Randomized trial demonstrates efficient separation of aluminum and sodium from acid-roasted slag, suggesting valuable recovery potential.
Acid‐roasting slag, a by‐product generated during the acid roasting process of solid waste (carbon slag) in aluminum electrolysis, has great potential for value recovery. To recover valuable components, a novel process using carbon powder catalytic calcination was proposed to separate aluminum and sodium. Compared to traditional methods, this process catalyzed by carbon powder significantly reduces temperature (by over 200°C) and energy consumption. Experimental results identified optimal parameters for this process: a slag‐to‐carbon ratio of 0.15:1, calcination temperature of 670°C, duration of 2 h, resulting in a conversion efficiency of NaAl(SO 4 ) 2 of 99.8%. The subsequent water leaching step was optimized at an L/S ratio of 10, room temperature, and 2 h, achieving a leaching efficiency of 99.3% for sodium. Additionally, the resulting Na 2 SO 4 was converted into high‐purity sodium sulfide through carbon thermal reduction at a Na 2 SO 4 to carbon ratio of 0.25:1, 750°C for 2 h, with a Na 2 S recovery rate of 97.3%. Overall, the carbonization catalytic calcination process has proven to be an effective method for the clean and efficient resource utilization of waste residue after carbon slag acidification.
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Yao et al. (2026) studied this question.
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