Equilibrium solubility of CO 2 in aqueous blends of 0.23 mol/kg piperazine (PZ) + 0.92 mol/kg 2-diethylaminoethanol (DEAE), 0.52 mol/kg PZ + 2.08 mol/kg DEAE, 0.92 mol/kg PZ + 3.68 mol/kg DEAE, and 1.49 mol/kg PZ + 5.96 mol/kg DEAE in the low pressure region of 0.1–65 kPa and at temperatures of 303.15–323.15 K is reported in the present article. A thermodynamic model is developed, which correlates the experimentally generated data on CO 2 solubility in the newly proposed blend with an excellent agreement. Density and viscosity of DEAE + PZ + H 2 O have been measured at temperatures of 303.1–323.1 K and total amine mass percentage in all the blends are kept constant at 0.3. The mass % ratios of PZ/DEAE considered for measurements were 3:27, 6:24, 9:21, and 12:18. p K a of aqueous DEAE solution are reported in 298.15–333.15 K temperature range. Generated density data are correlated using Redlich–Kister equation, Grunberg and Nissan, and Gonzalez-Olmos, and Iglesias type models and viscosity data are correlated using Grunberg and Nissan model.
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Adak et al. (2017) studied this question.
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