Study of CO2 removal in natural gas process using mixture of ionic liquid and MEA through process simulation

Abstract There has been a shift to less carbon intensive fuels such as natural gas to meet energy demand due to increasing pressure to cut CO 2 emissions. This has prompted a need to assess unconventional and contaminated natural gas reserves (which contains CO 2 concentration of 20 mol% or more). The CO 2 capture process with MEA as the solvent is mostly adopted to treat contaminated natural gas. In this study, the option of using a blend of ionic liquids (IL) and MEA as a promising solvent in the process was investigated through modelling and simulation. A detailed rate-based model was developed for both MEA (30 wt%) solvent and IL (30 wt%)-MEA (30 wt%) blend using Aspen Plus® to assess both process and economic performances. The 1-Butylpyridinium ([bpy][BF 4 ]) ionic liquid was selected in this study. The physiochemical properties of [bpy][BF 4 ], predicted using Aspen Plus®, showed good accuracy compared with experimental data. The results from this study showed about 15% and 7.44% lower energy consumption in the reboiler duty and CO 2 removal cost respectively with aqueous [bpy][BF 4 ]-MEA solvent compared to 30 wt% MEA solvent. It is concluded that the aqueous [bpy][BF 4 ]-MEA solvent is therefore a promising solvent that could replace 30 wt% MEA solvent in this process.