用硝酸从荧光灯荧光粉中浸出钇和铕:动力学及优化

IF 1.5 Q3 GEOSCIENCES, MULTIDISCIPLINARY
T. Huynh, V. Ha, Minh Trang Vu
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引用次数: 2

摘要

稀土元素是公认的最关键的元素之一,对可持续能源技术、激光、电子、合金、催化剂和其他应用的发展至关重要。然而,为了满足日益增加的需求以确保这些基本用途,初级来源的稀土供应是有限的。因此,从二级资源(如被称为电子废物的废弃电气和电子设备)中回收稀土至关重要。这类废物中的荧光灯由于含有大量稀土元素而受到特别关注。本文讨论了一种有潜力的湿法冶金方法——硝酸浸出法从荧光灯废液中回收稀土(钇和铕)。考察了酸浓度、温度等因素对浸出效果的影响。为了提高这些金属的浸出率,专门研究了碱性熔融的影响。基于缩核模型研究了直接浸出和碱性熔融辅助浸出两个过程的动力学。直接浸出时,金属的溶解受表面化学反应控制,在303 ~ 333 K的温度范围内,钇和铕的表观活化能分别为43.9和48.1 kJ/mol。预处理即碱熔将后续浸出机制转变为扩散控制,在相同温度范围内,两种金属的表观活化能分别为7.4和9.5 kJ/mol。采用基于中心复合设计(CCD)的响应面法(RSM)对碱融合辅助酸浸工艺进行了优化。在碱/荧光粉质量比为0.65 g/g、温度为1223 K、反应时间为7200 s的碱熔条件下,再进行酸浸(硝酸浓度为3.5 M、温度为323 K、矿浆密度为30 g/L、浸出时间为1200 s),钇和铕的浸出率分别为92.6%和99.5%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Leaching of yttrium and europium from fluorescent lamp phosphor powder using nitric acid: kinetics and optimization
ABSTRACT Rare earth elements (REEs) are recognized as one of the most critical elements and considered essential for the development of sustainable energy technologies, lasers, electronics, alloys, catalysts, and other applications. In order to meet the increasing demand to ensure those essential usages, the supply of REEs is however limited from the primary sources. Recovery of REEs from secondary resources, such as discarded electrical and electronic equipment, referred to as electronic waste (e-waste) is consequently crucial. Fluorescent lamps among such wastes are of special concern due to the high quantity of REEs present in them. This article discusses a potential hydrometallurgical method for recovering REEs (yttrium and europium) from fluorescent lamp waste via nitric acid leaching. The effects of leaching factors including acid concentration and temperature were examined. To assist the leaching yields of those metals, the effect of alkaline fusion was specifically examined. The kinetics of both processes, direct- and alkaline fusion-assisted leaching were investigated based on the shrinking core model. In the case of direct leaching, the metal dissolution was controlled by surface chemical reaction with apparent activation energies of 43.9 and 48.1 kJ/mol for yttrium and europium, respectively, in the temperature range 303–333 K. Pretreatment, viz., the alkaline fusion changed the subsequent leaching mechanism to diffusion control with apparent activation energies of 7.4 and 9.5 kJ/mol for the respective metal in the same temperature range. Optimization of the alkaline fusion-assisted acid leaching process was undertaken by applying response surface methodology (RSM) based on the central composite design (CCD). Under the alkaline fusion conditions such as soda/fluorescent powder mass ratio of 0.65 g/g, temperature of 1223 K and reaction time of 7200 s followed by acid leaching (nitric acid concentration – 3.5 M, temperature-323 K, pulp density – 30 g/L and leaching duration – 1200 s), the leaching efficiencies of 92.6% and 99.5% for yttrium and europium, respectively, could be achieved.
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来源期刊
Geosystem Engineering
Geosystem Engineering GEOSCIENCES, MULTIDISCIPLINARY-
CiteScore
2.70
自引率
0.00%
发文量
11
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