
CO2 absorption curves for various MEA concentrations
https://doi.org/10.1016/j.ijggc.2018.10.008 “First, the solutions were loaded with CO2 until a low absorption rate was achieved as it can be seen in Fig. 3. The obtained rich loadings

https://doi.org/10.1016/j.ijggc.2018.10.008 “First, the solutions were loaded with CO2 until a low absorption rate was achieved as it can be seen in Fig. 3. The obtained rich loadings

https://doi.org/10.3390/en14206822 “The CO2 absorption of blended PZ-MPDL solvent was experimentally measured in terms of CO2 loading (mol CO2/mol amine). This CO2 absorption performance indicator is widely used in the

https://doi.org/10.3390/en14206822 “In this study, the physical diffusivity of CO2 in blended PZ-MPDL solvent was calculated based on the modified Stokes–Einstein equation as Eq. (9) [15] through the dynamic viscosity

https://doi.org/10.3390/en14206822 “Viscosity of blended PZ-MPDL aqueous solution was experimentally determined over temperatures and PZ/MPDL concentration ratios of 313–333 K and 5/25–15/15 %wt., respectively. The viscosity data are

https://doi.org/10.3390/en14206822 “Density of blended PZ-MPDL aqueous solution was measured over ranges of temperatures (313, 323, and 333 K) and PZ/MPDL concentration ratios (5/25, 10/20, and

https://doi.org/10.1016/j.egyr.2021.07.056 “Typical reactive solvents used for capturing CO2 are amines such as monoethanolamine (MEA), diethanolamine (DEA), triethanolamine (TEA), N-methyldiethanolamine (MDEA), 2-amino-2-methyl-1-propanol (AMP), and piperazine (PZ). Among these amines,

https://doi.org/10.1002/ghg.2059 “IC of MDEAH+ and TEAH+ The IC of MDEAH+ and TEAH+ are summarized in Table 3. The IC and absolute value of electric charge of OH− and HCO3− involved Eqns

https://doi.org/10.1002/ghg.2059 “With CACchem and total absorption time obtained in the two systems, CACchem per unit time, termed as OAR, was calculated and they are shown in Fig. 4.

https://doi.org/10.1002/ghg.2059 “The chemical CO2 absorption capacity (CACchem; mol CO2·L−1 solution) and amine utilization (mol CO2·mol−1 amine) of the low- (0.1–0.5 M) and high- (15.0–30.0 wt%) concentration MDEA and

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
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