An efficient recycling process of spent cathode carbon blocks via low temperature molten salt roasting and two stage leaching

烘烤 浸出(土壤学) 熔盐 冶金 阴极 火法冶金 材料科学 碳纤维 过程(计算) 单级 废物管理 化学 环境科学 工程类 物理化学 复合材料 土壤水分 土壤科学 冶炼 航空航天工程 操作系统 复合数 计算机科学
作者
Xiaojun Lv,Xiaoli Sun,Wengang Bu,Xuan Tan,Zhu Jian-zhen,Zexun Han
出处
期刊:Separation and Purification Technology [Elsevier BV]
卷期号:361: 131566-131566 被引量:6
标识
DOI:10.1016/j.seppur.2025.131566
摘要

• Roasting process occurs at air atmosphere due to high ignition temperature of SCC. • Carbon content of the recovered graphite reaches 98.67 wt% • Leaching rate of Al,Na,K,Li,F valuable elements exceeds 97 % • 96.55 % of Al and F were recycled from filtrate in the form of cryolite. • DFT calculations confirm favorable electrochemical properties of recovered graphite. Spent cathode carbon (SCC) as a hazardous solid waste from the aluminum electrolysis industry, contains numerous valuable components, but poses a serious threat to ecological environment. Molten salt roasting is an efficient separation and purification method for SCC than directly leaching of hyfrometallurgy. However, the current treatment of SCC by molten salt roasting is under inert atmosphere and high temperature conditions, which causes high production costs and low product economics. Herein, a low-temperature molten salt roasting process with 550 °C and NaOH additive under air atmosphere-followed by water leaching and acid leaching in turn is proposed to deeply purify SCC. A single-factor optimal experiment indicates that most of the impurities, such as Na 3 AlF 6 , were removed after water leaching and the refractory substances like silica-aluminate, were further transformed by acid leaching, which results in a significant improvement in the purity of the recovered graphite (RG) from 43.55 wt% to 98.67 wt%. DFT calculations confirm that RG have a greater density of states (DOS) near the Fermi energy level and lower migration energy barriers for Li ion, which provides a theoretical foundation for the high-value utilization of RG in anode material for lithium batteries. The primary and second leach filtrates were combined to recover 96.55% fluorine from solution in the form of cryolite under optimum conditions, based on solution equilibrium chemistry calculations of Al and F complexes. The whole process features low cost and environmental protection, and basically completes harmless treatment of SCC and recovery of valuable components.
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