Lead Sulfate Scale in a Copper Smelter Acid Plant

Author(s):  
J. M. Rapkoch
2014 ◽  
Vol 16 (12) ◽  
pp. 2734-2741 ◽  
Author(s):  
Giancarlo M. Barassi ◽  
Martin Klimsa ◽  
Thomas Borrmann ◽  
Mathew J. Cairns ◽  
Joachim Kinkel ◽  
...  

Suspended solids in weak acid waste from a copper smelter have been identified to be anglesite, lead sulphate, nano- and microparticles. The particles bypass filters and could pose a serious environmental threat.


2021 ◽  
pp. 35-42
Author(s):  
A. S. Sharipova ◽  
K. A. Linnik ◽  
A. N. Zagorodnyaya ◽  
N. Bakhytuly

This paper examines the process of selenium precipitation from the slime generated by the sulphuric acid plant of the Balkhash Copper Smelter. Contrary to similar tailings generated by non-ferrous metals industry, such slime has a high concentration of selenium (12.5–4.6 wt. %). By utilizing it in the production process, one can raise the output of selenium by more than 30% compared with the amount of selenium recovered by the smelter from copper anode slimes. The slime that was used in the experiments had been separated from the slurry produced as a result of scrubbing of metallurgical gases generated by copper smelting and matte converting processes. The slime was rinsed with water to remove sulphuric acid from it and then dried at 105 oC. With the help of new-generation analytical equipment, the slime was analyzed for qualitative, quantitative and material compositions. 15 elements with significantly varying concentrations were detected. The main components include lead (51.17 wt. %) and selenium (12.49 wt. %), which are present in the form of lead sulphates and elemental selenium. Other lead and mercury compounds are also present as disseminations – i.e. different salts of selenium acids. Considering the forms in which lead and selenium are mainly found in the slime, lead was initially converted into carbonates by sodium carbonate leaching, and then nitric acid was used to make lead transfer from the cake into the solution. The authors looked at the effect produced by the sodium carbonate concentration (50–200 g/dm3), solid-to-liquid ratio (1:(2–6)), process duration (20–120 min) and temperature (20–70 oC) at constant slime feed and stirrer RPM on the behaviour of lead and selenium. Optimum conditions were identified in which both elements almost completely remain in the carbonate cake, and only 0.019% Pb and 0.17% Se get extracted into the solution. Different quantities of three carbonate-containing compounds of lead and seven selenium compounds were found in the cake. When the carbonate cake is leached with nitric acid, almost all of the lead transfer to the solution, while selenium remains in the cake as an elementary substance and mercury selenides. As compared with the slime, the concentration of selenium in the cake increased by 5.6 times. This research was funded by the Science Board of the Ministry of Science and Education of the Republic of Kazakhstan under the following programme: Development and Implementation of Innovative Technology Ensuring a Higher Recovery of Non-Ferrous, Noble, Rare and Rare Earth Metals, as well as Fulfillment of Production Targets by Industrial Companies of the Republic of Kazakhstan Set for 2018–2020.


2020 ◽  
Vol 20 (4) ◽  
Author(s):  
Bartosz Mikoda ◽  
Anna Potysz ◽  
Harry Kucha ◽  
Ewa Kmiecik

Abstract Spent catalysts being considered hazardous wastes exhibit a high metal content in mobile forms. In addition, growing demand for circular economy policy applications requires proper utilization of these wastes. This study aimed at the assessment of vanadium leaching from spent desulfurization catalyst derived from sulfuric acid plant dump located nearby a copper smelter. Chemical and phase composition of the catalyst has been characterized. The extraction has been performed using chemical (0.1-M and 1-M citric acid) and biological (biotic solution with Acidithiobacillus thiooxidans) methods, using different experimental parameters (pulp density, particle size, leaching time) to observe V leaching behavior and kinetics. The results revealed that both citric acid and bacteria carried out the extraction process well. The optimal parameters for acid leaching were < 0.2-mm particle size and 2% pulp density, which allowed to leach out 95% of V from spent catalyst within 48 h. The bacterially mediated extraction resulted in 93% V leached out within 21 days with 2% pulp density. The experiments showed that V present in the catalyst is susceptible to bioleaching and organic acid leaching with the latter being a quicker process.


2018 ◽  
Vol 122 ◽  
pp. 122-129 ◽  
Author(s):  
Eduardo Balladares ◽  
O. Jerez ◽  
F. Parada ◽  
L. Baltierra ◽  
C. Hernández ◽  
...  

2021 ◽  
Vol 413 ◽  
pp. 125365
Author(s):  
Jianrong Xue ◽  
Dongping Long ◽  
Hong Zhong ◽  
Shuai Wang ◽  
Lihua Liu

Author(s):  
Humberto Aponte ◽  
Pedro Mondaca ◽  
Christian Santander ◽  
Sebastián Meier ◽  
Jorge Paolini ◽  
...  

2021 ◽  
Vol 296 ◽  
pp. 126512
Author(s):  
Lin Chen ◽  
Peng Chen ◽  
Zhenhu Wang ◽  
Weifeng Liu ◽  
Duchao Zhang ◽  
...  

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