Sodium hydrosulfide (NaSH), which is utilized for recovering rare metals, was synthesized in a laboratory-scale batch reactor by absorbing a simulated flue gas containing H 2 S into NaOH solution. The effects of H 2 S flow rate, NaOH concentration, and reaction time on the synthesis of NaSH were examined. With an increase in the H 2 S flow rate, the absorption ratio, conversion ratio, and total NaSH productivity showed a decreasing tendency. On the other hand, a higher concentration of NaSH could be synthesized with a higher concentration of NaOH. Most of the Na 2 S (the intermediate product) were produced at a pH > 12, and the NaSH synthesis reaction was feasible at a pH 11.5. Contrary to the increased H 2 S flow rate, increased NaOH concentration resulted in an enhanced Na 2 S=NaSH ratio. With a maximum equivalent ratio of NaOH=H 2 S at 0.88, the chemical composition of the product could maintain equilibrium with the highest NaSH concentration and less than 1% weight-to-weight ratio (w/w) Na 2 S concentration.