Enhanced Leaching of Mn from Electrolytic Manganese Anode Slime via an Electric Field

Author(s):  
Yong Yang ◽  
Jiancheng Shu ◽  
Lei Zhang ◽  
Pengxin Su ◽  
Weile Meng ◽  
...  
Author(s):  
Pengxin Su ◽  
Qiuyue Wan ◽  
Yong Yang ◽  
Jiancheng Shu ◽  
Hongyuan Zhao ◽  
...  

2014 ◽  
Vol 878 ◽  
pp. 163-170 ◽  
Author(s):  
Liang Qu Huang ◽  
Ya Fan Bi ◽  
Lin Lin Mu ◽  
Hong Bo Zhang

Production of electrolytic manganese metal inevitably produces a certain amount of solid wasteelectrolytic manganese anode slime, with a high manganese content, but its difficult to recycle due to the presence of other impurities. Firstly, the washing method was used to remove the anode slime soluble salts, then its chemical composition and phase were analyzed. The flame atomic absorption spectrometer and X-ray fluorescence (XRF) analysis showed the anode slime mainly contained Mn, Pb, Ca, Fe, Cr, K, Se and other metal elements, with the average manganese content 45% and the lead 3.5%;X-ray diffraction (XRD) preliminary analysis showed that the anode slime was a colloidal system mainly containing the spinel structure of MnO2 and complex salts PbMn8O16xH2O phase, by high temperature roasting, the anode slime transformed from hexagonal system to cubic system , and the basic structure unit from edges connection to surfaces connection,the change of length,angle and fracture of manganese-oxygen bond provided the channel for the lead leaching;TG-DTA analysis showed that anode slime was dominated by water loss below 400°C,and started to lose oxygen beyond 425°C, and clear endothermic peak was observed at 500°C and 700°C, which showed the anode slime crystal structure changed at 500°C, anode slime weight loss tending to be gentle with some Mn2O3 generation at 700°C, and roasted crystal stabilizing to Mn2O3. Preliminary roasting and leaching purification technology route was proposed according to the above analysis results, and analysis of the purification process related factors was made. Under the condition of natural ventilation, anode slime was roasted at 700°C, and fully leached in 2mol/L HAc , with liquid-solid ratio 10:1, then leached anode slime was characterized by XRD and flame atomic absorption test, the results showed that anode slime manganese content increased from 45% to 67.5%, the lead content decreased from 3.5% to 0.1%, XRD indicated that the anode slime existing phase was Mn2O3. Anode slime after purification treatment can be further used for battery manganese source material, which provides an effective approach for the recovery of manganese anode slime utilization.


2019 ◽  
Vol 183 ◽  
pp. 98-105 ◽  
Author(s):  
Benjun Wang ◽  
Linlin Mu ◽  
Song Guo ◽  
Yafan Bi

2016 ◽  
Vol 31 ◽  
pp. 683-690 ◽  
Author(s):  
Hongbo Zhang ◽  
Yafan Bi ◽  
Xiongfei Chen ◽  
Liangqu Huang ◽  
Linlin Mu

2017 ◽  
Vol 806 ◽  
pp. 15-21 ◽  
Author(s):  
Jiancheng Shu ◽  
Renlong Liu ◽  
Zuohua Liu ◽  
Haiping Wu ◽  
Yuliang Chen ◽  
...  

2019 ◽  
Vol 236 ◽  
pp. 117708 ◽  
Author(s):  
Yang Tian ◽  
Jiancheng Shu ◽  
Mengjun Chen ◽  
Jianyi Wang ◽  
Yao Wang ◽  
...  

2021 ◽  
Author(s):  
Yong Yang ◽  
Jiancheng Shu ◽  
Pengxin Su ◽  
Haiping Wu ◽  
Lei Zhang ◽  
...  

Abstract Electrolytic manganese anode slime (EMAS) is produced during the production of electrolytic manganese metal. In this study, a method based on vacuum carbothermal reduction was used for Pb removal in EMAS. A Pb-removal efficiency of 99.85% and MnO purity in EMAS of 97.34 wt.% was obtained for a reduction temperature of 950°C and a carbon mass ratio of 10% for a holding time of 100 min. The dense structure of the EMAS was destroyed, a large number of multidimensional pores and cracks were formed, and the Pd-containing compound was reduced to elemental Pb by the vacuum carbothermal reduction. A recovery efficiency for chemical MnO2 of 36.6% was obtained via preparation from Pd-removed EMAS through the “roasting-pickling disproportionation” process, with an acid washing time of 100 min, acid washing temperature of 70°C, H2SO4 concentration of 0.8 mol/L, liquid-solid mass ratio of 7 mL/g, calcination temperature of 60°C and calcination time of 2.5 h. Moreover, the crystal form of the prepared chemical MnO2 was found to be basically the same as that of electrolytic MnO2, and its specific surface area, micropore volume and discharge capacity were all higher than that of electrolytic MnO2. This study provides a new method for Pd removal and recycling for EMAS.


Sign in / Sign up

Export Citation Format

Share Document