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- W767589191 abstract "In this study, computer simulation works have been performed for the capture process of the and gases contained in the effluent stream using methanol aqueous solution. In order to increase the solubilities of the and in the methanol aqueous stream, the operating pressure of the absorber was raised to 30 bar and the feeding temperature of the solvent was lowered to by using refrigeration cycle. NRTL liquid activity coefficient model was used to estimate the liquid phase nonidealities for methanol and water. Soave-Redlich-Kwong equation of state was used for the vapor phase nonidealities. Henry's law option was also used to calculate the solubilities of the supercritical noncondensible gases into the methanol aqueous solvent stream." @default.
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- W767589191 date "2008-01-01" @default.
- W767589191 modified "2023-09-23" @default.
- W767589191 title "A Study on the Thermodynamic Analysis and the Computer Simulation for the $CO_2$ and $H_{2}S$ Capture Process Using Methanol as a Solvent" @default.
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