A comprehensive thermodynamic investigation of water–ethanolamine mixtures at 10, 25, and 40 °C
TLDR
The density, isobaric specific heat capacity, and isentropic compressibility of water-ethanolamine (W-EA) mixtures have been measured at three temperatures (10, 25, and 40 °C) over the entire compo...Abstract:
The density, isobaric specific heat capacity, and isentropic compressibility of water–ethanolamine (W–EA) mixtures have been measured at three temperatures (10, 25, and 40 °C) over the entire compo...read more
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Thermodynamic modeling for CO2 absorption in aqueous MEA solution with electrolyte NRTL model
TL;DR: In this paper, the authors used the Electrolyte Nonrandom Two-Liquid activity coefficient model to develop a rigorous and thermodynamically consistent representation for the MDEA−H2O−CO2 system.
Journal ArticleDOI
Densities, excess molar volumes, and partial molar volumes for binary mixtures of water with monoethanolamine, diethanolamine, and triethanolamine from 25 to 80°C
TL;DR: This article measured densities of binary mixtures of water with monoethanolamine (MEA), diethanolamine (DEA), and triethanolamines (TEA) over the full range of compositions and over the temperature range from 25 to 80°C.
Journal ArticleDOI
Volumetric properties of (water + diethanolamine) systems
TL;DR: In this paper, the partial molar volumes and their derivatives with respect to temperature have been used for extending the understanding of molecular interactions in completely miscible (water + organic) systems.
Journal ArticleDOI
Density of Water (1) + Monoethanolamine (2) + CO2 (3) from (298.15 to 413.15) K and Surface Tension of Water (1) + Monoethanolamine (2) from (303.15 to 333.15) K
TL;DR: In this paper, a third-order Redlich-Kister equation and a linear relationship with the temperature was used to measure surface tension of CO2 loaded aqueous MEA solutions at temperatures from (298.15 to 413.15) K.
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