https://doi.org/10.1155/2015/965015 ” Figure 3 depicts the CO2 molar concentration of the gas phase stream at the inlet and outlet of the bubbler. It shows that, at an inlet
https://doi.org/10.1016/j.petlm.2016.11.002 “Due to the continuous and cyclic nature of a conventional MEA stripping process, the aim is to operate at a high working capacity over
https://doi.org/10.1016/j.petlm.2016.11.002 “Many researchers have measured the equilibrium properties of the CO2-MEA-H2O system at different thermodynamic conditions, observing a relatively high solubility even at low CO2 partial
https://doi.org/10.1016/j.petlm.2016.11.002 “Desorption rate provides an indication of how fast a CO2 rich amine solution can release the already absorbed CO2 at moderate or high temperatures (80–120 °C). Some
https://doi.org/10.1016/j.petlm.2016.11.002 ” Absorption rate and absorption capacity are desired properties of an optimized blended aqueous amine solution. Absorption rate determines the amount of absorbed CO2 per liter
https://doi.org/10.1088/1757-899X/859/1/012010 “The cyclic capacity is clarified as the difference in CO2 solubility at the absorption and regeneration conditions [9]. The CO2 loading is derived from
https://doi.org/10.3390/en14206822 “Figure 3 shows the characteristic curves obtained during the CO2 capture testing using EDA. Figure 3a depicts the drop in pressure as a function of time. The
https://doi.org/10.3390/en14206822 “Figure 2 shows the typical curves obtained during the CO2 solubility tests. Figure 2a represents the drop in pressure as a function of time, where the pressure
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