“…These strategies include (i) lowering the input of alkalis, [1,2,4,8,12,[20][21][22] (ii) maximizing the quality of sinter and coke, [20] (iii) charging coarse dunite as an alkali removal agent, [28] (iv) increasing the slag rate, [17,21] and (v) altering the slag composition. [4,[7][8][9]17,[19][20][21][22]29] In addition, less realistic suggestions for modern BF ironmaking have been proposed and operated, such as charging CaCl 2 as an alkali cleaner [20][21][22] and reducing in-plant recycling via the sinter. [20] The effect of lowering the input of alkalis into the BF is significant, e.g., the thermodynamic model developed by Chen et al [12] suggested that increasing the potassium or sodium load by 1 kg/tHM results in an increased circulating load by 27.7 and 15.5 kg/tHM, respectively.…”