黏土型锂矿悬浮焙烧—酸浸提锂技术研究

Study on Lithium Extraction from Clay−Type Lithium Ore by Suspension Roasting Combined with Acid Leaching

  • 摘要: 随着新能源汽车与储能电池产业快速发展,全球锂资源需求持续攀升;黏土型锂矿储量巨大、开发潜力突出,已成为我国重要锂资源接替方向之一。以某黏土型锂矿浮选精矿为研究对象,采用悬浮焙烧—硫酸浸出工艺开展提锂实验,系统优化焙烧与浸出工艺参数,并通过XRD、TOF−SIMS等表征手段揭示悬浮焙烧活化浸出提锂机理。实验结果表明:在焙烧温度600 ℃、焙烧时间30 min、空气流量700 mL/min,浸出温度80 ℃、硫酸质量浓度20%、液固比4∶1 (mL∶g)、浸出时间90 min的最优条件下,锂浸出率可达90.42%。机理分析显示,焙烧前,锂主要以结构态赋存于锂绿泥石致密的铝硅酸盐晶格之中,受到Si−O、Al−O强共价键及层间结构束缚,Li+活性极低,浸出过程硫酸中的H+难以穿透矿物骨架与晶格中的Li+置换,导致锂浸出困难;经过悬浮焙烧之后,锂绿泥石发生晶格畸变及非晶态转变,层间作用力减弱、层间距扩大,为Li+迁移提供了充足的扩散通道,原本被晶格紧密束缚的结构态锂大量转化为活性更高的游离态与弱结合态,显著增强Li+的活性与离子交换驱动力,从而使锂在酸浸过程更易被H+置换而实现高效浸出,显著提升锂浸出效果。

     

    Abstract: With the rapid development of the new energy vehicle and energy storage battery industries, the global demand for lithium resources continues to climb sharply, as lithium is an essential key raw material for manufacturing high−performance batteries. Clay−type lithium ore, which boasts enormous reserves and remarkable development potential, has become one of the important alternative directions for lithium resources in China, effectively alleviating the contradiction between the increasing demand for lithium and the shortage of traditional lithium ore resources. In this study, flotation concentrate from a certain clay−type lithium ore was selected as the research object, and lithium extraction experiments were carried out by adopting the suspension roasting–sulfuric acid leaching process. A series of single−factor and orthogonal experiments were conducted to systematically optimize the key process parameters of roasting and leaching, including roasting temperature, roasting time, air flow rate, leaching temperature, sulfuric acid concentration, liquid−solid ratio and leaching time. Meanwhile, characterization methods such as X−ray diffraction (XRD) and time−of−flight secondary ion mass spectrometry (TOF−SIMS) were employed to deeply reveal the lithium extraction mechanism of suspension roasting activated leaching. The experimental results show that under the optimal process conditions (roasting temperature of 600 ℃, roasting time of 30 min, air flow rate of 700 mL/min, leaching temperature of 80 ℃, sulfuric acid concentration of 20%, liquid−solid ratio of 4∶1 (mL∶g), and leaching time of 90 min), the lithium leaching efficiency can reach 90.42%. Mechanism analysis shows that before roasting, lithium mainly exists in a structural state within the dense aluminosilicate lattice of lithium−bearing chlorite, constrained by strong covalent Si–O and Al–O bonds as well as interlayer structures. The activity of Li+ is extremely low, making it difficult for H+ in sulfuric acid to penetrate the mineral framework and displace Li+ in the lattice during leaching, thus resulting in poor lithium leaching efficiency.In contrast, after suspension roasting, the crystal lattice of lithium−bearing chlorite undergoes distortion and amorphization, accompanied by weakened interlayer forces and enlarged interlayer spacing, which provide sufficient diffusion pathways for Li+ migration. A large amount of structurally bound lithium originally tightly confined in the lattice is converted into highly active free and weakly bound states, significantly enhancing the reactivity of Li+ and the driving force for ion exchange. Consequently, lithium is more readily displaced by H+ during acid leaching, achieving efficient lithium extraction and greatly improving the leaching performance.

     

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