Phase Equilibrium for the Aqueous Ternary Systems NH4+, Sr2+ (Ca2+)//Cl−–H2O at T=298 K

2018 ◽  
Vol 51 (7) ◽  
pp. 551-555 ◽  
Author(s):  
Lin Wang ◽  
Xudong Yu ◽  
Maolan Li ◽  
Xinglong Cheng ◽  
Xiongjun Tang ◽  
...  
Keyword(s):  
Phase Equilibrium ◽  
Ternary Systems

Detailed calculation of complex fluid phase equilibrium sections for ternary systems

2017 ◽  
Vol 130 ◽  
pp. 399-414
Author(s):  
Gerardo O. Pisoni ◽  
Martín Cismondi ◽  
Marcelo S. Zabaloy ◽  
Lucio Cardozo-Filho
Keyword(s):  
Phase Equilibrium ◽  
Fluid Phase ◽  
Ternary Systems ◽  
Detailed Calculation ◽  
Fluid Phase Equilibrium ◽  
Complex Fluid

scholarly journals Two-phase equilibrium in binary and ternary systems II. The system methane-ethylene III. The system methane-ethane-ethylene

1940 ◽  
Vol 176 (964) ◽  
pp. 140-152 ◽  
Keyword(s):  
Phase Equilibrium ◽  
Ternary System ◽  
Binary Systems ◽  
Ternary Systems ◽  
Two Phase ◽  
Composition Diagram ◽  
Wide Range ◽  
Binary And Ternary Systems

The liquid-vapour equilibrium of the system methane-ethylene has been determined at 0, -42 , -78, -88 and -104° C over a wide range of pressures and the results are shown on a pressure-composition-temperature diagram and by a series of pressure-composition curves. The liquid-vapour equilibrium of the ternary system methane-ethane-ethylene has been determined at -104, -78 and 0° C. Values for the two binary systems methane-ethane and methane-ethylene and for the ternary system methane-ethane-ethylene are shown on a composite pressure-composition diagram.

Phase equilibrium of PVAc + CO2 binary systems and PVAc + CO2 + ethanol ternary systems

2018 ◽  
Vol 458 ◽  
pp. 264-271 ◽  
Author(s):  
Teng Zhu ◽  
Houjian Gong ◽  
Mingzhe Dong ◽  
Zehao Yang ◽  
Chunqing Guo ◽  
...  
Keyword(s):  
Phase Equilibrium ◽  
Binary Systems ◽  
Ternary Systems

scholarly journals Two-phase equilibrium in binary and ternary systems - IV. The thermodynamic properties of propane

1940 ◽  
Vol 176 (965) ◽  
pp. 280-294 ◽  
Keyword(s):  
Phase Equilibrium ◽  
Thermodynamic Properties ◽  
Low Temperatures ◽  
Ternary Systems ◽  
Two Phase ◽  
Thermal Data ◽  
Binary And Ternary Systems

Existing physical and thermal data relative to propane have been summarized and correlated, and some new experimental determinations of pressure-volume-temperature relationships for the liquid at low temperatures have been carried out to make good deficiencies in the literature. On the basis of the information thus obtained the entropy and enthalpy of propane have been calculated for conditions of temperature between — 80 and 200° C, and at pressures of from 0.1 to 200 atm. The results are tabulated and also presented graphically on a temperature base.

Two-phase equilibrium in binary and ternary systems - V. Carbon dioxide-ethylene - VI. Carbon dioxide-propylene

1951 ◽  
Vol 209 (1096) ◽  
pp. 1-14 ◽  
Keyword(s):  
Carbon Dioxide ◽  
Phase Equilibrium ◽  
Ternary Systems ◽  
Two Phase ◽  
Plait Point ◽  
Composition Data ◽  
Binary And Ternary Systems ◽  
Critical Constants

The pressure-temperature-composition data for liquid-vapour equilibrium in the systems carbon dioxide-ethylene and carbon dioxide-propylene are given; the former system is shown to form a series of azeotropes. The plait-point curves and critical constants for the two series of mixtures have been determined.

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