https://doi.org/10.1016/j.seppur.2021.118959 ” Fig. 3(a) shows the optimization results considering only the performance of the FG-WW column and of the NH3 desorber, in the plane ωFG−WW–PrFG−WW: Greater NH3 concentration in
https://doi.org/10.2516/ogst/2013160 “Table 2 lists the solvent regeneration energies reported in the literature. The regeneration energies refer to the heat requirement for regeneration of solvents (reboiler
https://doi.org/10.1016/j.seppur.2021.118959 ” Table 8 shows the operating conditions that minimize the specific equivalent work of the overall capture process, ω, for the most representative advanced configurations aiming at
https://doi.org/10.1016/j.seppur.2021.118959 ” The NH3 capture process was analyzed for different mass concentrations of 2, 5, 7, and 15% respectively, comparing the results with the CO2 capture reference
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