl alcohol - water - toluene, nitromethane - hexane - water). The parameters of the rectification columns were presented.


2018 ◽  
Vol 93 ◽  
pp. 20-29 ◽  
Author(s):  
Lilong Zhu ◽  
Changdong Wei ◽  
Liang Jiang ◽  
Zhanpeng Jin ◽  
Ji-Cheng Zhao

2009 ◽  
Vol 54 (8) ◽  
pp. 1323-1328
Author(s):  
A. K. Pyartman ◽  
V. A. Keskinov ◽  
P. V. Zaitsev ◽  
N. A. Charykov

2016 ◽  
Vol 61 (1) ◽  
pp. 75-78
Author(s):  
A. Dezső ◽  
G. Kaptay

A general form of material balance equations to be used to calculate quasi-binary sections of multi-component phase diagrams is derived here. When this general equation is reduced to ternary systems, it coincides with those, given in the Thermo-Calc manual. For a k-component system, altogether only (k-2) such independent equations should be written from the list of k(k-1)/2 possible equations.


2001 ◽  
Vol 185 (1-2) ◽  
pp. 275-293 ◽  
Author(s):  
B.E. Garcı́a-Flores ◽  
G. Galicia-Aguilar ◽  
R. Eustaquio-Rincón ◽  
A. Trejo

1986 ◽  
Vol 40a ◽  
pp. 247-256 ◽  
Author(s):  
Krister Fontell ◽  
Andrea Ceglie ◽  
Björn Lindman ◽  
Barry Ninham ◽  
C. J. Nielsen ◽  
...  

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