Formation of carbon nanotubes and microsilica when obtaining crystalline silicon in three-phase electric ore smelting furnaces

M. P. Kuz’min, V. Kondratiev, A. S. Kuz’mina, A. Burdonov, Jiangtao Ran
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Abstract

The volume of silicon waste generated annually in the Irkutsk Region is 20 thousand tons per year, and the volume of waste accumulated in three sludge fields of JSC «Silicon» exceeds 3 million m3. The main type of crystalline silicon production waste is dust from gas cleaning systems of electric ore smelting furnaces. In this regard, this paper studies its chemical composition and the possibilities of using valuable components (amorphous silica, carbon nanotubes (CNT)) included in its composition. The study demonstrates that it is possible to separate this product by flotation into 3 components — sand fraction, flotation tailings enriched in SiO2, and froth enriched in carbon in the form of CNT. The structure of carbon nanotubes was studied and their physical and mechanical properties were determined: elastic modulus (2000 GPa), tensile strength (75 GPa), and thermal conductivity (4000 W/(m·K)). The amount of heat required to obtain 1 kg of CNT in electric ore smelting furnaces was calculated. Based on the material balance of commercial silicon electric smelting, it was found that 153 kg of CNT and 336 kg of flotation tailings are formed per ton of crystalline silicon during the endothermic process. Flotation tailings consist of 75 % amorphous microsilica particles. According to heat effect and Gibbs energy calculations made for amorphous microsilica formation reactions, it was found that all processes are exothermic, and the process of solid silicon carbide particles (2SiC + 3O2 → 2SiO2 + 2CO) oxidation with air oxygen has the highest thermodynamic probability. The economic efficiency of using amorphous silica to produce casting silumins was calculated, and its results clearly demonstrate a quick payback period (6 months), as well as a high level of its profitability (USD 819672).
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在三相电矿熔炼炉中获得结晶硅时碳纳米管和微二氧化硅的形成
伊尔库茨克地区每年产生的硅废物量为2万吨,“硅”合资公司的三个污泥场累积的废物量超过300万立方米。晶体硅生产废弃物的主要类型是电矿石冶炼炉气体净化系统产生的粉尘。在这方面,本文研究了它的化学组成以及在其组成中使用有价值的成分(无定形二氧化硅,碳纳米管(CNT))的可能性。研究表明,该产品可通过浮选分离为砂粒、富SiO2的浮选尾矿和以碳纳米管形式富集碳的泡沫3组分。研究了碳纳米管的结构,测定了其物理力学性能:弹性模量(2000 GPa)、抗拉强度(75 GPa)和导热系数(4000 W/(m·K))。计算了电炉冶炼1千克碳纳米管所需的热量。根据商业硅电熔炼的物料衡算,发现在吸热过程中,每吨晶体硅产生153 kg碳纳米管和336 kg浮选尾矿。浮选尾矿中75%为无定形微二氧化硅颗粒。根据非晶微二氧化硅生成反应的热效应和吉布斯能计算,发现所有过程都是放热的,其中固体碳化硅颗粒(2SiC + 3O2→2SiO2 + 2CO)与空气氧氧化的热力学概率最高。对使用非晶硅生产铸造硅明的经济效益进行了计算,结果清楚地表明投资回收期短(6个月),盈利能力高(819672美元)。
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