https://doi.org/10.1039/C7RA01352C “Increasing the CO2 partial pressure in the gas feed to the absorber column has two effects on KGCO2aV. First, increasing the CO2 partial pressure can lead to
doi:10.1088/1757-899X/859/1/012011 “The effect of CO2 content in gas phase is the concentration of CO2 in the gas stream after burning the fossil fuel. According to
doi:10.1088/1757-899X/859/1/012011 “For the effect of CO2 initial loading of MEA, it can be found in Figure 3. CO2 initial loading is defined as mole of
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/10.3390/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/10.1016/j.seppur.2020.118193 “Viscosity in water-lean solvents is usually higher than that of aqueous ones. This is particularly true for water-lean solvents with low volatility. Mixtures of
https://doi.org/10.1016/j.seppur.2020.118193 “There are three main factors that help defining the locus of the cross-over point. The first one is amine concentration. Some works have shown
https://doi.org/10.1016/j.seppur.2020.118193 “In terms of pure chemical activity and reaction, shifting from an aqueous to a water-lean solvent seems to consistently depress the solubility of CO2,
https://doi.org/10.1016/j.seppur.2020.117789 “The heat of absorption (−ΔHabs) is another important factor when evaluating absorption systems, as it is an essential part in determining the amount of
https://doi.org/10.1016/j.seppur.2020.118193 “From their inception, water-lean solvents are mixtures of amines with organic solvents that have higher CO2 physical solubility than water. Therefore, there are two important
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