https://doi.org/10.1016/j.egypro.2017.03.1298 “Primary and secondary amines form carbamates from their reaction with carbon dioxide. Fig . 9 shows equilibrium constant values for monoethanolamine and diethanolamine. Literature
https://doi.org/10.1016/j.egypro.2017.03.1322 ““
https://doi.org/10.1016/j.egypro.2017.03.1322 ““
https://doi.org/10.1039/C7RA01352C “Another other key parameter is liquid temperature, which can have an effect on KGCO2aV, the reaction kinetic, and equilibrium solubility. According to the Arrhenius equation,88 the
https://doi.org/10.1016/j.petlm.2016.11.002 “An aqueous 30 wt% MEA solution was first loaded with CO2 via an initial absorption step with an inlet gas stream of 20% CO2 balanced by N2 (this CO2 composition
https://doi.org/10.1016/j.ijggc.2018.10.008 “From these loaded solutions, microwave regenerations were performed at three different temperatures: 70, 80 and 90 °C and the CO2 desorption curves are reported in Fig. 4.”
https://doi.org/10.1088/1757-899X/859/1/012010 “Figure 3 represents the solubility of CO2 in each amine solution at the partial pressure of CO2 from 5 to 100 kPa and temperature
https://doi.org/10.1021/acs.energyfuels.0c00880 “In Table 2, one can see that Henry’s coefficients of the water-lean solvents containing NMP are statistically indistinct from those of the pure organic solvent. This
https://doi.org/10.1021/acs.energyfuels.0c00880 “The integral heat of absorption of NMP + DEEA 10 wt % at 40 °C shown in Figure 7 is also comparable to that of physical solvents
https://doi.org/10.1021/acs.energyfuels.0c00880 “Figure 6 shows the vapor–liquid equilibrium results obtained for solutions containing mixtures of different diluents and 10 wt % of N,N-diethylethanolamine, at both 40 and 80 °C.
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