Study of reaction characteristics and controlling mechanism of chlorinating conversion of cathode materials from spent lithium-ion batteries
Graphical Abstract
Introduction
Lithium transition metal oxide (LTMO) batteries including LiCoO2 (LCO), LiMn2O4 (LMO) and LiNixCoyMn1−x-yO2 (NCM) have occupied the major market share due to their excellent properties (Dunn et al., 2011, Goodenough and Park, 2013). Recently, spent LTMO-type batteries processing has attracted significant attention because it can greatly alleviate the problems of environmental pollution and resource shortage (Li et al., 2010, Xiao et al., 2019). Many promising technologies have been studies to recover metal products from spent LTMO-type batteries to realize the closed-loop process (Fu et al., 2020a, Zhang et al., 2018). Among these technologies, hydrometallurgy is regarded as one of the most competitive technologies of recycling high-purity products ready for the reproduction of new batteries (Fu et al., 2020b, Li et al., 2018). However, heavy use of chemicals in the metal extraction has limited its practical application from the perspective of cleaner production and sustainable development (Xiao et al., 2017).
Great efforts have been made to reduce chemicals consumption in extracting metals from spent LTMO-type batteries. By co-grinding method, waste polyvinyl chloride (PVC) was used to extract lithium (Li) and cobalt (Co) from LCO cathode materials in replacement of traditional leaching agents (Shu et al., 2004). Furthermore, to improve the extracting efficiency and avoid secondary organic pollution, supercritical water technology was reported to obtain over 95% metal extracting efficiencies without releasing toxic chlorinated organics (Liu and Zhang, 2016). Recently, subcritical water treatment was also applied in metal extraction from spent LCO batteries using the thermoplastic materials as chlorinated polyvinyl chloride (CPVC) as the additive (Nshizirungu et al., 2020a). The results indicated that more than 97.69% Li and Co was recycled in single step at 523 K in 60 min. Further study revealed that Ni2+ as the catalyst could accelerate the de-chlorination of CPVC to produce HCl and higher metals extracting rates were realized (Nshizirungu et al., 2020b). Nevertheless, in the metal extracting process, it is still of great interest to develop more applicable technologies for improving the handling capacity and reducing equipment costs.
Chlorinating metallurgy is known as an operable technology which is a traditional industrial method for metal extraction, where chlorine (Cl2), hydrogen chloride (HCl), chlorides (CaCl2, NaCl), and organic chlorides (PVC, CCl4) can be used as the chlorinating agents (Jena and Brocchi, 2008, Manukyan and Martirosyan, 2003). By chlorinating roasting, metals can be efficiently extracted out from metal ores or wastes. However, the production of harmful gases and the introduction of impurities have greatly limited its practical application (Xing et al., 2020). Recently, NH4Cl has been proved as a promising agent to provide NH3 and HCl for metal extraction, reducing environmental hazards and avoiding impurities introduction (Panda et al., 2020). Besides, the spare NH3 and HCl can regenerate as NH4Cl for the reuse. NH4Cl roasting was used by Fan et al. (2019) to recover high-purity products from spent LTMO-type batteries instead of wet-leaching process. According to Qu’s study, the recovered products could be used to regenerate LCO which delivered over 139.8 mAh/g at 0.5 C and kept a 99% capacity retention rate after 100 cycles (Qu et al., 2020). In addition, Xiao et al. (2020) proposed an O-layer cutting mechanism to explain the dry-extraction of metals from spent LTMO-type batteries. In a word, chlorinating technology with NH4Cl as the only additive has been proved as a promising method to replace wet-leaching process of spent LTMO-type batteries processing, and less waste is produced. However, lots of efforts are still needed to realize the practical application of NH4Cl roasting in spent LTMO-type batteries processing.
Until now, little attention has been paid on the in-depth study of chlorinating conversion of cathode materials from spent LTMO-type batteries. In-depth understanding the reaction controlling mechanism is important to the practical application of chlorinating technology. It should be highly noted that kinetic study on chlorinating conversion of spent LTMO-type batteries, has of great significance for increasing main reaction rate, controlling reaction processes, improving conversion efficiency (Ašperger, 2003, Chang et al., 2015). Therefore, the study of reaction controlling mechanism is becoming much necessary to further development of chlorinating technology for spent LTMO-type batteries recovery.
Accordingly, this study aims to investigate the thermal transformation mechanism of cathode materials from spent LTMO-type batteries. In previous works, the chlorinating conversion of cathode materials from LCO and LMO batteries was studies in detail and the results showed that three types LTMO batteries had similar properties in the processing (Xiao et al., 2021, Xiao et al., 2020). Therefore, NCM materials were chosen as the experimental materials in this study. Roasting and thermogravimetric analysis (TGA) experiments were first performed for the determination of chlorination reaction. The iso-conversional method was then applied to conduct the kinetic analysis. Finally, the reaction models and reaction controlling mechanisms were determined to better understand the chlorinating conversion.
Section snippets
Materials
During the chlorination conversion process, no obvious differences were observed between real cathode materials and chemical cathode materials (Xiao et al., 2021, Xiao et al., 2020). Therefore, chemical NCM cathode materials (which were easier to obtain) were chosen as the experimental materials. NCM cathode materials were obtained by SaiBo Electrochemical Material Network on TaoBao.com, and NH4Cl powders (A.R, 99.5%) were obtained from Sinopharm Chemical Reagent Co.Ltd. The experimental
Chlorinating reaction determination
As shown in Eq. (6), NH4Cl has been proved as a promising reagent to provide NH3 and HCl gases for the chlorination reaction (Itoh et al., 2009, Terakado et al., 2010). Theoretically, the chlorinating process of NCM was a weight increasing process as Eq. (8), and the increment was 132.49%. However, as shown in Fig. 1a, the weight change of mixed powders was mainly attributed to the
Conclusion
We studied the thermal transformation of NCM chlorination based on roasting experiments and kinetic analysis, to better understand its reaction controlling mechanisms. The roasting and TGA experiments were first conducted to determinate reaction interval of NCM chlorination with 10 K/min heating rate. Then, the iso-conversional method based on the TGA experiments was applied to calculated the kinetic parameters such as apparent activation energy (E), pre-exponential factor (A), and mechanism
CRediT authorship contribution statement
Jiefeng Xiao designed and conducted the experiments, and wrote the original manuscript. Ruitong Gao and Bo Niu provided the experimental materials, and participated in data analysis and manuscript revision. Zhenming Xu designed the research project, provided the funding, and supervised the experiments and manuscript preparation.
Declaration of Competing Interest
The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.
Acknowledgment
This work was supported by the National Natural Science Foundation of China (51534005). We express gratitude to Instrumental Analysis Center of SESE and SJTU for technical support.
Associated content
Data processing and analyzing; Detail information of tube furnace; Table S1 presented the main chemical compositions of NCM powders; Table S2 presented the common reaction models for thermal transformation in solids.
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