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The densities and viscosities of aqueous blends of N-methyldiethanolamine (MDEA) and 2-amino-2-methyl-1-propanol with monoethanolamine (MEA) and diethanolamine (DEA) have been measured at (25, 30, 35, 40, 45, and 50) °C. The total amine strength in the solution was kept at 30 mass % in view of recent interest in using concentrated amine solutions in gas treating. Correlations for the density and viscosity of the ternary mixtures are presented.

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In this work, the physical solubility of N 2 O in (monoethanolamine + water), (N-methyldiethanolamine + monoethanolamine + water), and (2-amino-2-methyl-1-propanol + monoethanolamine + water) and the diffusivity of N 2 O in (N-methyldiethanolamine + monoethanolamine + water) and (2-amino-2-methyl-1-propanol + monoethanolamine + water) have been measured at (293, 298, 303, 308, and 313) K. For the binary mixture, the amine concentration ranges studied are (2.0, 2.5, and 3.0) kmol‚m -3 . For the ternary mixtures, the total amine strength in the solution was kept at 30 mass %, in view of the recent interest in using concentrated amine solutions in gas treatment. A solubility apparatus was used to measure the solubility of N 2 O in amine solutions. The diffusivity was measured with a wetted wall column absorber. The accuracy of the measurement is estimated to be (2%. A semiempirical model of the excess Henry's constant was used to correlate the solubility of N 2 O in amine solutions. The parameters of the correlation were determined from the measured solubility data. The experimental N 2 O solubility and diffusivity data have been correlated. Comparison with the experimental results indicates that the models for solubility and diffusivity will be useful in estimating the solubility of N 2 O in (MEA + H 2 O), (MDEA + MEA + H 2 O), and (AMP + MEA + H 2 O) as well as the diffusivity of N 2 O in (MDEA + MEA + H 2 O) and (AMP + MEA + H 2 O) solvents. The "N 2 O analogy" is then used to estimate the solubility and diffusivity of CO 2 in the aqueous alkanolamine solutions.

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