The equilibrium distribution of manganese between slag and molten iron has been investigated under three different gas environments. MgO-saturated CaO-FeO-Al 2 O 3 -SiO 2 -MnO (0.2-0.8 wt%)-P 2 O 5 (0.1-0.9 wt%) slags were studied in the temperature range 1550-16008C under CO/CO 2 /H 2 /H 2 O (natural/coal gas, NG/CG), H 2 /H 2 O (H 2 reductant), and CO/CO 2 with pO 2 ¼ 10 À10 to 10 À9 atm. The first two gas mixtures represented the case of using natural or coal gas and hydrogen in the novel flash ironmaking technology. The average L Mn (manganese distribution ratio) was found to be 4, 5, and 6 under CO/CO 2 /H 2 /H 2 O (natural/ coal gas), H 2 /H 2 O (H 2 reductant), and CO/CO 2 , respectively. In other words, L Mn under H 2 and natural/coal gas conditions was 29% and 43% less than under the CO/CO 2 atmosphere. Therefore, water in the gas atmosphere depresses L Mn . When an ore with Mn content of 0.2 wt% is fed into three routes in addition to coke with 0.07 wt% Mn, which was added at the ratio of 0.4 coke-to-hot metal in the case of the CO/CO 2 gas mixture, the hot metal reduced under the CO/CO 2 , NG/CG, and H 2 conditions, is expected to contain 0.13, 0.14, and 0.15 wt% Mn, respectively. That is H 2 and NG/CG are expected to produce hot metal with 17% and 25% more Mn than in the CO/CO 2 conditions. This work has for the first time determined the effect of water vapor on the distribution of Mn between slag and molten iron.