Mathematical modeling of sulfuric acid leaching of pyrite cinders after preliminary chemical activation

IF 0.8 Q4 METALLURGY & METALLURGICAL ENGINEERING Kompleksnoe Ispolzovanie Mineralnogo Syra Pub Date : 2022-11-28 DOI:10.31643/2023/6445.12
Y. Abikak, B. Kenzhaliyev, H. Retnawati, S. Gladyshev, A. Akcil
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Abstract

Pyrite cinders, waste products of pyrite concentrate processing by firing to produce sulfuric acid, can serve as raw materials for the extraction of precious, ferrous, and non-ferrous metals. The paper considers the possibilities of obtaining non-ferrous metal concentrate from pyrite cinders by sulfuric acid leaching. This operation is one of the stages in the integrated technology. To increase the extraction of non-ferrous metals during leaching, the method of preliminary chemical activation was used. Chemical activation was carried out in a solution containing 40-120 g/dm3 NaНCO3 at temperatures of 90-230 ° C and a duration of 30-300 minutes. Sulfuric acid leaching of pyrite cinder after activation was carried out in H2SO4 solutions with a concentration of 5-20 % at a temperature of 60 ° C, duration of 30 minutes, and pulp density of 33 %. To determine the optimal conditions for the sulfuric acid leaching of pyrite cinders, a mathematical planning method was used, which allows to assess with a high degree of reliability the influence of the main factors (temperature, pulp density, the concentration of the solution NaHCO3 and duration) and predict an increase in the efficiency of the process by analyzing the numerical values of the regression equations. As a result of sulfuric acid leaching of pyrite cinders after preliminary chemical activation under optimal conditions determined by a mathematical model, the extraction of iron and non-ferrous metals into a solution is 10-15% higher than without activation.
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初步化学活化后硫铁矿渣硫酸浸出的数学模型
黄铁矿矿渣是黄铁矿精矿烧制硫酸的废产物,可作为提取贵重金属、黑色金属和有色金属的原料。探讨了用硫酸浸出法从黄铁矿渣中获得有色金属精矿的可能性。该操作是综合技术的一个阶段。为了提高浸出过程中有色金属的提取率,采用了初步化学活化法。化学活化在含有40-120 g/dm3 NaНCO3的溶液中进行,温度为90-230℃,持续时间为30-300分钟。对活化后的硫铁矿渣在浓度为5 ~ 20%的H2SO4溶液中进行硫酸浸出,浸出温度为60℃,浸出时间为30 min,矿浆密度为33%。为了确定硫铁矿渣硫酸浸出的最佳工艺条件,采用数学规划方法,对温度、矿浆密度、NaHCO3溶液浓度和浸出时间等主要因素的影响进行了高可靠性评估,并通过回归方程的数值分析预测了浸出效率的提高。在数学模型确定的最佳条件下,对硫铁矿渣进行初步化学活化后的硫酸浸出,铁和有色金属的提取率比未活化时高10-15%。
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