Effective separation and recovery of valuable metals from high value-added lead anode slime by sustainable vacuum distillation

2021 ◽  
pp. 128731
Author(s):  
Jiafei Yi ◽  
Guozheng Zha ◽  
Daxin Huang ◽  
Xiangfeng Kong ◽  
Bin Yang ◽  
...  
JOM ◽  
2019 ◽  
Vol 71 (7) ◽  
pp. 2413-2419 ◽  
Author(s):  
Guozheng Zha ◽  
Bin Yang ◽  
Chongfang Yang ◽  
Xinyu Guo ◽  
Wenlong Jiang

Metals ◽  
2021 ◽  
Vol 11 (10) ◽  
pp. 1535
Author(s):  
Zhe Gao ◽  
Xiangfeng Kong ◽  
Jiafei Yi ◽  
Bin Yang ◽  
Baoqiang Xu ◽  
...  

Tellurium is the indispensable base material of semiconductors in solar panels. Traditional tellurium recycling, a highly complicated separation process, has exhausted reagents and energy sources whilst producing waste residue and water containing multitudinous heavy metal that is hugely harmful to the ecological environment. A clean and eco-friendly vacuum distillation-directional condensation treatment was investigated for its potential to recycle tellurium from tellurium-rich lead anode slime (TLAS). The optimal distillation temperature and response time conditions of 1173 K and 50 min were obtained based on a large number of experiments. Gasification results indicated that under the optimal conditions of distillation temperature 1173 K, constant temperature time 50 min, and system pressure 5–15 Pa, 92% of tellurium was volatilized and enriched into the condenser from TLAS. Condensate results revealed that 88% of elemental tellurium was directly recovered in the volatile matter. The appropriate gasification-condensation processes realized a clean utilization to extract tellurium and separate multi valuable metals effectively.


2013 ◽  
Vol 20 (3) ◽  
pp. 615-621 ◽  
Author(s):  
Liang Li ◽  
Yang Tian ◽  
Da-chun Liu ◽  
Hou-jun Zhou ◽  
Yong-nian Dai ◽  
...  

2019 ◽  
Vol 209 ◽  
pp. 863-869 ◽  
Author(s):  
Guozheng Zha ◽  
Chongfang Yang ◽  
Yunke Wang ◽  
Xinyu Guo ◽  
Wenlong Jiang ◽  
...  

2013 ◽  
Vol 813 ◽  
pp. 153-156
Author(s):  
Wen Hua Wu ◽  
Zhi Jian Wang ◽  
Ji Bo Liu

After stacking pre-oxidation treatment, lead anode slime was leached in sulfuric acid added with sodium chloride and oxidant of sodium chlorate. The leaching rates of As, Te, Sb, Bi and Cu are more than 98% with potential controlled at 500mV. And noble metals are left in the residue, which are separated from the base metals effectively. Through cooling and crystallizing out arsenate, the solution is reduced with potential controlled. According to reducing slag, the recovery rate of Te is 96.52%. Sb is recovered by neutralizing hydrolysis and the recovery rate is 95.2%. By the effect of iron powder, As, Bi and Cu are entirely reduced with the recovery rates of Bi and Cu to be 91.56% and 83.49%, respectively. The total recovery of As from the crystalline product and reducing slag achieves 91.56%.


2010 ◽  
Vol 20 (12) ◽  
pp. 2397-2403 ◽  
Author(s):  
Hua-zhen CAO ◽  
Jin-zhong CHEN ◽  
Hai-jun YUAN ◽  
Guo-qu ZHENG
Keyword(s):  

2020 ◽  
Vol 38 (11) ◽  
pp. 1214-1221
Author(s):  
Yuhui Zhang ◽  
Xiaoyan Feng ◽  
Bingjie Jin

Separation of arsenic and valuable metals (Pb, Zn, Cu, Bi, Sn, In, Ag, Sb, etc.) is a core problem for effective utilization of high arsenic-containing copper smelting ashes (HACSA). This study developed an effective separation process of arsenic, lead, and zinc from HACSA via alkali leaching followed by sulfide precipitation. The separation behaviors and optimum conditions for alkali leaching of arsenic and sulfide precipitation of lead and zinc were established respectively as follows: NaOH concentration 3.81 M; temperature 80°C; time 90 minutes; liquid-to-solid ratio 4:1; agitation speed 450 revolutions/minute (r/min) and 2.0 times of theoretical quantity of sodium sulfide (Na2S); temperature 70°C; and time 60 minutes. The results indicated that the leaching rates of As, Pb, and Zn were 92.4%, 36.9% and 13.4%, respectively. More than 99% of lead and zinc were precipitated from the alkali leachate. The scanning electron microscopy/energy dispersive X-ray spectroscopy study confirmed that arsenic was dissolved from HACSA into the alkali leachate. Furthermore, lead and zinc were precipitated as sulfides from the alkali leachate. The proposed process was a good technique for separation of arsenic and enrichment of valuable metals for further centralized treatment separately. It provided high separation efficiency of arsenic and valuable metals, as well as low environmental pollution.


2018 ◽  
Vol 176 ◽  
pp. 26-35 ◽  
Author(s):  
Yongming Chen ◽  
Nannan Liu ◽  
Longgang Ye ◽  
Shan Xiong ◽  
Shenghai Yang

Materials ◽  
2019 ◽  
Vol 12 (10) ◽  
pp. 1625 ◽  
Author(s):  
Ndue Kanari ◽  
Eric Allain ◽  
Seit Shallari ◽  
Frederic Diot ◽  
Sebastien Diliberto ◽  
...  

Development of our modern society requests a number of critical and strategic elements (platinum group metals, In, Ga, Ge…) and high value added elements (Au, Ag, Se, Te, Ni…) which are often concentrated in by-products during the extraction of base metals (Cu, Pb, Zn…). Further, recycling of end-of-life materials employed in high technology, renewable energy and transport by conventional extractive processes also leads to the concentration of such chemical elements and their compounds in metallurgical by-products and/or co-products. One of these materials, copper anode slime (CAS), derived from a copper electrolytic refining factory, was used for this study. The sample was subjected to isothermal treatment from 225 to 770 °C under air atmosphere and the reaction products were systematically analyzed by scanning electron microscopy through energy dispersive spectroscopy (SEM-EDS) and X-ray diffraction (XRD) to investigate the thermal behavior of the treated sample. The main components of the anode slime (CuAgSe, Cu2-xSeyS1-y, Ag3AuSe2) react with oxygen, producing mostly copper and selenium oxides as well as Ag-Au alloys as final products at temperatures higher than 500 °C. Selenium dioxide (SeO2) is volatilized and recovered in pure state by cooling the gaseous phase, whilst copper(II) oxide, silver, gold and tellurium remain in the treatment residue.


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