Institute for Advanced Materials and Technology, University of Science and Technology Beijing, Beijing 100083, PR China.
Nuclear Chemistry Industrial Material Recycling, Department of Chemistry and Chemical Engineering, Chalmers University of Technology, Gothenburg 41296, Sweden.
Sci Total Environ. 2021 Mar 15;760:143968. doi: 10.1016/j.scitotenv.2020.143968. Epub 2020 Dec 8.
Secondary aluminum dross (SAD) is solid waste of primary aluminum dross extracted aluminum, which contains approximately 40-60 wt% alumina, 10-30 wt% aluminum nitride (AlN), 5-15 wt% salts and other components. The salts include sodium chloride, potassium chloride and fluorine salts. SAD has dual attributes as resource and pollutant. SAD landfill disposal has the disadvantages of occupying land, wasting resources, a high cost and great environmental impact. SAD utilization methods are currently pyrometallurgy and hydrometallurgy. In pyrometallurgy, AlN is oxidized and the salts are evaporated at high temperature. After mixing, molding and calcination, firebricks and ceramics can be manufactured from SAD. In hydrometallurgy, AlN is hydrolyzed and salts are dissolved in water. After dissolving, filtrating, precipitating, washing and calcination, γ-AlO can be prepared from SAD. Resource consumption and emission from both utilization methods were assessed. A ton of magnesium aluminum titanate based ceramics by pyrometallurgy consumes 1043 kg raw materials and releases 69 kg of waste gas, 4.17 t of waste water and no solid waste. A ton of γ-AlO by hydrometallurgy consumes 3389 kg raw materials and releases 111 kg of waste gas, 12.98 t of waste water and 267 kg of solid waste. Therefore, the resource consumption and emission of SAD utilization by pyrometallurgy is lower than that by hydrometallurgy. We should focus on reducing the emission of the three wastes from pyrometallurgy. We are sure that SAD can be utilized for glass ceramics by pyrometallurgy. AlN and salts can be transformed into alumina and glass phases at high temperature with no emission. We should clarify mechanisms for SAD composition adjustment to lower the glass ceramics' melting point, AlN and salts transformed into alumina and glass phases respectively, and nucleation and crystal growth of glass ceramics at high temperature.
二次铝渣(SAD)是从原铝渣中提取铝后产生的固体废物,其中含有约 40-60wt%氧化铝、10-30wt%氮化铝(AlN)、5-15wt%盐和其他成分。盐包括氯化钠、氯化钾和氟盐。SAD 具有资源和污染物的双重属性。SAD 填埋处置存在占地、浪费资源、成本高和对环境影响大等缺点。SAD 的利用方法目前有火法冶金和湿法冶金。在火法冶金中,AlN 在高温下被氧化,盐被蒸发。混合、成型和煅烧后,可由 SAD 制造耐火砖和陶瓷。在湿法冶金中,AlN 水解,盐溶解在水中。溶解、过滤、沉淀、洗涤和煅烧后,可由 SAD 制备γ-AlO。评估了两种利用方法的资源消耗和排放。通过火法冶金生产一吨镁铝钛酸盐基陶瓷消耗 1043kg 原料,排放 69kg 废气、4.17t 废水和无固体废物。通过湿法冶金生产一吨γ-AlO 消耗 3389kg 原料,排放 111kg 废气、12.98t 废水和 267kg 固体废物。因此,火法冶金利用 SAD 的资源消耗和排放低于湿法冶金。我们应该重点减少火法冶金三废的排放。我们确信可以通过火法冶金将 SAD 用于玻璃陶瓷。AlN 和盐在高温下可以转化为氧化铝和玻璃相,没有排放。我们应该阐明 SAD 成分调整机制,降低玻璃陶瓷的熔点,使 AlN 和盐分别转化为氧化铝和玻璃相,以及玻璃陶瓷在高温下的成核和晶体生长。