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Oxidative Roasting-Selective Pressure Leaching Process for Rare Earth Recovery from NdFeB Magnet Scrap

机译:从NDFEB磁体废料稀土回收氧化焙烧选择性压力浸出过程

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摘要

To recover rare earths (RE) with low acid consumption and low environmental pollution, selective pressure leaching with hydrochloric acid from roasted NdFeB scrap was explored. The phase evolution of NdFeB scrap during roasting at 800 degrees C as a function of time was confirmed, and after complete oxidation, its phase components consisted of Fe2O3, NdFeO3, and NdBO3. In the selective pressure leaching procedure, the optimal leaching was achieved at 110 degrees C for 30 min, in which the leaching rate of rare earth was 96.27% along with 13.33% of Fe. Subsequently, the effects of the hydrochloric acid dosage, the hydrochloric acid concentration and the particle size of the roasted NdFeB powder on the leaching rate of rare earth were investigated. For leaching at 110 degrees C for 30 min, the leaching of 13.33% Fe2O3 was derived from the Fe2O3 and NdFeO3 phases in the fully oxidized NdFeB scrap. This phenomenon was verified by the leaching of Fe from Fe2O3 of analytical purity and synthetic NdFeO3. Moreover, the leaching of Nd and Fe from the NdFeO3 phase was found to occur simultaneously. The advantages of the selective pressure leaching process using hydrochloric acid for the oxidized NdFeB scrap were comprehensively evaluated.
机译:为了恢复低酸性消耗和低环境污染的稀土(RE),探讨了来自焙烧的NdFeB废料的盐酸的选择性压力浸出。确认在800摄氏度下焙烧时NdFeB废料的相位演化,并在完全氧化后,其相组分由Fe 2 O 3,NdFeO 3和NDBO 3组成。在选择性压力浸出程序中,在110℃下实现最佳浸出30分钟,其中稀土的浸出速率为96.27%,而含量为9​​6.27%,均为13.33%。随后,研究了盐酸剂量,盐酸浓度和焙烧的NdFeB粉末对稀土浸出速率的影响。为了在110℃下浸出30分钟,浸出13.33%Fe 2 O 3的浸出从完全氧化的NdFeB废料中的Fe 2 O 3和NdFeO 3相。通过分析纯度和合成NdFeO3的Fe 2 O 3浸出Fe的浸出来验证这种现象。此外,发现来自NdFeO3相的Nd和Fe的浸出同时发生。综合评价使用盐酸的选择性压力浸出方法的优点。

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