scholarly journals Recovery of rare earths from waste cathode ray tube (CRT) phosphor powder by selective sulfation roasting and water leaching

2019 ◽  
Vol 183 ◽  
pp. 60-70 ◽  
Author(s):  
Mehmet Ali Recai Önal ◽  
Koen Binnemans
2019 ◽  
Vol 95 ◽  
pp. 53-58 ◽  
Author(s):  
L. Alvarado-Hernández ◽  
G.T Lapidus ◽  
Federico González

2016 ◽  
Vol 4 (12) ◽  
pp. 7080-7089 ◽  
Author(s):  
Xiaofei Yin ◽  
Yufeng Wu ◽  
Xiangmiao Tian ◽  
Jiamei Yu ◽  
Yi-Nan Zhang ◽  
...  

2019 ◽  
Vol 74 (2) ◽  
pp. 663-671 ◽  
Author(s):  
E. A. Ajiboye ◽  
E. F. Olasehinde ◽  
A. O. Adebayo ◽  
O. O. Ajayi ◽  
M. K. Ghosh ◽  
...  

2018 ◽  
Vol 119 ◽  
pp. 82-92 ◽  
Author(s):  
Rodolfo Marin Rivera ◽  
Brecht Ulenaers ◽  
Ghania Ounoughene ◽  
Koen Binnemans ◽  
Tom Van Gerven

2020 ◽  
Vol 10 (1) ◽  
Author(s):  
Qiangchao Sun ◽  
Hongwei Cheng ◽  
Xiaoyong Mei ◽  
Yanbo Liu ◽  
Guangshi Li ◽  
...  

2007 ◽  
Vol 561-565 ◽  
pp. 1569-1573 ◽  
Author(s):  
Qi Wu Zhang ◽  
Fumio Saito

As the extension of mineral processing, recycling metals from wastes is very important for a sustainable society. We have been working on mechanochemistry and its engineering applications. One of the applications is to recover and separate useful components from different kinds of wastes emitted in our society. When a waste sample is subjected to grinding in air so called mechanical treatment, it changes its structure to disordered system, resulting in chemical reactions with other substances when it takes over the certain level of energy. Depending on the existing states of target elements in the wastes, mechanical activation and mechanochemical (MC) reaction can be applied for the recycling of useful compositions and a process based on MC treatment has been developed. We will report several examples from our research experiences at the conference. The first example is to recover rare earths from fluorescent powders in waste lamps. The waste is firstly subjected to dry grinding to cause amorphization of their structures. This amorphization makes it possible to dissolve the rare earths from the waste at high yield by leaching with mild acid solution at room temperature. Similar phenomenon can be seen in the case of ITO (indium tin oxide) scrap when it is ground, followed by leaching with acid solution. In this case, dry grinding the scrap induces disordering the In2O3 in the scrap, leading to high dissolution of In2O3 by leaching with weak acid solution at room temperature. The presence of alumina (α-Al2O3) in the scrap plays a significant role to the amorphization. Another advanced waste processing is to recover molybdenum (Mo), vanadium (V) and nickel (Ni) sulphide in catalysts in oil refineries. The processing is based on MC reactions between the sulphides and additives. That is, the sulphides are subjected to dry grinding with additives such as CaO, MnO2 and Na2CO3 to transform them into molybdate and vanadate. Subsequent water leaching allows us to recover Mo and V from the ground product. Other successful example is dry grinding metals or their oxides with polyvinyl chloride (PVC) to transform into chlorides, which dissolve easily in water at ambient condition. The waste processing described above is now in the investigation on industrial applications, and this is a great expectation in the field of industries which emit such waste materials.


JOM ◽  
2019 ◽  
Vol 71 (12) ◽  
pp. 4473-4482 ◽  
Author(s):  
Junjie Shi ◽  
Chao Peng ◽  
Min Chen ◽  
Yun Li ◽  
Hurman Eric ◽  
...  

Abstract Sulfation roasting followed by water leaching has been proposed as an alternative route for recycling valuable metals from spent lithium-ion batteries (LIBs). In the present work, the reaction mechanism of the sulfation roasting of synthetic LiCoO2 was investigated by both thermodynamic calculations and roasting experiments under flowing 10% SO2-1% O2-89% Ar gas atmosphere at 700°C. The products and microstructural evolution processes were characterized by x-ray diffraction, scanning electron microscope and energy dispersive x-ray spectrometer, and atomic absorption spectroscopy. It was confirmed that Co3O4 was formed as an intermedia product, and the final roasted products were composed by Li2SO4, Li2Co(SO4)2, and CoO. The leaching results indicated that 99.5% Li and 17.4% Co could be recovered into water after 120 min of roasting. The present results will provide the basis and solid guidelines for recycling of Li and Co from spent LIBs.


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