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

• 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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Publication Details

Journal
Separation and Purification Technology
Published
2025-01-09
DOI
https://doi.org/10.1016/j.seppur.2025.131566
Citations
7
Primary Topic
Extraction and Separation Processes
Type
article
Field-Weighted Citation Impact
4.99

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article

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

Xuan Tan, Wengang Bu, Xiaoli Sun, Zhu Jian-zhen et al.
7 citations
Separation and Purification Technology
Extraction and Separation Processes
4.99
article

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

Xuan Tan, Wengang Bu, Xiaoli Sun, Zhu Jian-zhen, Xiaojun Lv, Zexun Han
article en
7 citations

Abstract

• 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.

Separation and Purification TechnologyVol. 361
Central South University (CN)
Major Science and Technology Projects in Yunnan Province
Openalex Percentile: Top 5%
Extraction and Separation Processes
4.99
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