Zinc recovery from the effluent of the viscose industry with carboxylic cation exchangers

1971 ◽  
Vol 2 (1) ◽  
pp. 92-93
Author(s):  
V. S. Morgenshtern ◽  
L. N. Matorenok
2021 ◽  
Vol 11 (1) ◽  
Author(s):  
Abdolrahim Foroutan ◽  
Majid Abbas Zadeh Haji Abadi ◽  
Yaser Kianinia ◽  
Mahdi Ghadiri

AbstractCollector type and pulp pH play an important role in the lead–zinc ore flotation process. In the current study, the effect of pulp pH and the collector type parameters on the galena and sphalerite flotation from a complex lead–zinc–iron ore was investigated. The ethyl xanthate and Aero 3418 collectors were used for lead flotation and Aero 3477 and amyl xanthate for zinc flotation. It was found that maximum lead grade could be achieved by using Aero 3418 as collector at pH 8. Also, iron and zinc recoveries and grades were increased in the lead concentrate at lower pH which caused zinc recovery reduction in the zinc concentrate and decrease the lead grade concentrate. Furthermore, the results showed that the maximum zinc grade and recovery of 42.9% and 76.7% were achieved at pH 6 in the presence of Aero 3477 as collector. For both collectors at pH 5, Zinc recovery was increased around 2–3%; however, the iron recovery was also increased at this pH which reduced the zinc concentrate quality. Finally, pH 8 and pH 6 were selected as optimum pH values for lead and zinc flotation circuits, respectively.


2016 ◽  
Vol 119 ◽  
pp. 38-49 ◽  
Author(s):  
Tatiana A. Pozdniakova ◽  
Luciana P. Mazur ◽  
Rui A.R. Boaventura ◽  
Vítor J.P. Vilar

1998 ◽  
Vol 33 (4) ◽  
pp. 467-481 ◽  
Author(s):  
Carmine Colella ◽  
Maurizio De' Gennaro ◽  
Alessio Langella ◽  
Michele Pansini

2016 ◽  
Vol 286 ◽  
pp. 1-15 ◽  
Author(s):  
Maria A.P. Cechinel ◽  
Diego A. Mayer ◽  
Tatiana A. Pozdniakova ◽  
Luciana P. Mazur ◽  
Rui A.R. Boaventura ◽  
...  

1974 ◽  
Vol 12 (10) ◽  
pp. 555-558 ◽  
Author(s):  
R. A. Barford ◽  
L. T. Olszewski ◽  
D. H. Saunders ◽  
P. Magidman ◽  
H. L. Rothbart

Author(s):  
M. Leuchtenmueller ◽  
C. Legerer ◽  
U. Brandner ◽  
J. Antrekowitsch

AbstractEffective recycling of zinc-containing industrial wastes, most importantly electric arc furnace dust, is of tremendous importance for the circular economy of the steel and zinc industry. Herein, we propose a comprehensive kinetic model of the combined carbothermic and metallothermic reduction of zinc oxide in a metal bath process. Pyro-metallurgical, large-scale lab experiments of a carbon-saturated iron melt as reduction agent for a molten zinc oxide slag were performed to determine reaction constants and accurately predict mass transfer coefficients of the proposed kinetic model. An experimentally determined kinetic model demonstrates that various reactions run simultaneously during the reduction of zinc oxide and iron oxide. For the investigated slag composition, the temperature-dependent contribution of the metallothermic zinc oxide reduction was between 25 and 50 pct of the overall reaction mechanism. The mass transfer coefficient of the zinc oxide reduction quadrupled from 1400 °C to 1500 °C. The zinc recovery rate was > 99.9 pct in all experiments.


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