Kinetics and Mechanism of Simultaneous Leaching of Lithium,Rubidium,and Cesium from Lepidolite Smelting Slag
Chinese Journal of Rare Metals | Vol.50, Issue 3, 2026 |
pp. 427-438
Lepidolite smelting slag,a voluminous solid waste generated during lithium extraction
from lepidolite,is produced at an annual rate of millions of tons. These slags still
retain significant amounts of valuable metals,such as lithium (Li),rubidium (Rb),and
cesium (Cs),and therefore possess considerable recovery potential. However,current
approaches to their resource utilization face several challenges:conventional methods
for use in building materials fail to effectively recover the valuable metals contained
in the slag,resulting in resource wastage;meanwhile,existing hydrometallurgical lithium
recovery technologies mainly focus on extracting lithium alone,overlooking the synergistic
recovery of associated metals such as Rb and Cs. Moreover,the dissolution mechanisms
underlying the leaching process remain unclear,which hinders further process optimization.
To address these issues,this study developed a synchronous sulfuric acid leaching
process. The effects of key parameters-including liquid-to-solid ratio,sulfuric acid
concentration,leaching temperature,and leaching time-on the leaching rates of Li,Rb,and
Cs were systematically investigated,and the leaching kinetics and synchronous leaching
mechanisms were explored in depth. The results showed that efficient and synergistic
leaching of Li,Rb,and Cs could be achieved under the following optimal conditions:leaching
temperature of 80 ℃,sulfuric acid concentration of 20%,liquid-to-solid ratio of 5∶1
g·ml−1,and leaching time of 2 h. Under these conditions,the leaching rates of Li,Rb,and
Cs reached 91.72 %,90.40 %,and 93.16 %,respectively. Through systematic product characterization
and kinetic analysis,this study revealed the intrinsic mechanism of the synchronous
leaching process. Sulfuric acid primarily disrupted the crystal structure of silicate
minerals in the lithium slag,releasing occluded Li+,Rb+,and Cs+ ions into the solution. Concurrently,the calcium sulfate surface coating formed during
the reaction played a critical role:it inhibited the inward diffusion of H+ and hindered the outward migration of dissolved metal ions such as Li+,Rb+,and Cs+,especially in the later stages of leaching. Kinetic studies indicated that the leaching
process followed the shrinking core model,with a rate-controlling mechanism governed
by a combination of chemical reaction and internal diffusion. Detailed kinetic analysis
yielded apparent activation energies of 37.759,14.076,and 35.015 kJ·mol-1 for the leaching of Li,Rb,and Cs,respectively. These kinetic parameters offered important
insights into the rate-limiting steps of the process and provide a theoretical foundation
for its further optimization. The synchronous sulfuric acid leaching process developed
in this study offered advantages such as a short flowsheet,simple operation,and high
metal recovery. It presented a practical and feasible technical route for the comprehensive
resource utilization of lepidolite smelting slag. The successful development of this
process not only facilitated the effective recovery of strategic metal resources and
reduced solid waste accumulation but also significantly enhanced resource utilization
efficiency. Furthermore,this study contributed to strengthening China's supply security
for critical strategic metals and promotes the establishment of a high-value recycling
system for metallurgical solid wastes,thereby providing new technical support for
the sustainable development of the metallurgical industry.
DOI: 10.13373/j.cnki.cjrm.XY25100018 Cited: 0 Download: 0
