Grand canonical Monte Carlo simulations are conducted to investigate the adsorption ability of a 3-D graphene sponge (GS) to separate acidic gases from flue gas stream. To assess the adsorption capacity of GS, first, adsorption of pure component flue gas is studied at a temperature of 303 K and varying pressure up to 2.5 bar. Subsequently, the adsorption capacity and selectivity of GS are investigated for a ternary mixture (CO 2 /SO 2 /N 2 ) of flue gas under the same conditions. This study shows that the maximum adsorption capacity of GS for pure component flue gas is observed for SO 2 followed by CO 2 and N 2 . The adsorption uptake decreases with an increase in pore size of GS. At 1 bar, the amount of adsorption of SO 2 and CO 2 are ∼13 mmol/g and ∼2.6 mmol/g, respectively. Upon increasing the average pore size to 20 Å, the excess amount decreases by 56% and 58% for SO 2 and CO 2 , respectively. The adsorption capacities of GS for CO 2 and SO 2 are better than other carbonbased adsorbents except for CNT bundles. In the case of a ternary mixture of N 2 , CO 2 , and SO 2 in the mole ratios of 0.8, 0.15, and 0.05, we found that the adsorption behavior follows the same order as in the pure component flue gas adsorption. However, the adsorption amount decreases significantly from that of pure component adsorption amount in GS. The adsorption amount of SO 2 and CO 2 at postcombustion conditions decreases to 1.3 mmol/g and 0.5 mmol/g, respectively, which further decreases upon increasing the average pore size. Selectivity analysis of adsorption shows that the adsorption selectivity of SO 2 over N 2 is the maximum followed by the selectivity of CO 2 over N 2 and SO 2 over CO 2 . Both selectivity and uptake capacity decreases with increase in average pore size of GS.