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. 2024 May 9;69(10):3435–3449. doi: 10.1021/acs.jced.4c00077

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
a

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.