Table 2. Experimental Matrix for Studied Solutionsa.
Comp 3 | 102 w2 | 102 w3 | b2/m0 | b3/m0 | Properties | Tmin (K) | Tmax (K) | α/αsat |
---|---|---|---|---|---|---|---|---|
– | 29.80 | 0.00 | 6.95 | 0.00 | ρ, η, σ | 298.15 | 343.15 | 0, 0.5, 1.0 |
HEIA | 0.00 | 24.10 | 0.00 | 2.44 | ρ, η | 298.15 | 333.15 | 0 |
HEIA | 0.00 | 48.80 | 0.00 | 7.32 | ρ, η | 298.15 | 353.15 | 0 |
HEIA | 0.00 | 72.80 | 0.00 | 20.59 | ρ, η | 298.15 | 353.15 | 0 |
HEIA | 28.01 | 6.64 | 7.02 | 0.78 | ρ, η, σ | 298.15 | 343.15 | 0, 0.5, 1.0 |
HEIA | 25.87 | 13.78 | 7.02 | 1.75 | ρ, η, σ | 298.15 | 343.15 | 0, 0.5, 1.0 |
HEEDA | 28.00 | 4.00 | 6.74 | 0.56 | ρ, η, σ | 298.15 | 343.15 | 0, 0.5, 1.0 |
OZD | 25.00 | 7.00 | 6.74 | 0.68 | ρ, η, σ | 298.15 | 343.15 | 0, 0.5, 1.0 |
wi denotes mass fraction of component i in the stock solution prior to absorption of CO2, bi denotes the corresponding molality with water as the solvent, m0 = 1 mol kg–1, Tmin and Tmax are the minimum and maximum experimental temperatures, and α/αsat is the approximate degree of CO2 saturation at the solution preparation temperature of (294 ± 1) K. Component 2 is MEA while component 3 is identified in the table.