Influence of the temperature on the equilibrium phase diagram of the ternary system water + ammonium chloride + 2-propanol at 101.3 kPa

 Experimental determinations at 101.3 kPa of the solid-liquid-liquid-vapor, liquid-liquidvapor, solid-liquid-vapor and liquid-vapor equilibrium for the water + Na2SO4 + 1propanol and 2-propanol ternary systems. Experimental determinations at 101.3 kPa of the solid-liquid-vapor and liquid-vapor equilibrium for the water + K2SO4 + 1-propanol and 2-propanol ternary systems.  Experimental data prediction with UNIQUAC using AQSOL software.

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Study of the liquid-liquid equilibrium for aqueous ternary systems containing choline bitartrate and 1-propanol or 2-propanol at different temperatures and their performances in acetaminophen separation and alcohols recovery

Zafarani-Moattar

Shekaari

Pourbagherian

2020

Fluid Phase Equilibria

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Influence of the temperature on the equilibrium phase diagram of the ternary system water + ammonium chloride + 2-propanol at 101.3 kPa

Abstract: SLLV equilibrium data at the boiling temperature and 101.3 kPa  The lowest temperature at which NH 4 Cl can split water + 2-propanol into two liquid phases is 310.4 K  Extended UNIQUAC have been used to model phase equilibrium including solid

Cited by 6 publications

References 14 publications

Measurements and Thermodynamic Modeling of Solid–Liquid Equilibria Data for the Ternary (KCl + PEG8000 + H2O) System at 288.2, 298.2, and 308.2 K

Measurements and Thermodynamic Modeling of Solid–Liquid Equilibria Data for the Ternary (KCl + PEG8000 + H2O) System at 288.2, 298.2, and 308.2 K

Equilibrium diagram of the water + K2SO4 or Na2SO4 + 1-propanol or 2-propanol systems at boiling conditions and 101.3 kPa

Study of the liquid-liquid equilibrium for aqueous ternary systems containing choline bitartrate and 1-propanol or 2-propanol at different temperatures and their performances in acetaminophen separation and alcohols recovery

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Influence of the temperature on the equilibrium phase diagram of the ternary system water + ammonium chloride + 2-propanol at 101.3 kPa

Abstract: SLLV equilibrium data at the boiling temperature and 101.3 kPa  The lowest temperature at which NH 4 Cl can split water + 2-propanol into two liquid phases is 310.4 K  Extended UNIQUAC have been used to model phase equilibrium including solid

Cited by 6 publications

References 14 publications

Measurements and Thermodynamic Modeling of Solid–Liquid Equilibria Data for the Ternary (KCl + PEG8000 + H2O) System at 288.2, 298.2, and 308.2 K

Measurements and Thermodynamic Modeling of Solid–Liquid Equilibria Data for the Ternary (KCl + PEG8000 + H2O) System at 288.2, 298.2, and 308.2 K

Equilibrium diagram of the water + K2SO4 or Na2SO4 + 1-propanol or 2-propanol systems at boiling conditions and 101.3 kPa

Study of the liquid-liquid equilibrium for aqueous ternary systems containing choline bitartrate and 1-propanol or 2-propanol at different temperatures and their performances in acetaminophen separation and alcohols recovery

Contact Info

Product

Resources

About

Influence of the temperature on the equilibrium phase diagram of the ternary system water + ammonium chloride + 2-propanol at 101.3 kPa