https://doi.org/10.1016/j.ccst.2022.100028 ” The effect of solvent concentration on the CO2 removal efficiency of MDEA + KLys, MDEA and MEA solutions is shown in Fig. 8. Download : Download high-res image (171KB)
https://doi.org/10.1016/j.egypro.2017.03.1322 ““
https://doi.org/10.1039/C7RA01352C “In general, increasing the amine concentration causes an increase of the KGCO2aV values. This is because of the availability of an extra amount of amine molecules
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.ijggc.2018.10.008 “Before performing regeneration analysis of CO2-loaded MEA solutions, fresh solutions were first submitted to microwave irradiation to gauge their behaviour to this specific heating
10.1039/C9CP03976G “Simulations were carried out for starting compositions of alkanolamine/water solvent ratios of 30/70 w/w MEA/W and 22.5/77.5 w/w DEAB/W which are typical for the
https://doi.org/10.1021/acs.energyfuels.0c00880 “To better understand the role of N-methyl-2-pyrrolidone in depressing the CO2 absorption capacity of solvents based on diisopropylamine and DEEA, we have assessed the VLE and
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 4 shows the integral heat of absorption obtained for solutions containing mixtures of different diluents and 10 wt % diisopropylamine only at 40 °C. Data
https://doi.org/10.1021/acs.energyfuels.0c00880 “Figure 3 shows the vapor–liquid equilibrium results obtained for solutions containing mixtures of different diluents and 10 wt % of diisopropylamine, at both 40 and 80
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