The main goal of traditional methods for sweetening natural gas (NG) is to remove hydrogen sulfide (HS) and significantly lower carbon dioxide (CO). However, when NG processes are integrated into the carbon capture and storage (CCS) framework, there is potential for synergy between these two technologies. A steady-state model utilizing a hybrid solvent consisting of -methyl-2-pyrrolidone (NMP) and monoethanolamine (MEA) has been developed to successfully anticipate the CO and HS capture process from NG.
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