1992
DOI: 10.1021/je00006a028
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Densities and viscosities of the ethanolamines

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Cited by 150 publications
(132 citation statements)
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“…These compounds are used for the industries such as the petroleum for the removal of the CO 2 and H 2 S from the petroleum streams, surfactants, detergents, personal-care products, textiles, agricultural products and many others. (1,2) The physical and thermodynamic properties of pure aminoalcohols such as density and viscosity, (3) thermal conductivity (4) and heat capacity (5) have been reported earlier. The densities and excess molar volumes of aqueous solutions, (6)(7)(8)(9) viscosities (10) and excess molar enthalpies of these mixtures (5,(11)(12)(13) have also been studied.…”
Section: Introductionmentioning
confidence: 89%
“…These compounds are used for the industries such as the petroleum for the removal of the CO 2 and H 2 S from the petroleum streams, surfactants, detergents, personal-care products, textiles, agricultural products and many others. (1,2) The physical and thermodynamic properties of pure aminoalcohols such as density and viscosity, (3) thermal conductivity (4) and heat capacity (5) have been reported earlier. The densities and excess molar volumes of aqueous solutions, (6)(7)(8)(9) viscosities (10) and excess molar enthalpies of these mixtures (5,(11)(12)(13) have also been studied.…”
Section: Introductionmentioning
confidence: 89%
“…Data sources for vapor-phase viscosity were not found. Data from several limited liquid-phase data sets at atmospheric pressure (Blanco, Garcia-Abuin, Gomez-Diaz, Navaza, & Villaverde, 2013;R. M. DiGuilio, Lee, Schaeffer, Brasher, & Teja, 1992;J.-H. Song, Park, Yoon, Lee, & Lee, 1996;Yin, Zhu, & Ma, 2016) were used to obtain the coefficients in Table 2.…”
Section: Monoethanolamine (Mea)mentioning
confidence: 99%
“…Data sources for vapor-phase viscosity were not found. Data from several limited liquid-phase data sets at atmospheric pressure (Aguila-Hernandez, Trejo, Garcia-Flores, & Molnar, 2008;Blanco et al, 2013;R. M. DiGuilio, Lee, et al, 1992;Haghtalab & Shojaeian, 2014;Teng, Maham, Hepler, & Mather, 1994) were used to obtain the coefficients in Table 2.…”
Section: Diethanolamine (Dea)mentioning
confidence: 99%
“…(1,2) Densities, excess molar volumes, and excess molar enthalpies of (monoethanolamine, MEA, + H 2 O), (monomethylethanolamine, MMEA, + H 2 O), and (dimethylethanolamine, DMEA, + H 2 O) were studied at T = 298.15 K. (3) Excess molar volumes of aqueous solutions of (MEA + H 2 O), (diethanolamine, DEA, + H 2 O), and (triethanolamine, TEA, + H 2 O) (4) and of (methyldiethanolamine, MDEA, + H 2 O) and (ethyldiethanolamine, EDEA, + H 2 O) (5) were measured from T = (298.15 to 353.15) K. Densities and excess molar volumes of (DMEA + H 2 O) and (diethylethanolamine, DEEA, + H 2 O) were reported at T = (293.15 to 313.15) K. (6) Transport properties of pure ethanolamines (7) and (DEA + H 2 O) and (MDEA + H 2 O) have also been studied. (8) Heat capacities (9) and thermal conductivities (10) (12) and of (monoethylethanolamine,…”
Section: Introductionmentioning
confidence: 99%