In this work, we present new results for heat capacities of aqueous mixtures of diethanolamine with N-methyldiethanolamine over the temperature range (303.2 to 353.2) K with a differential scanning calorimeter. For mole fractions of water ranging from 0.2 to 0.8, 16 concentrations of the (DEA + MDEA + water) systems were investigated. For the binary system, (DEA + MDEA), heat capacities of nine concentrations were also measured. A Redlich Kister-type equation for representing excess molar heat capacity was applied to correlate the measured Cp of aqueous alkanolamine solutions. For a total of 176 data points for the (DEA + MDEA + water) system, the overall average absolute percentage deviation of the calculations are 16.5% and 0.2% for the excess molar heat capacity and the molar heat capacity, respectively. The heat capacities presented in this study are, in general, of sufficient accuracy for most engineeringdesign calculations.
Compounds
#
Formula
Name
1
C5H13NO2
N-methyldiethanolamine
2
C4H11NO2
diethanolamine
3
H2O
water
Datasets
The table above is generated from the ThermoML associated json file (link above).
POMD and RXND refer to PureOrMixture and Reaction Datasets. The compound numbers are included in properties, variables, and phases, if specificied;
the numbers refer to the table of compounds on the left.
Type
Compound-#
Property
Variable
Constraint
Phase
Method
#Points
POMD
1
2
Excess molar heat capacity, J/K/mol ; Liquid
Temperature, K; Liquid
Mole fraction - 2; Liquid
Pressure, kPa; Liquid
Liquid
Large sample (1 g) DSC
99
POMD
1
2
Molar heat capacity at constant pressure, J/K/mol ; Liquid
Temperature, K; Liquid
Mole fraction - 2; Liquid
Pressure, kPa; Liquid
Liquid
Large sample (1 g) DSC
99
POMD
1
2
3
Molar heat capacity at constant pressure, J/K/mol ; Liquid