Adsorption is one of the most promising methods for gaseous mercury (Hg 0 ) uptake from industrial flue gas, and the designing and synthesis of a sorbent are of significance for utilization. However, for a pilotscale experiment, the macrodynamics, adsorption kinetics, and thermodynamics should be optimized before real applications. This study designed a scale-up fixed-bed reaction unit that worked with CuS-coated Al 2 O 3 sorbent to investigate the influence of the gaseous diffusion, particle size, and wall effect on Hg 0 removal performances. The results showed that the lower gas flow rate enhanced the mercury removal efficiencies. The combination of CuS/Al 2 O 3 (1−2 mm) and a reaction tube (20 mm) mitigated the influence of size and wall effects, which maintained nearly complete mercury removal over 10 h under at 80 °C and had the average adsorption rate of 0.6 μg g −1 min −1 . Moreover, CuS/Al 2 O 3 possessed a higher SO 2 resistance under a 1%− 6% concentration range, guaranteeing a real application under SO 2 -rich industrial gas. The Hg 0 adsorption was controlled by external diffusion processes based on the kinetic analysis. The negative ΔG (−30.71 to approximately −38.93 kJ mol −1 ), positive ΔS (123.39−138.80 J (mol K) −1 ), and positive ΔH (5.65−12.86 kJ mol −1 ) inferred the spontaneous, irreversible, and endothermic progress of Hg 0 adsorption. The above key parameters have guiding significance for sorbent preparation and bed design in subsequent expanded applications.