In response to the development of low-carbon smelting technology, reducing the use of fluor-containing materials in desulfurizers is an important research topic. The development of new-generation KR (Kambara Reactor) desulfurizers is shifting towards a higher Al
2O
3 content rather than CaF
2, yet there is currently an absence of thorough and comprehensive mechanisms for desulfurization. Consequently, this research provides an extensive comparison using a specially constructed small-scale KR desulfurization hot model test, alongside FactSage simulation and SEM analysis (of desulfurization process). The findings indicate that at 1400 °C, for the desulfurization of molten iron, the capacity for desulfurization initially increases and then diminishes as the Al
2O
3 content in the KR desulfurizer rises. With Al
2O
3 content in the desulfurizer below 22 wt.%, the phase composition predominantly consists of C
3A, employing a solid
(slag)–liquid
(metal) diffusion method for desulfurization. The optimal desulfurization capacity (Ls: 64.1) is observed when the Al
2O
3 content is 15 wt.%, attributed to the simultaneous presence of CaO particle precipitation and C
3A. However, as the Al
2O
3 content reaches 20 wt.%, all the oversaturated CaO integrates into C
3A, leading to a reduction in Ls from 64.1 to 10.7, thereby diminishing the desulfurization capacity by approximately sixfold. When Al
2O
3 exceeds 22 wt.%, the phase composition transitions from the C
3A to C
12A
7 phase, and the desulfurization approach shifts from solid
(slag)–liquid
(metal) to liquid
(slag)–liquid
(metal) diffusion, with Ls decreasing to 23.4. This reduction is due to C
12A
7’s lower sulfur capacity compared to C
3A and the absence of saturated CaO particle precipitation. Therefore, for Al
2O
3 to effectively replace fluorite in KR desulfurizers, a higher presence of C
3A phases and CaO particle precipitation are essential. The desulfurizer must contain over 65 wt.% CaO and maintain A
l2O
3 levels at 10~16.2 wt.%.
Full article